WO2012002004A1 - Water purifier - Google Patents
Water purifier Download PDFInfo
- Publication number
- WO2012002004A1 WO2012002004A1 PCT/JP2011/055115 JP2011055115W WO2012002004A1 WO 2012002004 A1 WO2012002004 A1 WO 2012002004A1 JP 2011055115 W JP2011055115 W JP 2011055115W WO 2012002004 A1 WO2012002004 A1 WO 2012002004A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- activated carbon
- carbon layer
- water
- filter
- case
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 386
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 677
- 239000012528 membrane Substances 0.000 claims abstract description 73
- 239000012510 hollow fiber Substances 0.000 claims abstract description 68
- 238000000746 purification Methods 0.000 claims abstract description 66
- 239000008213 purified water Substances 0.000 claims abstract description 39
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 17
- 239000002245 particle Substances 0.000 claims description 37
- 239000000919 ceramic Substances 0.000 claims description 33
- 230000002093 peripheral effect Effects 0.000 claims description 27
- 238000001914 filtration Methods 0.000 claims description 15
- 238000004891 communication Methods 0.000 claims description 12
- 230000000844 anti-bacterial effect Effects 0.000 claims description 8
- 125000006850 spacer group Chemical group 0.000 claims description 6
- 239000010419 fine particle Substances 0.000 claims description 5
- 230000004308 accommodation Effects 0.000 claims description 4
- 239000013014 purified material Substances 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 description 24
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 23
- 239000000460 chlorine Substances 0.000 description 23
- 229910052801 chlorine Inorganic materials 0.000 description 23
- 239000008399 tap water Substances 0.000 description 18
- 235000020679 tap water Nutrition 0.000 description 18
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 17
- 230000000052 comparative effect Effects 0.000 description 14
- 239000013618 particulate matter Substances 0.000 description 11
- 230000002829 reductive effect Effects 0.000 description 11
- 230000007423 decrease Effects 0.000 description 7
- 235000012215 calcium aluminium silicate Nutrition 0.000 description 6
- 239000000404 calcium aluminium silicate Substances 0.000 description 6
- WNCYAPRTYDMSFP-UHFFFAOYSA-N calcium aluminosilicate Chemical compound [Al+3].[Al+3].[Ca+2].[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O WNCYAPRTYDMSFP-UHFFFAOYSA-N 0.000 description 6
- 229940078583 calcium aluminosilicate Drugs 0.000 description 6
- 239000011148 porous material Substances 0.000 description 6
- 239000008239 natural water Substances 0.000 description 5
- 239000005909 Kieselgur Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
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- 238000010586 diagram Methods 0.000 description 3
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
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- 150000002500 ions Chemical class 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000003566 sealing material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- -1 trihalomethane Chemical compound 0.000 description 2
- 239000010456 wollastonite Substances 0.000 description 2
- 229910052882 wollastonite Inorganic materials 0.000 description 2
- DQCMWCVJSOFDSA-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl.CC(Cl)(Cl)Cl DQCMWCVJSOFDSA-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
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- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000011538 cleaning material Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
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Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2055—Carbonaceous material
- B01D39/2058—Carbonaceous material the material being particulate
- B01D39/2062—Bonded, e.g. activated carbon blocks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2068—Other inorganic materials, e.g. ceramics
- B01D39/2072—Other inorganic materials, e.g. ceramics the material being particulate or granular
- B01D39/2075—Other inorganic materials, e.g. ceramics the material being particulate or granular sintered or bonded by inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
- C02F9/20—Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/065—More than one layer present in the filtering material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/006—Cartridges
Definitions
- the present invention relates to a water purifier for purifying tap water through a purifying material, and more particularly to a device characterized by technical means for improving purification performance.
- Tap water may contain various particles such as red rust and other turbid components, residual chlorine, agricultural chemicals, lead and other harmful components.
- harmful trihalomethane produced by the reaction of chlorine and organic substances in tap water and other harmful trichloroethane (1,1,1-trichloroethane) mixed in the river also enter the tap water and are contained therein. Sometimes it is. Therefore, conventionally, tap water is generally used after being purified through a water purifier.
- the tap water (raw water) is passed through the purification material inside the water purifier and becomes purified water by the purification action of the purification material and flows out of the water purification device.
- activated carbon granular activated carbon
- a hollow fiber membrane filter removes solids such as particles contained in tap water and other turbid components and floc (aggregated particles) from tap water by filtration.
- the hollow fiber membrane has innumerable fine pores (through-holes), and tap water can pass from the outside to the inside of the membrane through these pores. Turbid component particles (water particles) are filtered and removed from the tap water.
- the pores of the hollow fiber membrane are extremely fine, and particles of turbid components such as particulate matter contained in tap water can be removed by this hollow fiber membrane filter to as small as about 0.1 ⁇ m.
- an activated carbon layer (activated carbon layer) is disposed on the upstream side, and a hollow fiber membrane filter is disposed on the downstream side.
- the raw water flowing in from the raw water inlet is first passed through an activated carbon layer as shown in the schematic diagram of FIG. 11, where residual chlorine, trihalomethane, trichloroethane and the like in tap water are removed by an adsorption reaction, and then hollow.
- the turbid component particles are removed by filtration, and the raw water (tap water) is purified and the purified water is discharged from the purified water outlet.
- this type of water purifier is disclosed in Patent Literature 1 and Patent Literature 2 below.
- the activated carbon layer on the upstream side not only removes harmful components dissolved in the raw water by adsorption, but also the activated carbon layer has a large turbidity substance. Is also removed, clogging of the downstream hollow fiber membrane filter is reduced, and the service life is extended.
- the hollow fiber membrane filter not only removes particulate matter in the raw water, but also prevents the activated carbon (granular) from flowing upstream, and the invasion of germs into the water purifier from the purified water outlet, that is, preventing back contamination of germs. Can play multiple functions and roles at the same time. As a result, this type of water purifier has been widely used as an excellent balance between compactness and long life.
- trihalomethane and trichloroethane which are harder to adsorb than residual chlorine, can be removed together with residual chlorine in tap water in the activated carbon layer at the beginning, trihalomethane and trichloroethane are removed by the activated carbon layer due to a decrease in adsorption performance as they continue to be used. There is a possibility that these may be included in the purified water flowing out of the water purifier.
- the upstream activated carbon layer removes particulate matter that is the cause of clogging of the hollow fiber membrane filter, clogging of the downstream hollow fiber membrane filter is suppressed, resulting in clogging of the hollow fiber membrane filter.
- the durability life is extended.
- Patent Document 3 discloses this type of water purifier.
- residual chlorine and various harmful chemical substances contained in the raw water (tap water) directly act on the hollow fiber membrane located upstream, thereby accelerating the deterioration of the hollow fiber membrane and reducing the filtration accuracy. Is a problem.
- the activated carbon layer preferentially adsorbs residual chlorine in tap water that is more easily adsorbed than other substances, thereby inhibiting the adsorption of trihalomethane and trichloroethane, which are relatively difficult to adsorb, and the activated carbon layer inhibits these trihalomethanes and trichloroethane.
- trihalomethane, trichloroethane, etc. are partially contained in the purified water and are discharged from the water purifier without being sufficiently removed.
- the present invention has been made for the purpose of providing a water purifier having high purification performance for raw water and capable of maintaining high purification performance for a long period of time against the background as described above.
- 1st invention of this invention accommodates a purification material in the inside of the case provided with the raw
- the water purifier that flows out from the raw water, as the purification material, the first activated carbon layer from the upstream side to the downstream side of the flow of the raw water flowing in from the raw water inlet, and the raw water is removed through the raw water through the formed through-holes to remove underwater particles.
- the filter is arranged in the order of the filter and the second activated carbon layer, and the raw water is purified by passing through the first activated carbon layer, the filter and the second activated carbon layer in this order.
- the case is formed in a cylindrical shape, and the first activated carbon layer is disposed in a cylindrical accommodating space on the outer peripheral side of the inner space of the case.
- the filter and the second activated carbon layer are disposed in the central portion inside the first activated carbon layer in the space in the case, and the filter is disposed downstream of the first activated carbon layer.
- the second activated carbon layer was arranged in the axial direction at a position adjacent to the side portion in the radial direction and the upstream side portion of the first activated carbon layer in the radial direction, and flowed from the raw water inlet. After the raw water is circulated in the axial direction inside the first activated carbon layer, the raw water passes through the filter and flows into and through the second activated carbon layer to be purified, and purified water is discharged from the purified water outlet. It is characterized by.
- the case in any one of the first and second aspects, includes a cylindrical case body having a bottom portion at one end in the axial direction and an opening at the other end.
- the opening is closed in a state of being axially divided into a cover body that is assembled to the case body in the axial direction, and the cover body is assembled to the case body so that the filter inside the case
- the activated carbon layer is restrained and fixed in the axial direction by the bottom and the lid.
- the second activated carbon layer is provided in a cylindrical shape, and the second activated carbon layer has a filter side.
- a cap is attached to the end of the filter, and the cap is provided with a plurality of legs as spacer portions that protrude from the outer periphery to the filter side at a plurality of locations in the circumferential direction and abut against the axial end surface of the filter.
- the leg is characterized in that a gap for water passage is formed between the filter side and the second activated carbon layer side in the axial direction.
- an outer peripheral side of the second activated carbon layer is provided with an activated carbon case for accommodating the second activated carbon layer therein, and an outer periphery of the cap.
- the projecting portion is provided with a plurality of projecting portions projecting radially outward and in contact with the inner peripheral surface of the activated carbon case at a plurality of locations in the circumferential direction, and the projecting portions are provided with the leg portions.
- the end of the second activated carbon layer is fixed in a radial position relative to the activated carbon case by contacting the activated carbon case with the activated carbon case, and the activated carbon case and the second activated carbon layer An annular water passage space is formed between them, and a communication passage for communicating the water passage space and the gap is formed between the protrusion and the protrusion.
- a cylindrical ceramic filter made of a porous sintered body is communicated with the purified water outlet at the center of the second activated carbon layer. It is provided as a support member for the second activated carbon layer in a state, and the second activated carbon layer and the ceramic filter perform purification by passing water in a radial direction.
- the ceramic filter has antibacterial properties.
- the filter is capable of filtering to fine particles of 0.1 ⁇ m.
- the filter is a hollow fiber membrane filter.
- the tenth invention of the present invention is a case having a raw water inlet and a purified water outlet, and a first activated carbon layer disposed in a position closer to the raw water inlet than the purified water outlet in the case, Inside the case, a second activated carbon layer disposed closer to the water purification outlet than the raw water inlet, and a filter disposed between the first activated carbon layer and the second activated carbon layer. It is a water purifier equipped with.
- the first activated carbon layer has a hollow shape
- the second activated carbon layer and the filter are disposed inside the hollow shape. It is characterized by that.
- the second surface on the opposite side of the first surface and the first surface is between the second activated carbon layer and the filter.
- a cap having a surface the first surface supports the second activated carbon layer
- the second surface has a leg, and the leg contacts the end of the filter.
- a gap for water passage is formed between the second activated carbon layer and the filter.
- this invention arrange
- natural water which flowed in the inside of a water purifier flows first through a 1st activated carbon layer.
- residual chlorine contained in the raw water is removed by adsorption by the first activated carbon layer. Accordingly, residual chlorine in the raw water can be prevented from acting on the filter disposed on the downstream side.
- the ninth invention even when a hollow fiber membrane filter is used as the filter (the ninth invention), the residual chlorine in the raw water is transferred to the hollow fiber membrane as in the conventional water purifier in which the hollow fiber membrane filter is disposed on the most upstream side. It is possible to solve the problem of acting to accelerate the deterioration and lowering the filtration accuracy by the hollow fiber membrane filter. That is, the filtration accuracy by the hollow fiber membrane filter can be maintained with high accuracy.
- the raw water flowing through the first activated carbon layer is passed through a filter, and turbid particles such as contaminants in the raw water are removed by the filtering action of the filter.
- the second activated carbon layer passes through the filter and passes through raw water from which turbid particles such as particles are removed, and removes harmful components contained in the raw water by adsorption.
- the second activated carbon layer is originally The maximum purification performance can be achieved.
- trihalomethane, trichloroethane, and the like contained in the raw water are removed by adsorption even in the first activated carbon layer in the initial stage of use of the water purifier.
- the activated carbon surface of the first activated carbon layer is covered with particulate matter and the adsorption capacity is lowered, and further, the adsorption performance for trihalomethane and trichloroethane having a weak adsorption force is lowered due to adsorption of residual chlorine. To do. For this reason, components such as trihalomethane and trichloroethane are not completely removed by the first activated carbon layer, but they pass downstream and flow downstream.
- the second activated carbon layer is provided further downstream of the filter, trihalomethane and trichloroethane that could not be removed by the first activated carbon layer are adsorbed well by the second activated carbon layer and removed from the raw water. can do.
- the present invention removes harmful components dissolved in the raw water by sharing the roles of the first activated carbon layer in the former stage and the second activated carbon layer in the latter stage.
- the water purifier of the present invention exhibits high purification performance from the beginning of use and can maintain the high purification performance over a long period of time.
- the second activated carbon layer maintains high purification performance for a long period of time, normally, before the purification performance of the second activated carbon layer deteriorates, the filter in the previous stage is clogged, and the water purifier The flow rate of water flowing through is reduced. Therefore, when a user uses a water purifier with a decrease in the flow rate due to clogging of the water purifier as a guideline for the service life, the water purifier is not clogged even though the purifying performance has deteriorated. It is possible to prevent the user from continuing to use it as it is.
- a second activated carbon layer is provided on the downstream side of the filter, and in this case, granular activated carbon is used as the activated carbon, and if this is simply filled in the accommodating portion as in the conventional case, the activated carbon flows out.
- granular activated carbon is used as the activated carbon, and if this is simply filled in the accommodating portion as in the conventional case, the activated carbon flows out.
- the case is formed into a cylindrical shape according to the second invention, and the first activated carbon layer is disposed in the axial direction along the inner peripheral surface of the case in the cylindrical accommodating space on the outer peripheral side of the case inner space.
- the filter and the second activated carbon layer are disposed in the central portion inside the first activated carbon layer in the space in the case, the filter is positioned adjacent to the downstream portion of the first activated carbon layer in the radial direction, and The second activated carbon layer is arranged side by side in the axial direction so as to be positioned radially adjacent to the upstream side portion of the first activated carbon layer.
- the raw water flowing in from the raw water inlet is circulated in the first activated carbon layer in the axial direction, the raw water passes through the filter and flows into and through the second activated carbon layer for purification, and the purified water flows out from the purified water outlet.
- the distance through which the raw water passes through the purification material can be increased within a limited size case (the contact time can be increased), and the purification capacity can be improved while reducing the size of the water purifier. Can be increased.
- capacitance of a 1st activated carbon layer can be enlarged by arrange
- the above case is assembled in the axial direction to the case main body in such a manner that the case main body has a bottom portion at one end in the axial direction and an opening at the other end, and the opening is closed.
- the filter and the second activated carbon layer inside the case are restrained and fixed in the axial direction by the bottom portion and the lid body.
- the number of parts for fixing the filter and the second activated carbon layer can be reduced, contributing to the downsizing and cost reduction of the water purifier, and the filter and the second activated carbon. Easy assembly of the layers.
- the second activated carbon layer is provided in a cylindrical shape according to the fourth aspect of the present invention.
- a cap is attached to the end of the second activated carbon layer on the filter side, and the spacer protrudes from the outer periphery to the filter side at a plurality of locations in the circumferential direction and contacts the axial end surface of the filter.
- a plurality of legs are provided. With the legs, a gap for passing water can be formed between the filter side and the second activated carbon layer side in the axial direction.
- the gap is formed by the legs provided in the cap, a special spacer member for forming the gap is not required separately, and the number of required parts can be reduced.
- the outer peripheral portion of the cap is provided with a plurality of projecting portions projecting radially outward and in contact with the inner peripheral surface of the activated carbon case at a plurality of locations in the circumferential direction.
- the end of the second activated carbon layer is fixed to the activated carbon case in a radially positioned state by the abutment of the plurality of protrusions to the activated carbon case, and an annular shape is provided between the activated carbon case and the second activated carbon layer.
- a communication passage that forms a water flow space and connects the water flow space and the gap is formed between the protrusion and the protrusion.
- the cap attached to the end of the second activated carbon layer can fix the end of the second activated carbon layer with respect to the activated carbon case in the radial direction.
- An annular water passage space can be formed between the two activated carbon layers. Further, the water passage space and the gap between the filter side and the second activated carbon layer side can be communicated through a communication path formed between the protrusions.
- water that has flowed out of the filter is first allowed to flow into the gap between the filter side and the second activated carbon layer, and further introduced into the annular water flow space around the second activated carbon layer through the communication path. Can do. Moreover, by doing in this way, the water from a filter can be smoothly introduce
- the end of the second activated carbon layer is fixed to the activated carbon case, the annular water passage space around the second activated carbon layer is formed, and the communication path between the gap and the water passage space is formed.
- a cylindrical ceramic filter made of a porous sintered body is provided at the center of the second activated carbon layer as a water-permeable support member for the second activated carbon layer, and the second activated carbon layer. And purification can be performed by passing water in the radial direction through the ceramic filter (sixth invention).
- the second activated carbon layer is formed of molded activated carbon, it is possible to make the molded activated carbon difficult to break due to the function as a support member of the ceramic filter.
- the ceramic filter can have antibacterial properties (seventh invention). In this way, it is possible to effectively prevent back-contamination where germs enter the inside from the outside of the water purifier through the water purification outlet.
- a hollow fiber membrane filter can be suitably used as the filter (the ninth invention), but a ceramic filter made of a porous sintered body can also be used. According to this configuration, a ceramic filter that can be filtered to fine particles of 0.1 ⁇ m can be suitably used.
- granular activated carbon can be used suitably as a 1st activated carbon layer and a 2nd activated carbon layer
- fibrous activated carbon and others can also be used.
- granular activated carbon those having a particle size (average particle size) in the range of 0.05 to 1.0 mm can be suitably used.
- This particle size range is an appropriate particle size range with low pressure loss during water passage and excellent purification performance.
- FIG. 1 is a view showing a water purifier according to an embodiment of the present invention together with an automatic faucet.
- (A) in FIG. 2 is a cross-sectional view showing the water purifier in FIG. 2B is a perspective view of the lower plate 90.
- FIG. (A) and (B) in FIG. 3 are the principal part enlarged views of the water purifier. It is the figure which decomposed
- (A) and (B) in FIG. 5 are perspective views of a lid and an upper plate in the water purifier.
- (A), (B), and (C) in FIG. 6 are views showing a lower cap in the water purifier.
- FIG. 7 are the figures which expressed by comparing the water purifier of this embodiment, and the water purifier of a comparative example.
- FIG. 8 are diagrams showing the water purification performance of the water purifier of this embodiment in comparison with a comparative example. It is the figure which showed the principal part of other embodiment of this invention. It is the figure which showed other embodiment of this invention. It is the schematic diagram which showed the example of arrangement
- FIG. 1 1 is a sink installed in the kitchen
- 2 is a cabinet
- 3 is a sink
- 10 is a counter
- 11 is an automatic faucet installed on the sink 1 and having a purified water discharge function.
- the automatic faucet 11 includes a base body 12 provided in a form standing from the counter 10 and a water discharge pipe 14 extending from the body 12.
- the water discharge pipe 14 is rotatable by a predetermined angle with respect to the main body 12.
- the main body 12 is provided with a single lever 16 at a position eccentric to the right side of the water discharge pipe 14 in a front view as viewed from the user.
- the single lever 16 adjusts the flow rate and temperature of the discharged water. Specifically, the temperature of the water discharge is adjusted by rotating the single lever 16 in the horizontal direction in the drawing, and the flow rate is adjusted by rotating the single lever 16 up and down.
- the water discharge pipe 14 has a substantially U-shaped gooseneck shape, and has a shape curved downward from a substantially intermediate portion in the tube axis direction to the tip portion.
- the water discharge pipe 14 has a water discharge port 18 at the tip, a water discharge head 22 that can be pulled out together with the flexible hose 20, and a water discharge head holder that holds the water discharge head 22 in the storage position.
- a water discharge pipe main body 24 having the function as described above.
- the main body portion 12 is connected to the upper ends of the water supply passage 26 and the hot water supply passage 28, and water and hot water are supplied to the main body portion 12 through the water supply passage 26 and the hot water supply passage 28.
- a mixing valve (not shown) is incorporated in the main body 12, and an outflow path 32 extends from the mixing valve. Through the outflow path 32, temperature control water (by mixing the single lever 16, In some cases, the temperature control water in which water and hot water are mixed at a predetermined ratio may consist of only water or hot water (hereinafter referred to as raw water).
- the hose 20 has an outflow path 32 formed inside thereof.
- a raw water valve (electromagnetic valve) 34 for opening and closing the outlet passage 32 is provided on the outflow passage 32.
- the operation of the raw water valve 34 is controlled by a controller (not shown).
- a water purification path 38 branches out from the water supply path 26 and extends, and the tip of the water purification path 38 is connected to the outflow path 32 at the downstream portion of the raw water valve 34.
- a water purifier 40 (electromagnetic valve) 42 for opening and closing the water purifier 40 and the water purifying path 38 is provided on the water purifying path 38.
- the operation of the water purification valve 42 is also controlled by a controller.
- 46 is a water stop cock.
- the raw water sensor 60 and the water purification sensor 58 are provided on the upper surface of the distal end portion of the water discharge pipe 14, specifically, on the upper surface of the uppermost portion of the substantially intermediate portion in the tube axis direction of the water discharge pipe 14. Are arranged side by side in the pipe axis direction.
- the raw water sensor 60 is an alternate sensor that alternately discharges raw water (temperature-controlled water) from the water outlet 18 and stops the water every time the inserted hand is detected.
- the raw water sensor 60 detects the hand in a non-contact manner, discharges the raw water from the spout 18 based on the detection, and then the raw water sensor 60 removes the hand. The raw water continues to be discharged even if the water is drawn. Then, when the raw water sensor 60 is operated again by extending the hand, that is, when the raw water sensor 60 detects the hand, the discharge of the raw water from the spout 18 is stopped.
- the water purification sensor 58 also alternately discharges purified water from the water outlet 18 and stops water discharge (stops water) every time a hand is detected (every human body is detected).
- the raw water sensor 60 is disposed on the front side and the lower side near the user, and the water purification sensor 58 is disposed on the far side and the upper side farther than the raw water sensor 60.
- reference numeral 41 denotes a metal bracket that holds the water purifier 40 inside the cabinet 2 and fixes it to the inner surface of the side wall 43 of the cabinet 2.
- Each of the hoses 38A and 38B forms a part of the water purification path 38 therein.
- the hose 38A guides the inflow path for allowing the raw water to flow into the water purifier 40 in the water purification path 38
- the hose 38B guides the purified water after being purified by the water purifier 40 to the spout 18 side. It forms an outlet for purified water.
- the pair of hoses 38 ⁇ / b> A and 38 ⁇ / b> B are fixed to the inner surface of the side wall portion 43 of the cabinet by a fixing portion 52.
- the internal structure of the water purifier 40 is specifically shown in (A) and (B) in FIG.
- 62 is a cylindrical case with both ends in the axial direction closed.
- This case 62 has a case body 66 having a bottom 64 at one end in the axial direction and an opening at the other end, and the opening is closed. In such a state, it is divided in the axial direction into a lid body 68 that is assembled to the case main body 66 in the axial direction.
- the lid 68 integrally has a circular and plate-like closing portion 69 and a cylindrical portion 70, and a male screw portion 72 on the outer peripheral surface of the case main body 66 at a female screw portion 72 on the inner peripheral surface of the cylindrical portion 70. 74 is screwed together.
- the case body 66 and the lid body 68 are sealed watertight by a sealing material.
- the closing portion 69 of the lid 68 is integrally provided with a raw water inlet 76 at a position eccentric from the center and a purified water outlet 78 at the center.
- the raw water inlet 76 and the purified water outlet 78 are provided so as to protrude from the closing portion 69.
- the hose 38A is connected to the raw water inlet 76
- the hose 38B is connected to the purified water outlet 78.
- a cylindrical filter case 80 for accommodating a hollow fiber membrane filter 130 to be described later and a cylindrical activated carbon case 82 for accommodating a second activated carbon layer to be described later are axially connected to each other.
- the filter case 80 and the activated carbon case 82 divide the inner space of the case 62 into an outer peripheral side portion and a central portion.
- a cylindrical housing space 84 that forms an outer peripheral side portion of the space in the case 62 is filled with activated carbon (here, granular activated carbon) 86-1, and the activated carbon 86-1 forms a first activated carbon layer 88.
- the accommodation space 84 that is, the first activated carbon layer 88 is a nonwoven fabric in which one end in the axial direction (lower end in the figure) is defined by the lower plate 90 as a partition plate and the other end (upper end in the figure) forms an activated carbon presser. 92.
- the granular activated carbon forming the first activated carbon layer 88 one having a particle diameter (average particle diameter) of 0.1 to 1.0 mm can be suitably used. If the particle size is smaller than 0.1 mm, the particle size is too small, the filling rate of the activated carbon 86-1 becomes too high, and the pressure resistance during water passage becomes high, making it difficult for water to flow. On the other hand, if the particle diameter is more than 1.0 mm, the particle diameter is too large, the surface area of the entire activated carbon becomes small, and the adsorption efficiency is lowered.
- a rib 94 is provided in an upright state at the bottom 64 of the case body 66, and the lower plate 90 is supported by the rib 94 from below.
- the lower plate 90 forms a water passing space 96 between the lower side, that is, the bottom 64.
- the lower plate 90 has a through-opening 98 on the outer peripheral side of the filter case 80, and the water passage space 96 and the accommodation space 84 are communicated with each other through the opening 98.
- the lower plate 90 further has a through-opening 100 inside and at the center of the filter case 80, and the water passage space 96 communicates with the inside of the filter case 80 through the opening 100.
- a projecting portion 102 having a circular ring shape is provided on the upper surface side of the lower plate 90 in the drawing, and a lower end of the filter case 80 in the drawing is fitted to the protruding portion 102 in the drawing.
- the lower end of the filter case 80 is positioned and fixed with respect to the lower plate 90, that is, the case 62 in a state where the filter case 80 is supported from the lower side by the lower plate 90.
- a circular upper plate 104 as a presser is arranged on the lid body 68 side.
- the upper plate 104 has an annular and circular protruding portion 106 standing upward in the figure, and this protruding portion 106 is an inner surface of the closing portion 69 (see FIG. It is fitted in a groove 108 formed in the middle and lower surface.
- the lid 68 is screwed downward with respect to the case main body 66, the force is transmitted to the upper plate 104, and the nonwoven fabric 92 serving as an activated carbon presser is pressed downward in the figure by the upper plate 104. .
- the upper plate 104 is provided with a through opening 110.
- the raw water flowing in from the raw water inlet 76 passes through the opening 110 of the upper plate 104 and flows into the first activated carbon layer 88.
- a radial rib 112 protruding downward from the closing portion 69 and a circular rib 114 are provided on the back surface of the lid 68.
- the circular rib 114 is a radial rib.
- the height of the downward protrusion in the figure is lower than that of the rib 112, and the groove 108 is formed by the step.
- a fitting portion 116 is provided at the lower end portion of the activated carbon case 82 in the drawing, and the fitting portion 116 is fitted to the upper end portion of the filter case 80 in the drawing state.
- the upper end portion of the filter case 80 and the lower end portion of the activated carbon case 82 are connected in the axial direction, that is, in the vertical direction in the figure, while being positioned in the radial direction.
- the filter case 80 and the activated carbon case 82 are sealed in a watertight manner by a sealing material.
- a lower cap 118 and an upper cap 120 are provided at a lower end portion and an upper end portion of a second activated carbon layer 132 to be described later, respectively.
- the upper cap 120 is provided with a first fitting portion 122 at a radially outer position and a second fitting portion 124 at an inner position.
- the 1st fitting part 122 is fitted by the upper end part of the activated carbon case 82 in the external fitting state.
- the upper end part of the activated carbon case 82 is positioned by radial direction by the fitting.
- the upper end of the activated carbon case 82 is fitted upward in the figure inside a circular annular groove formed between the first fitting portion 122 and the second fitting portion 124, and activated carbon
- the upper end portion of the case 82 is positioned in the radial direction.
- a cylindrical male fitting portion 126 is provided upward, and the male fitting portion 126 protrudes into the case of the water purification outlet 78.
- the portion 128 is fitted in a watertight manner.
- the hollow fiber membrane filter 130 is in the lower side in the figure, and the second activated carbon layer 132 having a cylindrical shape is in the figure. It is housed in a state located on the upper side.
- the hollow fiber membrane filter 130 is located at a position adjacent in the radial direction to the downstream portion (portion located on the downstream side of the raw water flow) in the first activated carbon layer 88, and the second activated carbon layer 132 is the first activated carbon layer 132.
- the upstream portion portion located upstream of the flow of raw water
- they are arranged side by side in the central accommodation space in the axial direction. .
- innumerable fine pores are formed in the hollow fiber membrane, and the raw water can pass from the outside to the inside of the membrane through these pores. Solids containing fine particles are filtered off.
- the pores of the hollow fiber membrane are extremely fine, and the hollow fiber membrane filter 130 removes even small ones of about 0.1 ⁇ m contained in the raw water by filtration.
- the second activated carbon layer 132 is composed of molded activated carbon obtained by previously molding granular activated carbon 86-2 into a cylindrical shape.
- the granular activated carbon 86-2 forming the second activated carbon layer 132 one having a smaller particle diameter than the activated carbon 86-1 forming the first activated carbon layer 88 can be used.
- granular activated carbon 86-1 forming the first activated carbon layer 88 having a particle diameter of 0.15 mm to 0.30 mm is used, and granular activated carbon 86-2 forming the second activated carbon layer 132 is used as the particle diameter. Having a thickness of 0.05 mm to 0.15 mm can be used.
- activated carbon 86-2 and activated carbon 86-1 may have the same particle size.
- a cylindrical ceramic filter 136 made of a porous sintered body allows water permeability to the second activated carbon layer 132 in a state where the inside thereof communicates with the water purification outlet 78. It is provided as a support member.
- the ceramic filter 136 can remove particles up to a size of 0.5 ⁇ m by filtration.
- Diatomaceous earth 138 is integrally laminated on the outer peripheral surface of the ceramic filter 136 over almost the entire surface. Here, the diatomaceous earth 138 is baked on the ceramic filter 136.
- the ceramic filter 136 has antibacterial properties.
- the ceramic filter 136 is made of a porous sintered body of calcium aluminosilicate. Specifically, it is composed of a porous sintered body of calcium aluminosilicate having a composition of SiO 2 : 75 to 85%, Al 2 O 3 : 5 to 10%, and CaO: 10 to 20% in terms of mass%. When it adheres or is immersed in water, it releases antibacterial effects by gradually releasing Ca 2+ ions as antibacterial components.
- This calcium aluminosilicate is obtained by blending siliceous wax, limestone, and clay such that SiO 2 , Al 2 O 3 , and CaO have the above ratios, and firing and sintering the mixture.
- the calcium aluminosilicate having this composition effectively produces a large amount of ⁇ -wollastonite (CaO ⁇ SiO 2 ) by firing.
- This ⁇ -wollastonite gradually dissolves Ca 2+ ions over a long period of time to form a weakly alkaline state, thereby acting as an antibacterial.
- the calcium aluminosilicate having this composition is known (disclosed in Japanese Patent No. 3612766), and in the present invention, the one disclosed in Japanese Patent No. 3612766 can be suitably used. Since this calcium aluminosilicate is a known one disclosed in the patent, further detailed explanation is omitted here.
- the upper and lower ends of the ceramic filter 136 in the figure protrude from the second activated carbon layer 132 in a minute dimension upward and downward.
- the upper end of the upper cap 120 is fitted into the male fitting portion 126. Further, the lower end portion is fitted into a fitting hole 140 (see (A) to (C) in FIG. 6) in the center of the lower cap 118 described later.
- the lower cap 118 is water-impermeable (this also applies to the upper cap 120, the filter case 80, and the activated carbon case 82), and the main body as shown in FIGS. 6A to 6C. And a circular rising portion 142 that rises upward in the drawing along the outer peripheral portion thereof.
- the lower cap 118 is attached to the end of the second activated carbon layer 132 so that the lower end of the second activated carbon layer 132 is fitted inside the rising portion 142.
- the lower cap 118 is provided with projecting portions 144 projecting radially outward at four locations separated by 90 ° in the circumferential direction. These projecting portions 144 are shown in FIG.
- the activated carbon case 82 is in contact with the inner peripheral surface.
- the lower cap 118 is fixed to the activated carbon case 82, that is, the lower end portion of the second activated carbon layer 132 in the figure is fixed in a radial position relative to the activated carbon case 82.
- an annular and circular water passage space 148 is formed around the second activated carbon layer 132 between the activated carbon case 82 and the second activated carbon layer 132 by the abutment of the protrusions 144 on the activated carbon case 82. Has been.
- protruding portions 144 are provided with legs 146 as spacer portions that protrude downward and come into contact with the upper surface of the hollow fiber membrane filter 130, and by the contact of the legs 146, the hollow fiber membrane filter 130 side is provided.
- a gap 150 for passing water is formed between the lower cap 118, that is, between the second activated carbon layer 132 side. Further, the gap 150 and the annular water passage 148 communicate with each other between the protrusions 144 and 144 by the protrusion 144. That is, the water flowing out of the hollow fiber membrane filter 130 can flow into the water flow space 148 through the communication path 152 shown in FIG. 3B between the gap 150 and the protrusions 144 and 144. .
- the second activated carbon layer 132 and the ceramic filter 136 perform purification by passing raw water in the radial direction.
- the upper end portion of the second activated carbon layer 132 is fitted into the second fitting portion 124 of the upper cap 120, whereby the upper end portion of the second activated carbon layer 132 is the plate-like portion of the upper cap 120.
- the lid 68 is attached to the case body 66 in a state where the hollow fiber membrane filter 130 and the second activated carbon layer 132 are set in the center of the case body 66 together with the filter case 80 and the activated carbon case 82.
- the lid body 68 of the case main body 66 via the lower plate 90 and the upper plate 104 to be in a fixed state. Become. That is, it is in an assembled state with respect to the case 62.
- the raw water flowing from the raw water inlet 76 first passes through the first activated carbon layer 88 in the axial direction, and then passes through the opening 98 of the lower plate 90 and passes through the lower plate 90. It flows out into the water space 96.
- the raw water that has flowed into the water flow space 96 passes through the opening 100 at the center of the lower plate 90, flows into the filter case 80, flows through the hollow fiber membrane from the outside to the inside, and then flows through the hollow fiber membrane. It flows out to the gap 150 between the upper end of 130 and the second activated carbon layer 132, specifically, the lower cap 118 attached to the lower end portion thereof. Further, it passes through the communication passage 152 shown in FIG.
- the raw water that has flowed into the water purifier 40 first flows through the first activated carbon layer 88, and the residual chlorine contained in the raw water at this time is the first activated carbon layer. It is removed by adsorption by 88. Accordingly, it is possible to prevent residual chlorine in the raw water from acting on the hollow fiber membrane filter 160 disposed on the downstream side.
- the residual chlorine in the raw water acts on the hollow fiber membrane and accelerates its deterioration as in the conventional water purifier 40A in which the hollow fiber membrane filter 130A is arranged on the most upstream side, and the filtration accuracy by the hollow fiber membrane filter 130A is reduced.
- the problem of damaging can be solved, and the filtration accuracy by the hollow fiber membrane filter 130A can be maintained with high accuracy.
- the raw water flowing through the first activated carbon layer 88 is passed through the hollow fiber membrane filter 130, and turbid particles such as particles in the raw water are removed by the filtration action of the hollow fiber membrane filter 130. Remove.
- the second activated carbon layer 132 passes through the hollow fiber membrane filter 130 and passes the raw water from which turbid particles such as particulate matter are removed, and removes harmful components contained in the raw water by adsorption.
- the raw water flowing to the second activated carbon layer 132 contains no particulate matter, and the surface of the activated carbon 86-2 is not covered by the adhesion of the particulate matter.
- the activated carbon layer 132 can maximize the original purification performance.
- the second activated carbon layer 132 adsorbs trihalomethane or trichloroethane. Are not inhibited by residual chlorine and their harmful components are well adsorbed and removed from the raw water.
- trihalomethane, trichloroethane, and the like contained in the raw water are removed by adsorption in the first activated carbon layer 88 in the initial stage of use of the water purifier 40, but if the use of the water purifier 40 is used for a long time, the first The surface of the activated carbon 86-1 of the activated carbon layer 88 is covered with particles to reduce the adsorption capacity, and further, the adsorption performance for trihalomethane and trichloroethane having a weak adsorption force due to the adsorption of residual chlorine decreases.
- Components such as trichloroethane are not completely removed by the first activated carbon layer 88, but they flow downstream through the hollow fiber membrane filter 130 at the subsequent stage.
- the second activated carbon layer 132 is provided further downstream of the hollow fiber membrane filter 130, trihalomethane and trichloroethane that cannot be removed by the first activated carbon layer 88 are removed by the second activated carbon layer 132. Adsorbs well and can be removed from raw water.
- the first activated carbon layer 88 in the former stage and the second activated carbon layer 132 in the latter stage each share a role and remove harmful components dissolved in the raw water.
- the water purifier 40 according to the present embodiment exhibits a high purification performance from the beginning of use, and can maintain the high purification performance over a long period of time.
- the hollow fiber membrane filter 130 in the preceding stage is usually clogged before the purification performance of the second activated carbon layer 132 decreases.
- the flow rate of water flowing through the water purifier 40 is reduced. Accordingly, when the user uses the water purifier 40 with the decrease in the flow rate due to the clogging of the water purifier 40 as a guide for the life, the clogging is not caused even though the purifying performance is lowered. It is possible to prevent the device 40 from being used as it is.
- the second activated carbon layer 132 molded activated carbon obtained by solidifying granular activated carbon 86-2 with an adhesive or the like is used. In this case, the entire second activated carbon layer 132 is maintained in a cylindrical shape. This eliminates the need for the holding member and reduces the number of parts for holding the shape.
- a cylindrical ceramic filter 136 is disposed as a support member at the center of the second activated carbon layer 132, the second activated carbon layer 132 made of molded activated carbon can be prevented from being broken on the center side. Even if a part of the filter collapses, the ceramic filter 136 can prevent the ceramic filter 136 from flowing out of the water purifier 40.
- the case 62 has a cylindrical shape
- the first activated carbon layer 88 is disposed in the axial direction along the inner peripheral surface of the case 62 in a portion on the outer peripheral side of the inner space of the case 62.
- the hollow fiber membrane filter 130 and the second activated carbon layer 132 are disposed in the central portion inside the first activated carbon layer 88, and the hollow fiber membrane filter 130 is adjacent to the downstream portion of the first activated carbon layer 88 in the radial direction.
- the second activated carbon layer 132 is arranged in the axial direction so that the second activated carbon layer 132 is positioned adjacent to the upstream side portion of the first activated carbon layer 88 in the radial direction.
- the flow is folded back in the vicinity of the bottom 64 to flow into the hollow fiber membrane filter 130, and pass through this to pass through the second Life Since it purifies by flowing in and through the coal bed 132 and purifies the purified water through the purified water outlet 78, the distance through which the raw water passes through the purification material in the case 62 of a limited size is increased ( The contact time can be lengthened), and the purification capacity can be enhanced while making the water purifier 40 compact.
- the capacity of the first activated carbon layer 88 can be increased.
- the axial length can be increased, and the residual chlorine removal performance by the first activated carbon layer 88 can be maintained for a long time.
- the lid body 68 is assembled to the case body 66, so that the hollow fiber membrane filter 130 and the second activated carbon layer 132 inside the case 62 are axially restrained and fixed by the bottom portion 64 and the lid body 68. Therefore, the number of parts for fixing the hollow fiber membrane filter 130 and the second activated carbon layer 132 can be reduced, contributing to the downsizing and cost reduction of the water purifier 40 and the hollow fiber membranes.
- the filter 130 and the second activated carbon layer 132 can be easily assembled.
- the lower cap 118 is attached to the end of the second activated carbon layer 132 provided in a cylindrical shape on the hollow fiber membrane filter 130 side, and a plurality of legs 146 are provided on the lower cap 118. 146, a water passage gap 150 is formed between the hollow fiber membrane filter 130 side and the second activated carbon layer 132 side. Therefore, a special spacer member for forming the gap 150 is required separately. The required number of parts can be reduced.
- the end portions of the second activated carbon layer 132 are fixed to the activated carbon case 82 in a radially positioned state by the plurality of protrusions 144 provided on the lower cap 118, and the activated carbon case 82, the second activated carbon layer 132, An annular water passage space 148 is formed between the projection portion 144 and the projection portion 144, and a communication passage 152 that connects the water passage space 148 and the gap 150 is formed.
- the end of the second activated carbon layer 132 is fixed to the activated carbon case 82, the annular water passage space 148 around the second activated carbon layer 132 is formed, and the communication path 152 between the gap 150 and the water passage space 148 is formed. Therefore, a special member is not required separately, and the number of parts can be reduced.
- the water flowing out from the hollow fiber membrane filter 130 is allowed to flow into the gap 150, and further introduced into the annular water passage space 148 around the second activated carbon layer 132 through the communication path 152.
- Water from the hollow fiber membrane filter 130 can be smoothly introduced into the annular water passage space 148 around the second activated carbon layer 132 without increasing the pressure resistance against the outflow of water from the hollow fiber membrane filter 130.
- the ceramic filter 136 at the end of the flow that forms the support member of the second activated carbon layer 132 has antibacterial properties, it is effective for back-contamination in which bacteria enter the inside through the water purification outlet 78 from the outside of the water purifier 40. Can be prevented.
- Example> A comparative test of water purification performance was performed using the water purifier 40 of the above embodiment and the water purifier 40A of the comparative example shown in FIG.
- the water purifier 40 shown in FIG. 7 (A) is the same as the water purifier shown in FIGS. 2 to 6, and is shown in FIG. 7 (A) for comparison with the water purifier of Comparative Example 40A. It is a thing.
- the water purifier 40A of the comparative example shown in FIG. 7B the arrangement of the hollow fiber membrane filter 130A, the second activated carbon layer 132A, and the ceramic filter 136A is the water purifier 40 of this embodiment, that is, FIG. 7A. It is upside down with the water purifier 40 shown. Further, in the water purifier 40A of the comparative example, the water that has passed through the first activated carbon layer 88A passes through the through water passage hole provided in the lower part of the non-permeable activated carbon case 82A in the drawing, and the inner annular water passage space 148A. It is the structure which flows into. In this test, the water purifier 40 of the present embodiment sets the amount of activated carbon in the first activated carbon layer 88 to 350 cc and the amount of activated carbon in the second activated carbon layer 132 to 90 cc.
- the activated carbon amount of the first activated carbon layer 88A is 350 cc
- the activated carbon amount of the second activated carbon layer 132A is 90 cc. That is, the amount of activated carbon is the same in this embodiment and in the comparative example, and the arrangement differs between the two.
- the raw water flowing in from the raw water inlet 76A first passes through the first activated carbon layer 88A in the axial direction, and then the second activated carbon layer 132A and its center. Part of the ceramic filter 136A, and then passes through the hollow fiber membrane filter 130A disposed on the upper side in the drawing, and flows out from the purified water outlet 78A.
- the granular activated carbon in the first activated carbon layer 88 and the second activated carbon layer 132 is the same having a particle size distribution of 0.15 mm to 0.30 mm.
- the hollow fiber membrane has a membrane area of 0.75 m 2 .
- the activated carbon having the same particle size as that of the present embodiment is used. The thing of the form was used.
- FIG. 8 The result is shown in FIG. Among these, (A) in FIG. 8 is a result at the time of using the water purifier 40 of this embodiment, (B) in FIG. 8 is a result at the time of using the water purifier 40A of a comparative example. In addition, about what used the water purifier 40A of the comparative example, the test was performed 3 times about the same thing, and each result is shown.
- the total trihalomethane removal rate is slightly over 80% at the time of the accumulated flow rate of the raw water of 10000L, and the time until it reaches 10000L.
- the removal rate is not high enough.
- the total trihalomethane removal rate rapidly decreases when the integrated flow rate exceeds 12000 L.
- the raw water inlet 76 and the purified water outlet 78 are provided at the same axial end of the case 62.
- the hose can be connected to the case 62 on the same axial side, although the hose can be easily routed and the hose can be prevented from occupying a large space inside the cabinet 2 shown in FIG. 1, the present invention can provide advantages such as the raw water inlet 76 and the purified water outlet 78.
- a check valve 160 for preventing a backflow is provided at the raw water inlet 76, and when the raw water flows from the raw water inlet 76, the check valve 160 is opened to prevent a reverse flow. By closing the check valve 160, it is possible to prevent the water inside the water purifier 40 from flowing out from the raw water inlet 76.
- connection error of reverse connection such as connecting the hose 38A to be connected to the raw water inlet 76 to the purified water outlet 78 by mistake, and connecting the hose 38B to be connected to the purified water outlet 78 to the raw water inlet 76 is avoided. Can be prevented.
- this invention can also comprise a water purifier with various forms other than an example.
- FIG. 10 shows an example.
- the amount of protrusion of the female fitting portion 128 into the case is made larger than that shown in FIG. 2A, and the sponge 162 is sandwiched between the upper cap 120 and the upper plate 104.
- a cylindrical rib 164 is raised from the bottom 64 of the case 62 at a position on the outer peripheral side of the filter case 80 so as to be higher than the rib 94 shown in FIG.
- Rectangular cutouts 166 are provided at a plurality of locations in the circumferential direction, and water that has flowed downward from the opening 98 in the figure is moved radially inward through the cutouts 166.
- the height of the first activated carbon layer 88, the second activated carbon layer 132, the ceramic filter 136 and the diatomaceous earth 138 is set lower than that shown in FIG. 2A, and the thickness of the diatomaceous earth 138 is further illustrated. 2 is thicker than that shown in (A), and its outer diameter is increased.
- fibrous activated carbon or the like as the activated carbon.
- a filter disposed between the first and second activated carbon layers not only the hollow fiber membrane filter but also ceramics. It is also possible to use a filter. However, in this case, it is preferable to use a ceramic filter capable of removing even small particles of 0.1 ⁇ m.
- this invention can be comprised in the form which added the various change in the range which does not deviate from the meaning.
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Abstract
A water purifier which has high performance in purifying raw water and which can maintain the high performance over an extended period of time. A water purifier (40) is configured in such a manner that a purification material is contained within a case (62) provided with a raw water inlet (76) and a purified water outlet (78), raw water which flows from the raw water inlet (76) into the water purifier (40) is caused to pass through the purification material to purify the raw water, and the purified water is allowed to flow out of the purified water outlet (78). The purification material is formed by arranging in order, from the upstream side to the downstream side of the raw water which flows from the raw water inlet (76) into the water purifier (40), a first activated carbon layer (88), a hollow fiber membrane filter (130), and a second activated carbon layer (132). The raw water is purified by being caused to pass through the first activated carbon layer (88), the hollow fiber membrane filter (130), and the second activated carbon layer (132) in that order.
Description
この発明は水道水を浄化材に通して浄化する浄水器に関し、詳しくは浄化性能の向上のための技術手段に特徴を有するものに関する。
The present invention relates to a water purifier for purifying tap water through a purifying material, and more particularly to a device characterized by technical means for improving purification performance.
水道水中には赤錆等各種の粒子物やその他の濁りの元となる成分や、残留塩素,農薬,鉛その他有害成分が含まれていることがある。
また水道水中の塩素と有機物質との反応によって生成する有害なトリハロメタンや、その他に河川に混入していた有害なトリクロロエタン(1,1,1-トリクロロエタン)が水道水にも入り込んで、そこに含まれていることもある。
そこで従来、水道水を浄水器に通して浄化した後で使用することが広く一般に行われている。
水道水(原水)は浄水器内部の浄化材に通され、浄化材による浄化作用で浄水となって浄水器から流出する。 Tap water may contain various particles such as red rust and other turbid components, residual chlorine, agricultural chemicals, lead and other harmful components.
In addition, harmful trihalomethane produced by the reaction of chlorine and organic substances in tap water and other harmful trichloroethane (1,1,1-trichloroethane) mixed in the river also enter the tap water and are contained therein. Sometimes it is.
Therefore, conventionally, tap water is generally used after being purified through a water purifier.
The tap water (raw water) is passed through the purification material inside the water purifier and becomes purified water by the purification action of the purification material and flows out of the water purification device.
また水道水中の塩素と有機物質との反応によって生成する有害なトリハロメタンや、その他に河川に混入していた有害なトリクロロエタン(1,1,1-トリクロロエタン)が水道水にも入り込んで、そこに含まれていることもある。
そこで従来、水道水を浄水器に通して浄化した後で使用することが広く一般に行われている。
水道水(原水)は浄水器内部の浄化材に通され、浄化材による浄化作用で浄水となって浄水器から流出する。 Tap water may contain various particles such as red rust and other turbid components, residual chlorine, agricultural chemicals, lead and other harmful components.
In addition, harmful trihalomethane produced by the reaction of chlorine and organic substances in tap water and other harmful trichloroethane (1,1,1-trichloroethane) mixed in the river also enter the tap water and are contained therein. Sometimes it is.
Therefore, conventionally, tap water is generally used after being purified through a water purifier.
The tap water (raw water) is passed through the purification material inside the water purifier and becomes purified water by the purification action of the purification material and flows out of the water purification device.
従来、かかる浄水器では浄化材として活性炭(粒状活性炭)と中空糸膜フィルタとが併用して用いられている。
活性炭は主として吸着作用で水道水に溶存している残留塩素やトリハロメタン,トリクロロエタン等を除去する。
また中空糸膜フィルタは、水道水中に含まれている粒子物やその他濁りの元となる成分の粒子やフロック(粒子が凝集したもの)等の固形分を濾過作用により水道水から除去する。 Conventionally, in such a water purifier, activated carbon (granular activated carbon) and a hollow fiber membrane filter are used in combination as a purification material.
Activated carbon removes residual chlorine, trihalomethane, trichloroethane, etc. dissolved in tap water mainly by adsorption.
In addition, the hollow fiber membrane filter removes solids such as particles contained in tap water and other turbid components and floc (aggregated particles) from tap water by filtration.
活性炭は主として吸着作用で水道水に溶存している残留塩素やトリハロメタン,トリクロロエタン等を除去する。
また中空糸膜フィルタは、水道水中に含まれている粒子物やその他濁りの元となる成分の粒子やフロック(粒子が凝集したもの)等の固形分を濾過作用により水道水から除去する。 Conventionally, in such a water purifier, activated carbon (granular activated carbon) and a hollow fiber membrane filter are used in combination as a purification material.
Activated carbon removes residual chlorine, trihalomethane, trichloroethane, etc. dissolved in tap water mainly by adsorption.
In addition, the hollow fiber membrane filter removes solids such as particles contained in tap water and other turbid components and floc (aggregated particles) from tap water by filtration.
中空糸膜には微細な細孔(貫通孔)が無数に形成されており、水道水はこれら細孔を通過して膜の外から内側へと通過可能で、その際に水道水中に含まれる濁り成分の粒子(水中粒子)が濾過されて水道水から除去される。
中空糸膜の細孔は極めて微細なもので、水道水中に含まれている粒子物等の濁り成分の粒子は0.1μm程度の小さなものまでこの中空糸膜フィルタにて除去可能である。 The hollow fiber membrane has innumerable fine pores (through-holes), and tap water can pass from the outside to the inside of the membrane through these pores. Turbid component particles (water particles) are filtered and removed from the tap water.
The pores of the hollow fiber membrane are extremely fine, and particles of turbid components such as particulate matter contained in tap water can be removed by this hollow fiber membrane filter to as small as about 0.1 μm.
中空糸膜の細孔は極めて微細なもので、水道水中に含まれている粒子物等の濁り成分の粒子は0.1μm程度の小さなものまでこの中空糸膜フィルタにて除去可能である。 The hollow fiber membrane has innumerable fine pores (through-holes), and tap water can pass from the outside to the inside of the membrane through these pores. Turbid component particles (water particles) are filtered and removed from the tap water.
The pores of the hollow fiber membrane are extremely fine, and particles of turbid components such as particulate matter contained in tap water can be removed by this hollow fiber membrane filter to as small as about 0.1 μm.
これら活性炭,中空糸膜フィルタを浄化材として用いた浄水器では、従来、上流側に活性炭の層(活性炭層)が配置され、下流側に中空糸膜フィルタが配置されている。そして、原水入口から流入した原水を、図11の模式図に示しているように先ず活性炭層に通して、そこで吸着反応により水道水中の残留塩素やトリハロメタン,トリクロロエタン等を除去し、そしてその後に中空糸膜フィルタを通過させることで、そこで濁り成分の粒子を濾過作用にて除去し、原水(水道水)を浄化して浄水出口から浄水を流出させる。
例えばこの形態の浄水器は下記特許文献1,特許文献2に開示されている。 In water purifiers using these activated carbon and hollow fiber membrane filters as purification materials, conventionally, an activated carbon layer (activated carbon layer) is disposed on the upstream side, and a hollow fiber membrane filter is disposed on the downstream side. The raw water flowing in from the raw water inlet is first passed through an activated carbon layer as shown in the schematic diagram of FIG. 11, where residual chlorine, trihalomethane, trichloroethane and the like in tap water are removed by an adsorption reaction, and then hollow. By passing through the thread membrane filter, the turbid component particles are removed by filtration, and the raw water (tap water) is purified and the purified water is discharged from the purified water outlet.
For example, this type of water purifier is disclosed inPatent Literature 1 and Patent Literature 2 below.
例えばこの形態の浄水器は下記特許文献1,特許文献2に開示されている。 In water purifiers using these activated carbon and hollow fiber membrane filters as purification materials, conventionally, an activated carbon layer (activated carbon layer) is disposed on the upstream side, and a hollow fiber membrane filter is disposed on the downstream side. The raw water flowing in from the raw water inlet is first passed through an activated carbon layer as shown in the schematic diagram of FIG. 11, where residual chlorine, trihalomethane, trichloroethane and the like in tap water are removed by an adsorption reaction, and then hollow. By passing through the thread membrane filter, the turbid component particles are removed by filtration, and the raw water (tap water) is purified and the purified water is discharged from the purified water outlet.
For example, this type of water purifier is disclosed in
このように活性炭層,中空糸膜フィルタの順に浄化材を配置した浄水器では、上流側の活性炭層が単に吸着によって原水中に溶存する有害成分を除去するだけでなく、活性炭層が大きな濁り物質をも除去し、下流側の中空糸膜フィルタの目詰まりを軽減し、長寿命化する。
Thus, in the water purifier in which the purification material is arranged in the order of the activated carbon layer and the hollow fiber membrane filter, the activated carbon layer on the upstream side not only removes harmful components dissolved in the raw water by adsorption, but also the activated carbon layer has a large turbidity substance. Is also removed, clogging of the downstream hollow fiber membrane filter is reduced, and the service life is extended.
また中空糸膜フィルタは、原水中の粒子物の除去だけでなく、上流側の活性炭(粒状)の流出防止や、浄水出口側からの雑菌の浄水器内部への侵入、即ち雑菌の逆汚染防止といった複数の機能,役割を同時に担うことができる。
その結果、この形態の浄水器はコンパクトさと長寿命のバランスに優れたものとして従来広く普及していた。 The hollow fiber membrane filter not only removes particulate matter in the raw water, but also prevents the activated carbon (granular) from flowing upstream, and the invasion of germs into the water purifier from the purified water outlet, that is, preventing back contamination of germs. Can play multiple functions and roles at the same time.
As a result, this type of water purifier has been widely used as an excellent balance between compactness and long life.
その結果、この形態の浄水器はコンパクトさと長寿命のバランスに優れたものとして従来広く普及していた。 The hollow fiber membrane filter not only removes particulate matter in the raw water, but also prevents the activated carbon (granular) from flowing upstream, and the invasion of germs into the water purifier from the purified water outlet, that is, preventing back contamination of germs. Can play multiple functions and roles at the same time.
As a result, this type of water purifier has been widely used as an excellent balance between compactness and long life.
しかしながら、このように上流側に活性炭層が配置され、また下流側に中空糸膜フィルタが配置された浄水器では、鉄錆やほこり等の濁り成分や、浄水場で水中の懸濁粒子を沈降させるために添加された凝集剤(凝集剤として添加されたポリ塩化アルミニウムに由来するアルミ系凝集剤)のフロック等の粒子物が多数含まれた水質レベルの低い過酷な海外の水道水に対しては、活性炭の表面がこれらの夾雑物によって被覆され、表面での吸着或いは酸化反応が阻害されるため、浄化性能を十分に発揮することができない。
However, in the water purifier in which the activated carbon layer is arranged on the upstream side and the hollow fiber membrane filter is arranged on the downstream side, turbid components such as iron rust and dust, and suspended particles in water at the water purification plant are settled. For harsh overseas tap water with low water quality, which contains a large number of floc particles such as flocs of flocculant added to make it (aluminum flocculant derived from polyaluminum chloride added as flocculant) Since the surface of activated carbon is covered with these impurities and the adsorption or oxidation reaction on the surface is inhibited, the purification performance cannot be sufficiently exhibited.
そのため初期には活性炭層で水道水中の残留塩素とともに、残留塩素に比べて吸着し難いトリハロメタンやトリクロロエタンを除去できたとしても、使用を続けるうちに吸着性能の低下によってトリハロメタンやトリクロロエタンを活性炭層で除去し切れず、これらが浄水器から流出する浄水に含まれてしまう可能性がある。
Therefore, even if trihalomethane and trichloroethane, which are harder to adsorb than residual chlorine, can be removed together with residual chlorine in tap water in the activated carbon layer at the beginning, trihalomethane and trichloroethane are removed by the activated carbon layer due to a decrease in adsorption performance as they continue to be used. There is a possibility that these may be included in the purified water flowing out of the water purifier.
加えて、上流側の活性炭層が中空糸膜フィルタの目詰まり原因物質である粒子物を除去するため、下流側の中空糸膜フィルタの目詰まりが抑制され、結果として中空糸膜フィルタの目詰まり耐久寿命が長くなる。
In addition, since the upstream activated carbon layer removes particulate matter that is the cause of clogging of the hollow fiber membrane filter, clogging of the downstream hollow fiber membrane filter is suppressed, resulting in clogging of the hollow fiber membrane filter. The durability life is extended.
一般ユーザーは、通常、浄水器が目詰まりして流量が少なくなるまで使い続けることが多い。この場合、活性炭層による浄化性能が十分に発揮されないままの状態で長期間に亘って浄水器が使用されてしまう可能性がある。
General users usually continue to use until the water purifier is clogged and the flow rate is reduced. In this case, there is a possibility that the water purifier may be used for a long time in a state where the purification performance by the activated carbon layer is not sufficiently exhibited.
こうした問題を解決することを目的として、上流側に中空糸膜フィルタが配置され、下流側に活性炭層が配置された浄水器も提案されている。例えば下記特許文献3にこの種の浄水器が開示されている。
しかしながら、この構造では、原水(水道水)に含まれる残留塩素や各種有害化学物質が上流側に位置する中空糸膜に直接作用して、中空糸膜の劣化を早め、濾過精度を低下させてしまうことが問題となる。 In order to solve these problems, a water purifier in which a hollow fiber membrane filter is disposed on the upstream side and an activated carbon layer is disposed on the downstream side has been proposed. For example,Patent Document 3 below discloses this type of water purifier.
However, in this structure, residual chlorine and various harmful chemical substances contained in the raw water (tap water) directly act on the hollow fiber membrane located upstream, thereby accelerating the deterioration of the hollow fiber membrane and reducing the filtration accuracy. Is a problem.
しかしながら、この構造では、原水(水道水)に含まれる残留塩素や各種有害化学物質が上流側に位置する中空糸膜に直接作用して、中空糸膜の劣化を早め、濾過精度を低下させてしまうことが問題となる。 In order to solve these problems, a water purifier in which a hollow fiber membrane filter is disposed on the upstream side and an activated carbon layer is disposed on the downstream side has been proposed. For example,
However, in this structure, residual chlorine and various harmful chemical substances contained in the raw water (tap water) directly act on the hollow fiber membrane located upstream, thereby accelerating the deterioration of the hollow fiber membrane and reducing the filtration accuracy. Is a problem.
また、この浄水器の場合、中空糸膜フィルタによって粒子物が除去された後の原水が活性炭層に流入して来るため、活性炭表面が粒子物等にて覆われるといった問題は生じない。しかしながら、活性炭層では他の物質より吸着され易い水道水中の残留塩素が優先的に吸着されることによって、相対的に吸着され難いトリハロメタンやトリクロロエタン等の吸着が阻害され、活性炭層でこれらトリハロメタンやトリクロロエタンを十分に除去し切れずに、トリハロメタン,トリクロロエタン等が一部浄水に含まれて浄水器から流出してしまう可能性がある。
Further, in the case of this water purifier, since the raw water after the particulate matter is removed by the hollow fiber membrane filter flows into the activated carbon layer, the problem that the activated carbon surface is covered with the particulate matter does not occur. However, the activated carbon layer preferentially adsorbs residual chlorine in tap water that is more easily adsorbed than other substances, thereby inhibiting the adsorption of trihalomethane and trichloroethane, which are relatively difficult to adsorb, and the activated carbon layer inhibits these trihalomethanes and trichloroethane. There is a possibility that trihalomethane, trichloroethane, etc. are partially contained in the purified water and are discharged from the water purifier without being sufficiently removed.
本発明は以上のような事情を背景とし、原水に対する浄化性能が高く且つ高い浄化性能を長期間維持することのできる浄水器を提供することを目的としてなされたものである。
The present invention has been made for the purpose of providing a water purifier having high purification performance for raw water and capable of maintaining high purification performance for a long period of time against the background as described above.
本発明の第1の発明は、原水入口と浄水出口とを備えたケースの内部に浄化材を収容し、該原水入口から流入した原水を該浄化材に通して浄化し、浄水を該浄水出口から流出させる浄水器において、前記浄化材として、前記原水入口から流入した原水の流れの上流側から下流側に第1の活性炭層,分散形成された貫通孔に原水を通して濾過作用により水中粒子を除去するフィルタ,第2の活性炭層の順序で配置し、原水を該第1の活性炭層,フィルタ,第2の活性炭層の順に通して浄化することを特徴とする。
1st invention of this invention accommodates a purification material in the inside of the case provided with the raw | natural water inlet and the purified water outlet, purifies | cleans the raw | natural water which flowed in from this raw | natural water inlet through this purification | cleaning material, and cleans water to this purified water outlet In the water purifier that flows out from the raw water, as the purification material, the first activated carbon layer from the upstream side to the downstream side of the flow of the raw water flowing in from the raw water inlet, and the raw water is removed through the raw water through the formed through-holes to remove underwater particles. The filter is arranged in the order of the filter and the second activated carbon layer, and the raw water is purified by passing through the first activated carbon layer, the filter and the second activated carbon layer in this order.
本発明の第2の発明は、第1の発明において、前記ケースを筒状となして、ケース内空間の外周側の筒状の収容空間に前記第1の活性炭層を該ケースの内周面に沿って軸方向に配置するとともに、該ケース内空間の該第1の活性炭層の内側の中央部に前記フィルタと前記第2の活性炭層とを、該フィルタを該第1の活性炭層における下流側部分に対し径方向に隣接する位置に、また第2の活性炭層を第1の活性炭層における上流側部分に対し径方向に隣接する位置に軸方向に並べて配置し、前記原水入口から流入した原水を前記第1の活性炭層の内部を軸方向に流通移動させた後、前記フィルタを通過して前記第2の活性炭層に流入及び通過させて浄化し、浄水を前記浄水出口から流出させることを特徴とする。
According to a second aspect of the present invention, in the first aspect, the case is formed in a cylindrical shape, and the first activated carbon layer is disposed in a cylindrical accommodating space on the outer peripheral side of the inner space of the case. The filter and the second activated carbon layer are disposed in the central portion inside the first activated carbon layer in the space in the case, and the filter is disposed downstream of the first activated carbon layer. The second activated carbon layer was arranged in the axial direction at a position adjacent to the side portion in the radial direction and the upstream side portion of the first activated carbon layer in the radial direction, and flowed from the raw water inlet. After the raw water is circulated in the axial direction inside the first activated carbon layer, the raw water passes through the filter and flows into and through the second activated carbon layer to be purified, and purified water is discharged from the purified water outlet. It is characterized by.
本発明の第3の発明は、第1の発明と第2の発明の何れか一つにおいて、前記ケースは、軸方向一端側に底部を、他端側に開口を有する筒状のケース本体と、該開口を閉鎖する状態に該ケース本体に軸方向に組み付けられる蓋体とに軸方向に分割してあり、該ケース本体に該蓋体を組み付けることで、該ケースの内部の前記フィルタと第2の活性炭層とを前記底部と蓋体とで軸方向に拘束し固定することを特徴とする。
According to a third aspect of the present invention, in any one of the first and second aspects, the case includes a cylindrical case body having a bottom portion at one end in the axial direction and an opening at the other end. The opening is closed in a state of being axially divided into a cover body that is assembled to the case body in the axial direction, and the cover body is assembled to the case body so that the filter inside the case The activated carbon layer is restrained and fixed in the axial direction by the bottom and the lid.
本発明の第4の発明は、第1の発明~第3の発明の何れか一つにおいて、前記第2の活性炭層が筒状に設けてあって、該第2の活性炭層の前記フィルタ側の端部にキャップが装着してあり、該キャップには周方向の複数個所で外周部から該フィルタ側に突出して該フィルタの軸方向の端面に当接するスペーサ部としての複数の脚が設けてあって、該脚により、軸方向において該フィルタ側と前記第2の活性炭層側との間に通水用の間隙が形成してあることを特徴とする。
According to a fourth aspect of the present invention, in any one of the first to third aspects, the second activated carbon layer is provided in a cylindrical shape, and the second activated carbon layer has a filter side. A cap is attached to the end of the filter, and the cap is provided with a plurality of legs as spacer portions that protrude from the outer periphery to the filter side at a plurality of locations in the circumferential direction and abut against the axial end surface of the filter. The leg is characterized in that a gap for water passage is formed between the filter side and the second activated carbon layer side in the axial direction.
本発明の第5の発明は、第4の発明において、前記第2の活性炭層の外周側には、該第2の活性炭層を内部に収容する活性炭ケースが設けてあるとともに、前記キャップの外周部には径方向外方に突出して該活性炭ケースの内周面に当接する突出部が周方向の複数個所に設けてあって、該突出部に前記脚部が設けてあり、該複数の突出部の前記活性炭ケースへの当接により、前記第2の活性炭層の前記端部を該活性炭ケースに対し径方向に位置決状態に固定するとともに、該活性炭ケースと該第2の活性炭層との間に環状の通水空間を形成し、且つ該通水空間と前記間隙とを連通させる連通路を該突出部と突出部との間に形成してあることを特徴とする。
According to a fifth aspect of the present invention, in the fourth aspect, an outer peripheral side of the second activated carbon layer is provided with an activated carbon case for accommodating the second activated carbon layer therein, and an outer periphery of the cap. The projecting portion is provided with a plurality of projecting portions projecting radially outward and in contact with the inner peripheral surface of the activated carbon case at a plurality of locations in the circumferential direction, and the projecting portions are provided with the leg portions. The end of the second activated carbon layer is fixed in a radial position relative to the activated carbon case by contacting the activated carbon case with the activated carbon case, and the activated carbon case and the second activated carbon layer An annular water passage space is formed between them, and a communication passage for communicating the water passage space and the gap is formed between the protrusion and the protrusion.
本発明の第6の発明は、第5の発明において、前記第2の活性炭層の中心部には、多孔質の焼結体から成る筒状のセラミックスフィルタが、内部を前記浄水出口に連通させる状態で該第2の活性炭層に対する支持部材として設けてあり、該第2の活性炭層及びセラミックスフィルタが径方向に水を通過させて浄化を行うことを特徴とする。
According to a sixth aspect of the present invention, in the fifth aspect, a cylindrical ceramic filter made of a porous sintered body is communicated with the purified water outlet at the center of the second activated carbon layer. It is provided as a support member for the second activated carbon layer in a state, and the second activated carbon layer and the ceramic filter perform purification by passing water in a radial direction.
本発明の第7の発明は、第6の発明において、前記セラミックスフィルタが抗菌性を備えたものであることを特徴とする。
According to a seventh aspect of the present invention, in the sixth aspect, the ceramic filter has antibacterial properties.
本発明の第8の発明は、第1の発明~第7の発明の何れか一つにおいて、前記フィルタが0.1μmの微細な粒子まで濾過可能なものであることを特徴とする。
According to an eighth aspect of the present invention, in any one of the first to seventh aspects, the filter is capable of filtering to fine particles of 0.1 μm.
本発明の第9の発明は、第1の発明~第8の発明の何れか一つにおいて、前記フィルタが中空糸膜フィルタであることを特徴とする。
また、本発明の第10の発明は、原水入口と浄水出口とを有するケースと、前記ケースの内部において、前記浄水出口よりも前記原水入口に近い位置に配置される第1の活性炭層と、前記ケースの内部において、前記原水入口よりも前記浄水出口に近い位置に配置される第2の活性炭層と、前記第1の活性炭層と前記第2の活性炭層との間に配置されるフィルタとを備える浄水器である。
また、本発明の第11の発明は、第10の発明において、前記第1の活性炭層は中空形状であり、前記第2の活性炭層と前記フィルタは、前記中空形状の内部に配置されていることを特徴としている。
また、本発明の第12の発明は、第11の発明において、前記第2の活性炭層と前記フィルタとの間には、第1の面と前記第1の面とは反対側の第2の面とを有するキャップが配置されており、前記第1の面は前記第2の活性炭層を支持し、前記第2の面は脚部を有し、前記脚部が前記フィルタの端部と接触し、前記第2の活性炭層と前記フィルタとの間に通水用の間隙が形成されていることを特徴としている。 According to a ninth aspect of the present invention, in any one of the first to eighth aspects, the filter is a hollow fiber membrane filter.
Further, the tenth invention of the present invention is a case having a raw water inlet and a purified water outlet, and a first activated carbon layer disposed in a position closer to the raw water inlet than the purified water outlet in the case, Inside the case, a second activated carbon layer disposed closer to the water purification outlet than the raw water inlet, and a filter disposed between the first activated carbon layer and the second activated carbon layer. It is a water purifier equipped with.
In an eleventh aspect of the present invention, in the tenth aspect, the first activated carbon layer has a hollow shape, and the second activated carbon layer and the filter are disposed inside the hollow shape. It is characterized by that.
In addition, in a twelfth aspect of the present invention based on the eleventh aspect, the second surface on the opposite side of the first surface and the first surface is between the second activated carbon layer and the filter. A cap having a surface, the first surface supports the second activated carbon layer, the second surface has a leg, and the leg contacts the end of the filter. In addition, a gap for water passage is formed between the second activated carbon layer and the filter.
また、本発明の第10の発明は、原水入口と浄水出口とを有するケースと、前記ケースの内部において、前記浄水出口よりも前記原水入口に近い位置に配置される第1の活性炭層と、前記ケースの内部において、前記原水入口よりも前記浄水出口に近い位置に配置される第2の活性炭層と、前記第1の活性炭層と前記第2の活性炭層との間に配置されるフィルタとを備える浄水器である。
また、本発明の第11の発明は、第10の発明において、前記第1の活性炭層は中空形状であり、前記第2の活性炭層と前記フィルタは、前記中空形状の内部に配置されていることを特徴としている。
また、本発明の第12の発明は、第11の発明において、前記第2の活性炭層と前記フィルタとの間には、第1の面と前記第1の面とは反対側の第2の面とを有するキャップが配置されており、前記第1の面は前記第2の活性炭層を支持し、前記第2の面は脚部を有し、前記脚部が前記フィルタの端部と接触し、前記第2の活性炭層と前記フィルタとの間に通水用の間隙が形成されていることを特徴としている。 According to a ninth aspect of the present invention, in any one of the first to eighth aspects, the filter is a hollow fiber membrane filter.
Further, the tenth invention of the present invention is a case having a raw water inlet and a purified water outlet, and a first activated carbon layer disposed in a position closer to the raw water inlet than the purified water outlet in the case, Inside the case, a second activated carbon layer disposed closer to the water purification outlet than the raw water inlet, and a filter disposed between the first activated carbon layer and the second activated carbon layer. It is a water purifier equipped with.
In an eleventh aspect of the present invention, in the tenth aspect, the first activated carbon layer has a hollow shape, and the second activated carbon layer and the filter are disposed inside the hollow shape. It is characterized by that.
In addition, in a twelfth aspect of the present invention based on the eleventh aspect, the second surface on the opposite side of the first surface and the first surface is between the second activated carbon layer and the filter. A cap having a surface, the first surface supports the second activated carbon layer, the second surface has a leg, and the leg contacts the end of the filter. In addition, a gap for water passage is formed between the second activated carbon layer and the filter.
以上のように本発明は、浄水器内部の浄化材として、原水入口の側から第1の活性炭層,水中粒子を濾過作用で除去するフィルタ,第2の活性炭層の順序で配置し、原水を第1の活性炭層,フィルタ,第2の活性炭層の順に通して浄化するものである。
As mentioned above, this invention arrange | positions in order of the 1st activated carbon layer from the raw | natural water inlet side as a purification material inside a water purifier, the filter which removes an underwater particle | grain by filtration, and a 2nd activated carbon layer, The first activated carbon layer, the filter, and the second activated carbon layer are passed in order for purification.
本発明においては、浄水器内部に流入した原水が先ず第1の活性炭層を通過して流れる。
このとき原水中に含まれていた残留塩素が、第1の活性炭層による吸着によって除去される。
従ってその下流側に配置してあるフィルタに対し、原水中の残留塩素が作用してしまうのを防ぐことができる。 In this invention, the raw | natural water which flowed in the inside of a water purifier flows first through a 1st activated carbon layer.
At this time, residual chlorine contained in the raw water is removed by adsorption by the first activated carbon layer.
Accordingly, residual chlorine in the raw water can be prevented from acting on the filter disposed on the downstream side.
このとき原水中に含まれていた残留塩素が、第1の活性炭層による吸着によって除去される。
従ってその下流側に配置してあるフィルタに対し、原水中の残留塩素が作用してしまうのを防ぐことができる。 In this invention, the raw | natural water which flowed in the inside of a water purifier flows first through a 1st activated carbon layer.
At this time, residual chlorine contained in the raw water is removed by adsorption by the first activated carbon layer.
Accordingly, residual chlorine in the raw water can be prevented from acting on the filter disposed on the downstream side.
従って、フィルタとして中空糸膜フィルタを用いた場合(第9の発明)においても、中空糸膜フィルタを最も上流側に配置した従来の浄水器のように、原水中の残留塩素が中空糸膜に作用してその劣化を早めて中空糸膜フィルタによる濾過精度を低下させてしまう問題を解決できる。すなわち、中空糸膜フィルタによる濾過精度を高精度に維持することができる。
Therefore, even when a hollow fiber membrane filter is used as the filter (the ninth invention), the residual chlorine in the raw water is transferred to the hollow fiber membrane as in the conventional water purifier in which the hollow fiber membrane filter is disposed on the most upstream side. It is possible to solve the problem of acting to accelerate the deterioration and lowering the filtration accuracy by the hollow fiber membrane filter. That is, the filtration accuracy by the hollow fiber membrane filter can be maintained with high accuracy.
本発明においては、第1の活性炭層を通過して流れて来た原水をフィルタに通して、フィルタの濾過作用で原水中の夾雑物等の濁り粒子を除去する。
第2の活性炭層は、そのフィルタを通過して粒子物等の濁り粒子が除去された原水を通過させて、吸着により原水中に含まれている有害成分を除去する。 In the present invention, the raw water flowing through the first activated carbon layer is passed through a filter, and turbid particles such as contaminants in the raw water are removed by the filtering action of the filter.
The second activated carbon layer passes through the filter and passes through raw water from which turbid particles such as particles are removed, and removes harmful components contained in the raw water by adsorption.
第2の活性炭層は、そのフィルタを通過して粒子物等の濁り粒子が除去された原水を通過させて、吸着により原水中に含まれている有害成分を除去する。 In the present invention, the raw water flowing through the first activated carbon layer is passed through a filter, and turbid particles such as contaminants in the raw water are removed by the filtering action of the filter.
The second activated carbon layer passes through the filter and passes through raw water from which turbid particles such as particles are removed, and removes harmful components contained in the raw water by adsorption.
その際、第2の活性炭層まで流れて来た原水には粒子物が含まれておらず、活性炭の表面が粒子物の付着により覆われてしまうことがないため、第2の活性炭層は本来の浄化性能を最大限発揮することができる。
At that time, since the raw water flowing to the second activated carbon layer does not contain particulate matter and the surface of the activated carbon is not covered by the adhesion of particulate matter, the second activated carbon layer is originally The maximum purification performance can be achieved.
また第2の活性炭層に到った原水は、第1の活性炭層を通過した段階で残留塩素が吸着によって既に取り除かれているため、第2の活性炭層においてはトリハロメタンやトリクロロエタンの吸着が残留塩素にて阻害されることがなく、それらの有害成分が良好に吸着されて原水中から除去される。
Since the raw water that has reached the second activated carbon layer has already had its residual chlorine removed by adsorption when it has passed through the first activated carbon layer, the adsorption of trihalomethane and trichloroethane has been eliminated by residual chlorine in the second activated carbon layer. These harmful components are well adsorbed and removed from the raw water without being hindered.
即ち、原水中に含まれているトリハロメタン,トリクロロエタン等は、浄水器の使用初期においては第1の活性炭層でも吸着により除去される。そして、浄水器を長期間使用すると第1の活性炭層の活性炭表面が粒子物により覆われて吸着能が低下し、更には残留塩素の吸着により、吸着力の弱いトリハロメタンやトリクロロエタンに対する吸着性能が低下する。このため、トリハロメタンやトリクロロエタン等の成分を第1の活性炭層で除去し切れずに、それらが後段のフィルタを通過して下流側へと流れてしまう。
本発明ではそのフィルタの更に下流側に、第2の活性炭層が設けてあるため、第1の活性炭層で取り切れなかったトリハロメタンやトリクロロエタンを第2の活性炭層で良好に吸着し原水中から除去することができる。 That is, trihalomethane, trichloroethane, and the like contained in the raw water are removed by adsorption even in the first activated carbon layer in the initial stage of use of the water purifier. When the water purifier is used for a long period of time, the activated carbon surface of the first activated carbon layer is covered with particulate matter and the adsorption capacity is lowered, and further, the adsorption performance for trihalomethane and trichloroethane having a weak adsorption force is lowered due to adsorption of residual chlorine. To do. For this reason, components such as trihalomethane and trichloroethane are not completely removed by the first activated carbon layer, but they pass downstream and flow downstream.
In the present invention, since the second activated carbon layer is provided further downstream of the filter, trihalomethane and trichloroethane that could not be removed by the first activated carbon layer are adsorbed well by the second activated carbon layer and removed from the raw water. can do.
本発明ではそのフィルタの更に下流側に、第2の活性炭層が設けてあるため、第1の活性炭層で取り切れなかったトリハロメタンやトリクロロエタンを第2の活性炭層で良好に吸着し原水中から除去することができる。 That is, trihalomethane, trichloroethane, and the like contained in the raw water are removed by adsorption even in the first activated carbon layer in the initial stage of use of the water purifier. When the water purifier is used for a long period of time, the activated carbon surface of the first activated carbon layer is covered with particulate matter and the adsorption capacity is lowered, and further, the adsorption performance for trihalomethane and trichloroethane having a weak adsorption force is lowered due to adsorption of residual chlorine. To do. For this reason, components such as trihalomethane and trichloroethane are not completely removed by the first activated carbon layer, but they pass downstream and flow downstream.
In the present invention, since the second activated carbon layer is provided further downstream of the filter, trihalomethane and trichloroethane that could not be removed by the first activated carbon layer are adsorbed well by the second activated carbon layer and removed from the raw water. can do.
以上のように、本発明は、前段の第1の活性炭層と後段の第2の活性炭層とでそれぞれ役割分担して原水中に溶存している有害成分を除去するものであり、このことにより本発明の浄水器は使用初期から高い浄化性能を発揮するとともに、長期に亘ってその高い浄化性能を維持することができる。
As described above, the present invention removes harmful components dissolved in the raw water by sharing the roles of the first activated carbon layer in the former stage and the second activated carbon layer in the latter stage. The water purifier of the present invention exhibits high purification performance from the beginning of use and can maintain the high purification performance over a long period of time.
また第2の活性炭層は高い浄化性能を長期間維持するため、通常は、第2の活性炭層の浄化性能が低下する以前に、これよりも前段にあるフィルタが目詰まりを起し、浄水器を流れる水の流量が少なくなる。
従って、使用者が浄水器の目詰まりによる流量の減少を寿命の目安として浄水器を使った場合、浄化性能が低下しているにも拘らず目詰まりを起していないことによって、浄水器をそのまま使用し続けてしまうといったことを防ぐことが可能となる。 In addition, since the second activated carbon layer maintains high purification performance for a long period of time, normally, before the purification performance of the second activated carbon layer deteriorates, the filter in the previous stage is clogged, and the water purifier The flow rate of water flowing through is reduced.
Therefore, when a user uses a water purifier with a decrease in the flow rate due to clogging of the water purifier as a guideline for the service life, the water purifier is not clogged even though the purifying performance has deteriorated. It is possible to prevent the user from continuing to use it as it is.
従って、使用者が浄水器の目詰まりによる流量の減少を寿命の目安として浄水器を使った場合、浄化性能が低下しているにも拘らず目詰まりを起していないことによって、浄水器をそのまま使用し続けてしまうといったことを防ぐことが可能となる。 In addition, since the second activated carbon layer maintains high purification performance for a long period of time, normally, before the purification performance of the second activated carbon layer deteriorates, the filter in the previous stage is clogged, and the water purifier The flow rate of water flowing through is reduced.
Therefore, when a user uses a water purifier with a decrease in the flow rate due to clogging of the water purifier as a guideline for the service life, the water purifier is not clogged even though the purifying performance has deteriorated. It is possible to prevent the user from continuing to use it as it is.
尚、本発明ではフィルタの下流側に第2の活性炭層を設けており、この場合活性炭として粒状活性炭を用い、これを従来と同様に単に収容部に充填しただけであると、活性炭が流出してしまう恐れがある。
この場合、活性炭の流出防止のための専用の濾過膜等を設けておくといったことも考えられるが、その場合には所要部品が多くなってしまい、浄水器のコストアップをもたらしてしまう。
そこでかかる第2の活性炭層として、粒状の活性炭を接着剤等で固め成形した成形活性炭を用いるようになすことが望ましい。
このようにすることで、第2の活性炭層全体の形状を保持する保持部材を不要化でき、また活性炭の流出防止も併せて図ることができる。 In the present invention, a second activated carbon layer is provided on the downstream side of the filter, and in this case, granular activated carbon is used as the activated carbon, and if this is simply filled in the accommodating portion as in the conventional case, the activated carbon flows out. There is a risk that.
In this case, it may be possible to provide a dedicated filter membrane or the like for preventing the activated carbon from flowing out, but in that case, the number of required parts increases, resulting in an increase in the cost of the water purifier.
Therefore, it is desirable to use molded activated carbon obtained by solidifying granular activated carbon with an adhesive or the like as the second activated carbon layer.
By doing in this way, the holding member which hold | maintains the shape of the whole 2nd activated carbon layer can be made unnecessary, and the outflow of activated carbon can also be aimed at.
この場合、活性炭の流出防止のための専用の濾過膜等を設けておくといったことも考えられるが、その場合には所要部品が多くなってしまい、浄水器のコストアップをもたらしてしまう。
そこでかかる第2の活性炭層として、粒状の活性炭を接着剤等で固め成形した成形活性炭を用いるようになすことが望ましい。
このようにすることで、第2の活性炭層全体の形状を保持する保持部材を不要化でき、また活性炭の流出防止も併せて図ることができる。 In the present invention, a second activated carbon layer is provided on the downstream side of the filter, and in this case, granular activated carbon is used as the activated carbon, and if this is simply filled in the accommodating portion as in the conventional case, the activated carbon flows out. There is a risk that.
In this case, it may be possible to provide a dedicated filter membrane or the like for preventing the activated carbon from flowing out, but in that case, the number of required parts increases, resulting in an increase in the cost of the water purifier.
Therefore, it is desirable to use molded activated carbon obtained by solidifying granular activated carbon with an adhesive or the like as the second activated carbon layer.
By doing in this way, the holding member which hold | maintains the shape of the whole 2nd activated carbon layer can be made unnecessary, and the outflow of activated carbon can also be aimed at.
本発明においては、第2の発明に従い上記ケースを筒状となして、ケース内空間の外周側の筒状の収容空間に第1の活性炭層をケースの内周面に沿って軸方向に配置する。さらに、ケース内空間における第1の活性炭層の内側の中央部に上記フィルタと第2の活性炭層とを、フィルタが第1の活性炭層における下流側部分に径方向に隣接して位置し、また第2の活性炭層が第1の活性炭層における上流側部分に径方向に隣接して位置するように軸方向に並べて配置する。そして、原水入口から流入した原水を第1の活性炭層内部を軸方向に流通移動させた後、フィルタを通過して第2の活性炭層に流入及び通過させて浄化し、浄水を浄水出口から流出させることができる。
この第2の発明によれば、限られた大きさのケース内で原水が浄化材を通過する距離を長くとること(接触時間を長くすること)ができ、浄水器をコンパクト化しつつ浄化能力を高めることができる。 In the present invention, the case is formed into a cylindrical shape according to the second invention, and the first activated carbon layer is disposed in the axial direction along the inner peripheral surface of the case in the cylindrical accommodating space on the outer peripheral side of the case inner space. To do. Furthermore, the filter and the second activated carbon layer are disposed in the central portion inside the first activated carbon layer in the space in the case, the filter is positioned adjacent to the downstream portion of the first activated carbon layer in the radial direction, and The second activated carbon layer is arranged side by side in the axial direction so as to be positioned radially adjacent to the upstream side portion of the first activated carbon layer. After the raw water flowing in from the raw water inlet is circulated in the first activated carbon layer in the axial direction, the raw water passes through the filter and flows into and through the second activated carbon layer for purification, and the purified water flows out from the purified water outlet. Can be made.
According to the second aspect of the present invention, the distance through which the raw water passes through the purification material can be increased within a limited size case (the contact time can be increased), and the purification capacity can be improved while reducing the size of the water purifier. Can be increased.
この第2の発明によれば、限られた大きさのケース内で原水が浄化材を通過する距離を長くとること(接触時間を長くすること)ができ、浄水器をコンパクト化しつつ浄化能力を高めることができる。 In the present invention, the case is formed into a cylindrical shape according to the second invention, and the first activated carbon layer is disposed in the axial direction along the inner peripheral surface of the case in the cylindrical accommodating space on the outer peripheral side of the case inner space. To do. Furthermore, the filter and the second activated carbon layer are disposed in the central portion inside the first activated carbon layer in the space in the case, the filter is positioned adjacent to the downstream portion of the first activated carbon layer in the radial direction, and The second activated carbon layer is arranged side by side in the axial direction so as to be positioned radially adjacent to the upstream side portion of the first activated carbon layer. After the raw water flowing in from the raw water inlet is circulated in the first activated carbon layer in the axial direction, the raw water passes through the filter and flows into and through the second activated carbon layer for purification, and the purified water flows out from the purified water outlet. Can be made.
According to the second aspect of the present invention, the distance through which the raw water passes through the purification material can be increased within a limited size case (the contact time can be increased), and the purification capacity can be improved while reducing the size of the water purifier. Can be increased.
またケース内の収容空間の外周側部分に第1の活性炭層をケースの内周面に沿って軸方向に配置することで、第1の活性炭層の容量を大とすることができる。さらに、軸方向長さを長く取ることができ、第1の活性炭層による残留塩素の除去性能を長期間保持することができる。
Moreover, the capacity | capacitance of a 1st activated carbon layer can be enlarged by arrange | positioning a 1st activated carbon layer to an axial direction along the inner peripheral surface of a case in the outer peripheral side part of the storage space in a case. Furthermore, the axial length can be increased, and the residual chlorine removal performance by the first activated carbon layer can be maintained for a long time.
次に、本発明の第3の発明は、上記ケースを、軸方向一端側に底部を、他端側に開口を有するケース本体と、その開口を閉鎖する状態にケース本体に軸方向に組み付けられる蓋体とに軸方向に分割し、ケース本体に蓋体を組み付けることで、ケースの内部のフィルタと第2の活性炭層とを底部と蓋体とで軸方向に拘束し固定するものである。この第3の発明によれば、フィルタ及び第2の活性炭層を固定するための部品数を減らすことができ、浄水器のコンパクト化、低コスト化に寄与するとともに、それらフィルタ及び第2の活性炭層の組付けを簡単に行うことができる。
Next, according to a third aspect of the present invention, the above case is assembled in the axial direction to the case main body in such a manner that the case main body has a bottom portion at one end in the axial direction and an opening at the other end, and the opening is closed. By dividing into a lid body in the axial direction and assembling the lid body to the case body, the filter and the second activated carbon layer inside the case are restrained and fixed in the axial direction by the bottom portion and the lid body. According to the third aspect of the invention, the number of parts for fixing the filter and the second activated carbon layer can be reduced, contributing to the downsizing and cost reduction of the water purifier, and the filter and the second activated carbon. Easy assembly of the layers.
本発明においてはまた、本発明の第4の発明に従って第2の活性炭層を筒状に設ける。さらに、その第2の活性炭層のフィルタ側の端部にキャップを装着し、そしてそのキャップに、周方向の複数個所で外周部からフィルタ側に突出してフィルタの軸方向の端面に当接するスペーサ部としての複数の脚を設ける。その脚により、軸方向においてフィルタ側と第2の活性炭層側との間に通水用の間隙を形成しておくことができる。
この第4の発明では、キャップに備えた脚によって上記の間隙が形成されるため、その間隙を形成するための特別のスペーサ部材を別途に必要とせず、所要部品数を少なくすることができる。 In the present invention, the second activated carbon layer is provided in a cylindrical shape according to the fourth aspect of the present invention. Further, a cap is attached to the end of the second activated carbon layer on the filter side, and the spacer protrudes from the outer periphery to the filter side at a plurality of locations in the circumferential direction and contacts the axial end surface of the filter. A plurality of legs are provided. With the legs, a gap for passing water can be formed between the filter side and the second activated carbon layer side in the axial direction.
In the fourth aspect of the invention, since the gap is formed by the legs provided in the cap, a special spacer member for forming the gap is not required separately, and the number of required parts can be reduced.
この第4の発明では、キャップに備えた脚によって上記の間隙が形成されるため、その間隙を形成するための特別のスペーサ部材を別途に必要とせず、所要部品数を少なくすることができる。 In the present invention, the second activated carbon layer is provided in a cylindrical shape according to the fourth aspect of the present invention. Further, a cap is attached to the end of the second activated carbon layer on the filter side, and the spacer protrudes from the outer periphery to the filter side at a plurality of locations in the circumferential direction and contacts the axial end surface of the filter. A plurality of legs are provided. With the legs, a gap for passing water can be formed between the filter side and the second activated carbon layer side in the axial direction.
In the fourth aspect of the invention, since the gap is formed by the legs provided in the cap, a special spacer member for forming the gap is not required separately, and the number of required parts can be reduced.
本発明の第5の発明は、上記キャップの外周部に、径方向外方に突出して活性炭ケースの内周面に当接する突出部を周方向の複数個所に設けて、その突出部に上記の脚を設ける。また複数の突出部の活性炭ケースへの当接により第2の活性炭層の端部を活性炭ケースに径方向に位置決状態に固定するとともに、活性炭ケースと第2の活性炭層との間に環状の通水空間を形成し、且つ通水空間と上記の間隙とを連通させる連通路を、突出部と突出部との間に形成したものである。この第5の発明によれば、第2の活性炭層の端部に装着されたキャップによって、活性炭ケースに対する第2の活性炭層端部の径方向の固定を行うことができるとともに、活性炭ケースと第2の活性炭層との間に環状の通水空間を形成することができる。
更にその通水空間及びフィルタ側と第2の活性炭層側との間の上記の間隙を、突出部と突出部との間に形成される連通路を通じて連通させることができる。 According to a fifth aspect of the present invention, the outer peripheral portion of the cap is provided with a plurality of projecting portions projecting radially outward and in contact with the inner peripheral surface of the activated carbon case at a plurality of locations in the circumferential direction. Provide legs. In addition, the end of the second activated carbon layer is fixed to the activated carbon case in a radially positioned state by the abutment of the plurality of protrusions to the activated carbon case, and an annular shape is provided between the activated carbon case and the second activated carbon layer. A communication passage that forms a water flow space and connects the water flow space and the gap is formed between the protrusion and the protrusion. According to the fifth aspect of the invention, the cap attached to the end of the second activated carbon layer can fix the end of the second activated carbon layer with respect to the activated carbon case in the radial direction. An annular water passage space can be formed between the two activated carbon layers.
Further, the water passage space and the gap between the filter side and the second activated carbon layer side can be communicated through a communication path formed between the protrusions.
更にその通水空間及びフィルタ側と第2の活性炭層側との間の上記の間隙を、突出部と突出部との間に形成される連通路を通じて連通させることができる。 According to a fifth aspect of the present invention, the outer peripheral portion of the cap is provided with a plurality of projecting portions projecting radially outward and in contact with the inner peripheral surface of the activated carbon case at a plurality of locations in the circumferential direction. Provide legs. In addition, the end of the second activated carbon layer is fixed to the activated carbon case in a radially positioned state by the abutment of the plurality of protrusions to the activated carbon case, and an annular shape is provided between the activated carbon case and the second activated carbon layer. A communication passage that forms a water flow space and connects the water flow space and the gap is formed between the protrusion and the protrusion. According to the fifth aspect of the invention, the cap attached to the end of the second activated carbon layer can fix the end of the second activated carbon layer with respect to the activated carbon case in the radial direction. An annular water passage space can be formed between the two activated carbon layers.
Further, the water passage space and the gap between the filter side and the second activated carbon layer side can be communicated through a communication path formed between the protrusions.
即ち、フィルタから流出した水を先ずフィルタ側と第2の活性炭層との間の間隙に流出させ、更に、これを連通路を通じて第2の活性炭層周りの環状の通水空間へと導入することができる。
またこのようにすることで、フィルタからの水の流出に対する圧力抵抗を高めることなく、円滑にフィルタからの水を第2の活性炭層周りの環状の通水空間に導入することができる。 That is, water that has flowed out of the filter is first allowed to flow into the gap between the filter side and the second activated carbon layer, and further introduced into the annular water flow space around the second activated carbon layer through the communication path. Can do.
Moreover, by doing in this way, the water from a filter can be smoothly introduce | transduced into the cyclic | annular water flow space around the 2nd activated carbon layer, without raising the pressure resistance with respect to the outflow of the water from a filter.
またこのようにすることで、フィルタからの水の流出に対する圧力抵抗を高めることなく、円滑にフィルタからの水を第2の活性炭層周りの環状の通水空間に導入することができる。 That is, water that has flowed out of the filter is first allowed to flow into the gap between the filter side and the second activated carbon layer, and further introduced into the annular water flow space around the second activated carbon layer through the communication path. Can do.
Moreover, by doing in this way, the water from a filter can be smoothly introduce | transduced into the cyclic | annular water flow space around the 2nd activated carbon layer, without raising the pressure resistance with respect to the outflow of the water from a filter.
また活性炭ケースへの第2の活性炭層端部の固定、第2の活性炭層周りの環状の通水空間の形成及び上記間隙とその通水空間との連通路の形成を、キャップに備えた突出部にて行うことができる。それらを行うための特別な部材を別途に必要とせず、部品点数を少なくすることができる。
In addition, the end of the second activated carbon layer is fixed to the activated carbon case, the annular water passage space around the second activated carbon layer is formed, and the communication path between the gap and the water passage space is formed. Can be done in the department. A special member for performing them is not required separately, and the number of parts can be reduced.
この場合において、第2の活性炭層の中心部には、多孔質の焼結体から成る筒状のセラミックスフィルタを第2の活性炭層に対する透水性の支持部材として設け、そしてそれら第2の活性炭層及びセラミックスフィルタを径方向に水を通過させて浄化を行うことができる(第6の発明)。
この第6の発明では、セラミックスフィルタの支持部材としての働きにより、第2の活性炭層を成形活性炭で構成したときに、成形活性炭を壊れ難くすることができる。 In this case, a cylindrical ceramic filter made of a porous sintered body is provided at the center of the second activated carbon layer as a water-permeable support member for the second activated carbon layer, and the second activated carbon layer. And purification can be performed by passing water in the radial direction through the ceramic filter (sixth invention).
In the sixth aspect of the present invention, when the second activated carbon layer is formed of molded activated carbon, it is possible to make the molded activated carbon difficult to break due to the function as a support member of the ceramic filter.
この第6の発明では、セラミックスフィルタの支持部材としての働きにより、第2の活性炭層を成形活性炭で構成したときに、成形活性炭を壊れ難くすることができる。 In this case, a cylindrical ceramic filter made of a porous sintered body is provided at the center of the second activated carbon layer as a water-permeable support member for the second activated carbon layer, and the second activated carbon layer. And purification can be performed by passing water in the radial direction through the ceramic filter (sixth invention).
In the sixth aspect of the present invention, when the second activated carbon layer is formed of molded activated carbon, it is possible to make the molded activated carbon difficult to break due to the function as a support member of the ceramic filter.
そのセラミックスフィルタは、抗菌性を備えたことができる(第7の発明)。
このようにすれば、浄水器外部から浄水出口を通じて雑菌が内部に侵入する逆汚染を有効に防止することができる。 The ceramic filter can have antibacterial properties (seventh invention).
In this way, it is possible to effectively prevent back-contamination where germs enter the inside from the outside of the water purifier through the water purification outlet.
このようにすれば、浄水器外部から浄水出口を通じて雑菌が内部に侵入する逆汚染を有効に防止することができる。 The ceramic filter can have antibacterial properties (seventh invention).
In this way, it is possible to effectively prevent back-contamination where germs enter the inside from the outside of the water purifier through the water purification outlet.
尚、本発明においては、フィルタとして0.1μmの微細な粒子まで濾過可能なものを好適に用いることができる(第8の発明)。
In addition, in this invention, what can be filtered to a 0.1 micrometer fine particle | grain can be used suitably as a filter (8th invention).
またフィルタとして中空糸膜フィルタを好適に用いることができるが(第9の発明)、多孔質の焼結体から成るセラミックスフィルタを用いることも可能である。
この構成によれば、セラミックスフィルタとして、0.1μmの微細な粒子まで濾過可能なものを好適に用いることができる。 A hollow fiber membrane filter can be suitably used as the filter (the ninth invention), but a ceramic filter made of a porous sintered body can also be used.
According to this configuration, a ceramic filter that can be filtered to fine particles of 0.1 μm can be suitably used.
この構成によれば、セラミックスフィルタとして、0.1μmの微細な粒子まで濾過可能なものを好適に用いることができる。 A hollow fiber membrane filter can be suitably used as the filter (the ninth invention), but a ceramic filter made of a porous sintered body can also be used.
According to this configuration, a ceramic filter that can be filtered to fine particles of 0.1 μm can be suitably used.
本発明では、第1の活性炭層,第2の活性炭層として粒状活性炭を好適に用い得るが、繊維状活性炭その他を用いることも可能である。
また粒状活性炭を用いる場合において、粒度(平均粒径)が0.05~1.0mmの範囲内のものを好適に用いることができる。
この粒度範囲は通水時の圧力損失が低く、且つ浄化性能にも優れた適正な粒度範囲である。 In this invention, although granular activated carbon can be used suitably as a 1st activated carbon layer and a 2nd activated carbon layer, fibrous activated carbon and others can also be used.
When granular activated carbon is used, those having a particle size (average particle size) in the range of 0.05 to 1.0 mm can be suitably used.
This particle size range is an appropriate particle size range with low pressure loss during water passage and excellent purification performance.
また粒状活性炭を用いる場合において、粒度(平均粒径)が0.05~1.0mmの範囲内のものを好適に用いることができる。
この粒度範囲は通水時の圧力損失が低く、且つ浄化性能にも優れた適正な粒度範囲である。 In this invention, although granular activated carbon can be used suitably as a 1st activated carbon layer and a 2nd activated carbon layer, fibrous activated carbon and others can also be used.
When granular activated carbon is used, those having a particle size (average particle size) in the range of 0.05 to 1.0 mm can be suitably used.
This particle size range is an appropriate particle size range with low pressure loss during water passage and excellent purification performance.
次に本発明の実施形態を図面に基づいて以下に詳述する。
図1において、1はキッチンに設置された流し台で、2はキャビネット、3はシンク、10はカウンターで、11は流し台1に設置された浄水吐水機能を有する自動水栓である。
自動水栓11は、カウンター10から起立する形態で設けられた基部側の本体部12と、本体部12から延び出した吐水管14とを有している。
ここで吐水管14は、本体部12に対して所定角度回動可能とされている。 Next, embodiments of the present invention will be described in detail below with reference to the drawings.
In FIG. 1, 1 is a sink installed in the kitchen, 2 is a cabinet, 3 is a sink, 10 is a counter, and 11 is an automatic faucet installed on thesink 1 and having a purified water discharge function.
Theautomatic faucet 11 includes a base body 12 provided in a form standing from the counter 10 and a water discharge pipe 14 extending from the body 12.
Here, thewater discharge pipe 14 is rotatable by a predetermined angle with respect to the main body 12.
図1において、1はキッチンに設置された流し台で、2はキャビネット、3はシンク、10はカウンターで、11は流し台1に設置された浄水吐水機能を有する自動水栓である。
自動水栓11は、カウンター10から起立する形態で設けられた基部側の本体部12と、本体部12から延び出した吐水管14とを有している。
ここで吐水管14は、本体部12に対して所定角度回動可能とされている。 Next, embodiments of the present invention will be described in detail below with reference to the drawings.
In FIG. 1, 1 is a sink installed in the kitchen, 2 is a cabinet, 3 is a sink, 10 is a counter, and 11 is an automatic faucet installed on the
The
Here, the
本体部12には、使用者から見た正面視において吐水管14の右側に偏心した位置にシングルレバー16が設けられている。ここでシングルレバー16は吐水の流量調節と温度調節とを行う。
具体的には、シングルレバー16を図中左右方向に回動操作することで吐水の温度調節が行われ、また上下に回動操作することで流量調節が行われる。 Themain body 12 is provided with a single lever 16 at a position eccentric to the right side of the water discharge pipe 14 in a front view as viewed from the user. Here, the single lever 16 adjusts the flow rate and temperature of the discharged water.
Specifically, the temperature of the water discharge is adjusted by rotating thesingle lever 16 in the horizontal direction in the drawing, and the flow rate is adjusted by rotating the single lever 16 up and down.
具体的には、シングルレバー16を図中左右方向に回動操作することで吐水の温度調節が行われ、また上下に回動操作することで流量調節が行われる。 The
Specifically, the temperature of the water discharge is adjusted by rotating the
吐水管14は、図1に示しているように略U字状のグースネック形状をしており、管軸方向の略中間部位から先端部にかけて下向きに湾曲した形状をしている。
同図に示しているように吐水管14は、先端に吐水口18を有し、可撓性のホース20とともに引出し可能な吐水ヘッド22と、吐水ヘッド22を収納位置に保持する吐水ヘッドホルダとしての働きを有する吐水管本体24とを有している。 As shown in FIG. 1, thewater discharge pipe 14 has a substantially U-shaped gooseneck shape, and has a shape curved downward from a substantially intermediate portion in the tube axis direction to the tip portion.
As shown in the figure, thewater discharge pipe 14 has a water discharge port 18 at the tip, a water discharge head 22 that can be pulled out together with the flexible hose 20, and a water discharge head holder that holds the water discharge head 22 in the storage position. And a water discharge pipe main body 24 having the function as described above.
同図に示しているように吐水管14は、先端に吐水口18を有し、可撓性のホース20とともに引出し可能な吐水ヘッド22と、吐水ヘッド22を収納位置に保持する吐水ヘッドホルダとしての働きを有する吐水管本体24とを有している。 As shown in FIG. 1, the
As shown in the figure, the
本体部12には給水路26,給湯路28の上端部が接続されており、給水路26,給湯路28を通じて水,湯が本体部12へと供給されるようになっている。
本体部12には、図示を省略する混合弁が内蔵されており、この混合弁から流出路32が延び出していて、この流出路32を通じ、温調水(シングルレバー16の操作により混合弁にて水と湯とが所定比率で混合された温調水で水又は湯だけからなる場合もある。以下温調水を原水とする)が吐水口18へと導かれるようになっている。 Themain body portion 12 is connected to the upper ends of the water supply passage 26 and the hot water supply passage 28, and water and hot water are supplied to the main body portion 12 through the water supply passage 26 and the hot water supply passage 28.
A mixing valve (not shown) is incorporated in themain body 12, and an outflow path 32 extends from the mixing valve. Through the outflow path 32, temperature control water (by mixing the single lever 16, In some cases, the temperature control water in which water and hot water are mixed at a predetermined ratio may consist of only water or hot water (hereinafter referred to as raw water).
本体部12には、図示を省略する混合弁が内蔵されており、この混合弁から流出路32が延び出していて、この流出路32を通じ、温調水(シングルレバー16の操作により混合弁にて水と湯とが所定比率で混合された温調水で水又は湯だけからなる場合もある。以下温調水を原水とする)が吐水口18へと導かれるようになっている。 The
A mixing valve (not shown) is incorporated in the
上記ホース20は、その内側に流出路32を形成している。そしてこの流出路32上に、これを開閉する原水弁(電磁弁)34が設けられている。ここで原水弁34は図示を省略するコントローラにより動作制御される。
また給水路26からは浄水路38が分岐して延び出しており、その先端が原水弁34の下流部において流出路32に接続されている。 Thehose 20 has an outflow path 32 formed inside thereof. A raw water valve (electromagnetic valve) 34 for opening and closing the outlet passage 32 is provided on the outflow passage 32. Here, the operation of the raw water valve 34 is controlled by a controller (not shown).
Further, awater purification path 38 branches out from the water supply path 26 and extends, and the tip of the water purification path 38 is connected to the outflow path 32 at the downstream portion of the raw water valve 34.
また給水路26からは浄水路38が分岐して延び出しており、その先端が原水弁34の下流部において流出路32に接続されている。 The
Further, a
この浄水路38上には浄水器40及び浄水路38を開閉する浄水弁(電磁弁)42が設けられている。この浄水弁42もまたコントローラにて動作制御される。
尚、46は止水栓である。 A water purifier 40 (electromagnetic valve) 42 for opening and closing thewater purifier 40 and the water purifying path 38 is provided on the water purifying path 38. The operation of the water purification valve 42 is also controlled by a controller.
In addition, 46 is a water stop cock.
尚、46は止水栓である。 A water purifier 40 (electromagnetic valve) 42 for opening and closing the
In addition, 46 is a water stop cock.
図1に示しているように吐水管14先端部の上面、詳しくは吐水管14の管軸方向の略中間部位の最上部位から先端側の部分の上面に原水用センサ60と、浄水用センサ58とが管軸方向に前後に並べて配置されている。
ここで原水用センサ60は、差し出された手を検知するごとに吐水口18からの原水(温調水)の吐水と止水とを交互に行わせる交互センサである。 As shown in FIG. 1, theraw water sensor 60 and the water purification sensor 58 are provided on the upper surface of the distal end portion of the water discharge pipe 14, specifically, on the upper surface of the uppermost portion of the substantially intermediate portion in the tube axis direction of the water discharge pipe 14. Are arranged side by side in the pipe axis direction.
Here, theraw water sensor 60 is an alternate sensor that alternately discharges raw water (temperature-controlled water) from the water outlet 18 and stops the water every time the inserted hand is detected.
ここで原水用センサ60は、差し出された手を検知するごとに吐水口18からの原水(温調水)の吐水と止水とを交互に行わせる交互センサである。 As shown in FIG. 1, the
Here, the
詳しくは、原水用センサ60の上方に手をかざすと、原水用センサ60が非接触で手を検知して、その検知に基づいて吐水口18から原水を吐水させ、その後原水用センサ60から手を引き込めても原水の吐水が継続される。
そして再び手を延ばして原水用センサ60を操作すると、即ち原水用センサ60にて手を検知させると、吐水口18からの原水の吐水が停止する。
浄水用センサ58もまた、手を検知するごとに(人体検知するごとに)吐水口18からの浄水の吐水と吐水停止(止水)とを交互に行わせる。
この実施形態では、原水用センサ60が使用者に近い前側且つ下側に、また浄水用センサ58が原水用センサ60よりも遠い奥側且つ上側に配置されている。 Specifically, when the hand is held over theraw water sensor 60, the raw water sensor 60 detects the hand in a non-contact manner, discharges the raw water from the spout 18 based on the detection, and then the raw water sensor 60 removes the hand. The raw water continues to be discharged even if the water is drawn.
Then, when theraw water sensor 60 is operated again by extending the hand, that is, when the raw water sensor 60 detects the hand, the discharge of the raw water from the spout 18 is stopped.
Thewater purification sensor 58 also alternately discharges purified water from the water outlet 18 and stops water discharge (stops water) every time a hand is detected (every human body is detected).
In this embodiment, theraw water sensor 60 is disposed on the front side and the lower side near the user, and the water purification sensor 58 is disposed on the far side and the upper side farther than the raw water sensor 60.
そして再び手を延ばして原水用センサ60を操作すると、即ち原水用センサ60にて手を検知させると、吐水口18からの原水の吐水が停止する。
浄水用センサ58もまた、手を検知するごとに(人体検知するごとに)吐水口18からの浄水の吐水と吐水停止(止水)とを交互に行わせる。
この実施形態では、原水用センサ60が使用者に近い前側且つ下側に、また浄水用センサ58が原水用センサ60よりも遠い奥側且つ上側に配置されている。 Specifically, when the hand is held over the
Then, when the
The
In this embodiment, the
図1において、41はキャビネット2内部で浄水器40を保持し且つこれをキャビネット2の側壁部43内面に固定する金属製のブラケットである。
In FIG. 1, reference numeral 41 denotes a metal bracket that holds the water purifier 40 inside the cabinet 2 and fixes it to the inner surface of the side wall 43 of the cabinet 2.
ホース38A,38Bは、それぞれその内部に浄水路38の一部を形成している。詳しくはホース38Aは、浄水路38のうち原水を浄水器40に流入させるための流入路を、またホース38Bは、浄水器40で浄化された後の浄水を吐水口18の側へと案内する浄水の流出路を形成している。
図1に示しているようにこれら一対のホース38A,38Bは、固定部52にてキャビネットの側壁部43内面に固定されている。 Each of the hoses 38A and 38B forms a part of the water purification path 38 therein. Specifically, the hose 38A guides the inflow path for allowing the raw water to flow into the water purifier 40 in the water purification path 38, and the hose 38B guides the purified water after being purified by the water purifier 40 to the spout 18 side. It forms an outlet for purified water.
As shown in FIG. 1, the pair ofhoses 38 </ b> A and 38 </ b> B are fixed to the inner surface of the side wall portion 43 of the cabinet by a fixing portion 52.
図1に示しているようにこれら一対のホース38A,38Bは、固定部52にてキャビネットの側壁部43内面に固定されている。 Each of the
As shown in FIG. 1, the pair of
図2中の(A)と(B)には、上記浄水器40の内部構造が具体的に示してある。
図中62は、軸方向両端が閉鎖された形の円筒形状のケースで、このケース62は、軸方向の一端側に底部64を、他端側に開口を有するケース本体66と、開口を閉鎖する状態にケース本体66に軸方向に組み付けられる蓋体68とに軸方向に分割されている。 The internal structure of thewater purifier 40 is specifically shown in (A) and (B) in FIG.
In the figure, 62 is a cylindrical case with both ends in the axial direction closed. Thiscase 62 has a case body 66 having a bottom 64 at one end in the axial direction and an opening at the other end, and the opening is closed. In such a state, it is divided in the axial direction into a lid body 68 that is assembled to the case main body 66 in the axial direction.
図中62は、軸方向両端が閉鎖された形の円筒形状のケースで、このケース62は、軸方向の一端側に底部64を、他端側に開口を有するケース本体66と、開口を閉鎖する状態にケース本体66に軸方向に組み付けられる蓋体68とに軸方向に分割されている。 The internal structure of the
In the figure, 62 is a cylindrical case with both ends in the axial direction closed. This
蓋体68は円形且つ板状をなす閉鎖部69と、円筒部70とを一体に有しており、その円筒部70の内周面の雌ねじ部72において、ケース本体66の外周面の雄ねじ部74にねじ結合されている。
尚ケース本体66と蓋体68との間はシール材によって水密にシールされている。 Thelid 68 integrally has a circular and plate-like closing portion 69 and a cylindrical portion 70, and a male screw portion 72 on the outer peripheral surface of the case main body 66 at a female screw portion 72 on the inner peripheral surface of the cylindrical portion 70. 74 is screwed together.
Thecase body 66 and the lid body 68 are sealed watertight by a sealing material.
尚ケース本体66と蓋体68との間はシール材によって水密にシールされている。 The
The
この蓋体68の閉鎖部69には、その中心から偏心した位置に原水入口76が、また中心部に浄水出口78がそれぞれ一体に設けられている。
これら原水入口76,浄水出口78は閉鎖部69から突出する状態で設けられている。
ここで原水入口76には上記のホース38Aが接続され、また浄水出口78にはホース38Bが接続される。 The closingportion 69 of the lid 68 is integrally provided with a raw water inlet 76 at a position eccentric from the center and a purified water outlet 78 at the center.
Theraw water inlet 76 and the purified water outlet 78 are provided so as to protrude from the closing portion 69.
Here, thehose 38A is connected to the raw water inlet 76, and the hose 38B is connected to the purified water outlet 78.
これら原水入口76,浄水出口78は閉鎖部69から突出する状態で設けられている。
ここで原水入口76には上記のホース38Aが接続され、また浄水出口78にはホース38Bが接続される。 The closing
The
Here, the
ケース62の内部には、後述する中空糸膜フィルタ130を内部に収容する円筒形状のフィルタケース80と、後述の第2活性炭層を内部に収容する円筒形状の活性炭ケース82とが軸方向に互いに連結状態で同軸状に設けられており、これらフィルタケース80及び活性炭ケース82によって、ケース62内空間が外周側部分と中央部とに区画されている。
そしてケース62内空間の外周側部分をなす筒状の収容空間84に活性炭(ここでは粒状活性炭)86-1が充填され、かかる活性炭86-1によって第1の活性炭層88が形成されている。
ここで収容空間84即ち第1の活性炭層88は、軸方向の一端(図中下端)が仕切板としての下プレート90にて規定され、また他端(図中上端)が活性炭押えをなす不織布92にて規定されている。 Inside thecase 62, a cylindrical filter case 80 for accommodating a hollow fiber membrane filter 130 to be described later and a cylindrical activated carbon case 82 for accommodating a second activated carbon layer to be described later are axially connected to each other. The filter case 80 and the activated carbon case 82 divide the inner space of the case 62 into an outer peripheral side portion and a central portion.
Acylindrical housing space 84 that forms an outer peripheral side portion of the space in the case 62 is filled with activated carbon (here, granular activated carbon) 86-1, and the activated carbon 86-1 forms a first activated carbon layer 88.
Here, theaccommodation space 84, that is, the first activated carbon layer 88 is a nonwoven fabric in which one end in the axial direction (lower end in the figure) is defined by the lower plate 90 as a partition plate and the other end (upper end in the figure) forms an activated carbon presser. 92.
そしてケース62内空間の外周側部分をなす筒状の収容空間84に活性炭(ここでは粒状活性炭)86-1が充填され、かかる活性炭86-1によって第1の活性炭層88が形成されている。
ここで収容空間84即ち第1の活性炭層88は、軸方向の一端(図中下端)が仕切板としての下プレート90にて規定され、また他端(図中上端)が活性炭押えをなす不織布92にて規定されている。 Inside the
A
Here, the
この実施形態では、第1の活性炭層88を形成する粒状の活性炭として、粒子径(平均粒径)が0.1~1.0mmのものを好適に用いることができる。
粒子径が0.1mm未満の小さなものであると、粒子径が小さ過ぎて活性炭86-1の充填率が高くなり過ぎてしまい、通水時の圧力抵抗が高くなって水が流れ難くなる。
一方粒子径が1.0mm超であると、粒子径が大き過ぎて活性炭全体の表面積が小となり、吸着の効率が低下してしまう。 In this embodiment, as the granular activated carbon forming the first activatedcarbon layer 88, one having a particle diameter (average particle diameter) of 0.1 to 1.0 mm can be suitably used.
If the particle size is smaller than 0.1 mm, the particle size is too small, the filling rate of the activated carbon 86-1 becomes too high, and the pressure resistance during water passage becomes high, making it difficult for water to flow.
On the other hand, if the particle diameter is more than 1.0 mm, the particle diameter is too large, the surface area of the entire activated carbon becomes small, and the adsorption efficiency is lowered.
粒子径が0.1mm未満の小さなものであると、粒子径が小さ過ぎて活性炭86-1の充填率が高くなり過ぎてしまい、通水時の圧力抵抗が高くなって水が流れ難くなる。
一方粒子径が1.0mm超であると、粒子径が大き過ぎて活性炭全体の表面積が小となり、吸着の効率が低下してしまう。 In this embodiment, as the granular activated carbon forming the first activated
If the particle size is smaller than 0.1 mm, the particle size is too small, the filling rate of the activated carbon 86-1 becomes too high, and the pressure resistance during water passage becomes high, making it difficult for water to flow.
On the other hand, if the particle diameter is more than 1.0 mm, the particle diameter is too large, the surface area of the entire activated carbon becomes small, and the adsorption efficiency is lowered.
ケース本体66の底部64には、リブ94が起立状態に設けられており、下プレート90はこのリブ94にて下側から支持されている。
下プレート90はその状態で下側、つまり底部64との間に通水空間96を形成している。
下プレート90は、フィルタケース80の外周側に貫通の開口98を有し、この開口98において通水空間96と収容空間84とを連通させている。
下プレート90は更に、フィルタケース80の内側且つ中央部に貫通の開口100を有しており、この開口100において通水空間96とフィルタケース80の内部とを連通させている。 Arib 94 is provided in an upright state at the bottom 64 of the case body 66, and the lower plate 90 is supported by the rib 94 from below.
In this state, thelower plate 90 forms a water passing space 96 between the lower side, that is, the bottom 64.
Thelower plate 90 has a through-opening 98 on the outer peripheral side of the filter case 80, and the water passage space 96 and the accommodation space 84 are communicated with each other through the opening 98.
Thelower plate 90 further has a through-opening 100 inside and at the center of the filter case 80, and the water passage space 96 communicates with the inside of the filter case 80 through the opening 100.
下プレート90はその状態で下側、つまり底部64との間に通水空間96を形成している。
下プレート90は、フィルタケース80の外周側に貫通の開口98を有し、この開口98において通水空間96と収容空間84とを連通させている。
下プレート90は更に、フィルタケース80の内側且つ中央部に貫通の開口100を有しており、この開口100において通水空間96とフィルタケース80の内部とを連通させている。 A
In this state, the
The
The
下プレート90の図中上面側には円形の環状をなす突出部102が設けられており、この突出部102に対してフィルタケース80の図中下端が外嵌せしめられている。
そしてそのことによって、フィルタケース80が下プレート90により下側から支持された状態でその下端が下プレート90に対して、即ちケース62に対して径方向に位置決めされ固定されている。 A projectingportion 102 having a circular ring shape is provided on the upper surface side of the lower plate 90 in the drawing, and a lower end of the filter case 80 in the drawing is fitted to the protruding portion 102 in the drawing.
Thus, the lower end of thefilter case 80 is positioned and fixed with respect to the lower plate 90, that is, the case 62 in a state where the filter case 80 is supported from the lower side by the lower plate 90.
そしてそのことによって、フィルタケース80が下プレート90により下側から支持された状態でその下端が下プレート90に対して、即ちケース62に対して径方向に位置決めされ固定されている。 A projecting
Thus, the lower end of the
上記蓋体68側には、押えとしての円形の上プレート104が配置されている。
この上プレート104には、図5にも示しているように環状且つ円形の突出部106が図中上向きに起立しており、この突出部106が、蓋体68における閉鎖部69の内面(図中下面)に形成された溝108内に嵌め入れられている。
この実施形態では、蓋体68をケース本体66に対して下向きにねじ込んで行くと、その力が上プレート104に伝わって、上プレート104により活性炭押えとして働く不織布92が図中下向きに押圧される。 A circularupper plate 104 as a presser is arranged on the lid body 68 side.
As shown in FIG. 5, theupper plate 104 has an annular and circular protruding portion 106 standing upward in the figure, and this protruding portion 106 is an inner surface of the closing portion 69 (see FIG. It is fitted in a groove 108 formed in the middle and lower surface.
In this embodiment, when thelid 68 is screwed downward with respect to the case main body 66, the force is transmitted to the upper plate 104, and the nonwoven fabric 92 serving as an activated carbon presser is pressed downward in the figure by the upper plate 104. .
この上プレート104には、図5にも示しているように環状且つ円形の突出部106が図中上向きに起立しており、この突出部106が、蓋体68における閉鎖部69の内面(図中下面)に形成された溝108内に嵌め入れられている。
この実施形態では、蓋体68をケース本体66に対して下向きにねじ込んで行くと、その力が上プレート104に伝わって、上プレート104により活性炭押えとして働く不織布92が図中下向きに押圧される。 A circular
As shown in FIG. 5, the
In this embodiment, when the
図2中の(A)の部分拡大図に示しているように、この上プレート104には貫通の開口110が設けられている。
原水入口76から流入した原水は、この上プレート104の開口110を通過して第1の活性炭層88へと流入する。 As shown in the partial enlarged view of FIG. 2A, theupper plate 104 is provided with a through opening 110.
The raw water flowing in from theraw water inlet 76 passes through the opening 110 of the upper plate 104 and flows into the first activated carbon layer 88.
原水入口76から流入した原水は、この上プレート104の開口110を通過して第1の活性炭層88へと流入する。 As shown in the partial enlarged view of FIG. 2A, the
The raw water flowing in from the
尚蓋体68の裏面には、図5に示しているように閉鎖部69から下向きに突出する放射状のリブ112と、円形のリブ114とが設けられており、ここで円形のリブ114は放射状のリブ112よりも図中下向きの突出高さが低くされていて、その段差により上記の溝108が形成されている。
As shown in FIG. 5, a radial rib 112 protruding downward from the closing portion 69 and a circular rib 114 are provided on the back surface of the lid 68. Here, the circular rib 114 is a radial rib. The height of the downward protrusion in the figure is lower than that of the rib 112, and the groove 108 is formed by the step.
上記活性炭ケース82の図中下端部には嵌合部116が設けられており、この嵌合部116が、フィルタケース80の図中上端部に外嵌状態に嵌合されている。
そしてこの嵌合によって、フィルタケース80の上端部と活性炭ケース82の下端部とが、径方向に位置決めされた状態で軸方向即ち図中上下方向に連結されている。
ここでフィルタケース80と活性炭ケース82との間はシール材によって水密にシールされている。 Afitting portion 116 is provided at the lower end portion of the activated carbon case 82 in the drawing, and the fitting portion 116 is fitted to the upper end portion of the filter case 80 in the drawing state.
By this fitting, the upper end portion of thefilter case 80 and the lower end portion of the activated carbon case 82 are connected in the axial direction, that is, in the vertical direction in the figure, while being positioned in the radial direction.
Here, thefilter case 80 and the activated carbon case 82 are sealed in a watertight manner by a sealing material.
そしてこの嵌合によって、フィルタケース80の上端部と活性炭ケース82の下端部とが、径方向に位置決めされた状態で軸方向即ち図中上下方向に連結されている。
ここでフィルタケース80と活性炭ケース82との間はシール材によって水密にシールされている。 A
By this fitting, the upper end portion of the
Here, the
後述の第2の活性炭層132の図中下端部と上端部とには、それぞれ下キャップ118と上キャップ120とが設けられている。
而してこの上キャップ120には、図4にも示しているように径方向の外側の位置に第1の嵌合部122が、また内側の位置に第2の嵌合部124が設けられ、そしてその第1の嵌合部122が活性炭ケース82の上端部に外嵌状態に嵌合されている。
そしてその嵌合によって、活性炭ケース82の上端部が径方向に位置決めされている。
詳しくは、第1の嵌合部122と第2の嵌合部124との間に形成される円形の環状の溝の内部に、活性炭ケース82の上端部が図中上向きに嵌め入れられ、活性炭ケース82の上端部が径方向に位置決めされている。 Alower cap 118 and an upper cap 120 are provided at a lower end portion and an upper end portion of a second activated carbon layer 132 to be described later, respectively.
Thus, as shown in FIG. 4, theupper cap 120 is provided with a first fitting portion 122 at a radially outer position and a second fitting portion 124 at an inner position. And the 1st fitting part 122 is fitted by the upper end part of the activated carbon case 82 in the external fitting state.
And the upper end part of the activatedcarbon case 82 is positioned by radial direction by the fitting.
Specifically, the upper end of the activatedcarbon case 82 is fitted upward in the figure inside a circular annular groove formed between the first fitting portion 122 and the second fitting portion 124, and activated carbon The upper end portion of the case 82 is positioned in the radial direction.
而してこの上キャップ120には、図4にも示しているように径方向の外側の位置に第1の嵌合部122が、また内側の位置に第2の嵌合部124が設けられ、そしてその第1の嵌合部122が活性炭ケース82の上端部に外嵌状態に嵌合されている。
そしてその嵌合によって、活性炭ケース82の上端部が径方向に位置決めされている。
詳しくは、第1の嵌合部122と第2の嵌合部124との間に形成される円形の環状の溝の内部に、活性炭ケース82の上端部が図中上向きに嵌め入れられ、活性炭ケース82の上端部が径方向に位置決めされている。 A
Thus, as shown in FIG. 4, the
And the upper end part of the activated
Specifically, the upper end of the activated
この上キャップ120の中心部には、筒状をなす雄嵌合部126が上向きに設けられており、この雄嵌合部126が、浄水出口78のケース内に突出した筒状の雌嵌合部128の内部に水密に嵌入されている。
At the center of the upper cap 120, a cylindrical male fitting portion 126 is provided upward, and the male fitting portion 126 protrudes into the case of the water purification outlet 78. The portion 128 is fitted in a watertight manner.
上記フィルタケース80及び活性炭ケース82にて区画されたケース内空間の中央部の収容空間には、中空糸膜フィルタ130が図中下側に、円筒形状をなす第2の活性炭層132が図中上側に位置する状態に収容されている。
In the housing space at the center of the case space defined by the filter case 80 and the activated carbon case 82, the hollow fiber membrane filter 130 is in the lower side in the figure, and the second activated carbon layer 132 having a cylindrical shape is in the figure. It is housed in a state located on the upper side.
即ち、中空糸膜フィルタ130が第1の活性炭層88における下流側部分(原水の流れの下流側に位置する部分)に対し径方向に隣接した位置に、また第2の活性炭層132が第1の活性炭層88における上流側部分(原水の流れの上流側に位置する部分)に対し径方向に隣接した位置に位置する状態に、それらが中央部の収容空間に軸方向に並べて配置してある。
That is, the hollow fiber membrane filter 130 is located at a position adjacent in the radial direction to the downstream portion (portion located on the downstream side of the raw water flow) in the first activated carbon layer 88, and the second activated carbon layer 132 is the first activated carbon layer 132. In the activated carbon layer 88, the upstream portion (portion located upstream of the flow of raw water) is positioned adjacent to the radial direction, and they are arranged side by side in the central accommodation space in the axial direction. .
ここで中空糸膜には貫通の微細な細孔が無数に形成されていて、原水がこれら細孔を通過して膜の外から内側へと通過可能で、その際に原水中に含まれる微細な粒子を含む固形分が濾過されて除去される。
中空糸膜の細孔は極めて微細なもので、この中空糸膜フィルタ130により原水中に含まれている0.1μm程度の小さなものまで濾過により除去される。 Here, innumerable fine pores are formed in the hollow fiber membrane, and the raw water can pass from the outside to the inside of the membrane through these pores. Solids containing fine particles are filtered off.
The pores of the hollow fiber membrane are extremely fine, and the hollowfiber membrane filter 130 removes even small ones of about 0.1 μm contained in the raw water by filtration.
中空糸膜の細孔は極めて微細なもので、この中空糸膜フィルタ130により原水中に含まれている0.1μm程度の小さなものまで濾過により除去される。 Here, innumerable fine pores are formed in the hollow fiber membrane, and the raw water can pass from the outside to the inside of the membrane through these pores. Solids containing fine particles are filtered off.
The pores of the hollow fiber membrane are extremely fine, and the hollow
この実施形態において、第2の活性炭層132は粒状の活性炭86-2を予め円筒形状に成形した成形活性炭にて構成されている。
ここでは第2の活性炭層132を形成する粒状の活性炭86-2として、第1の活性炭層88を形成している活性炭86-1よりも粒子径の小さなものを用いることができる。
例えば第1の活性炭層88を形成する粒状の活性炭86-1として粒子径が0.15mm~0.30mmのものを用い、第2の活性炭層132を形成する粒状の活性炭86-2として粒子径が0.05mm~0.15mmのものを用いることができる。
但し活性炭86-2と活性炭86-1とを同じ粒度のものとなしておいても良い。 In this embodiment, the second activatedcarbon layer 132 is composed of molded activated carbon obtained by previously molding granular activated carbon 86-2 into a cylindrical shape.
Here, as the granular activated carbon 86-2 forming the second activatedcarbon layer 132, one having a smaller particle diameter than the activated carbon 86-1 forming the first activated carbon layer 88 can be used.
For example, granular activated carbon 86-1 forming the first activatedcarbon layer 88 having a particle diameter of 0.15 mm to 0.30 mm is used, and granular activated carbon 86-2 forming the second activated carbon layer 132 is used as the particle diameter. Having a thickness of 0.05 mm to 0.15 mm can be used.
However, activated carbon 86-2 and activated carbon 86-1 may have the same particle size.
ここでは第2の活性炭層132を形成する粒状の活性炭86-2として、第1の活性炭層88を形成している活性炭86-1よりも粒子径の小さなものを用いることができる。
例えば第1の活性炭層88を形成する粒状の活性炭86-1として粒子径が0.15mm~0.30mmのものを用い、第2の活性炭層132を形成する粒状の活性炭86-2として粒子径が0.05mm~0.15mmのものを用いることができる。
但し活性炭86-2と活性炭86-1とを同じ粒度のものとなしておいても良い。 In this embodiment, the second activated
Here, as the granular activated carbon 86-2 forming the second activated
For example, granular activated carbon 86-1 forming the first activated
However, activated carbon 86-2 and activated carbon 86-1 may have the same particle size.
この第2の活性炭層132の中心部には、多孔質の焼結体から成る円筒状のセラミックスフィルタ136が、その内部を浄水出口78に連通させる状態で、第2の活性炭層132に対する透水性の支持部材として設けられている。
ここでセラミックスフィルタ136は0.5μmの大きさまでの粒子を濾過によって除去可能である。
このセラミックスフィルタ136の外周面には珪藻土138がほぼ全面に亘って一体に積層されている。ここで珪藻土138はセラミックスフィルタ136に対して焼き付けられている。 At the center of the second activatedcarbon layer 132, a cylindrical ceramic filter 136 made of a porous sintered body allows water permeability to the second activated carbon layer 132 in a state where the inside thereof communicates with the water purification outlet 78. It is provided as a support member.
Here, theceramic filter 136 can remove particles up to a size of 0.5 μm by filtration.
Diatomaceousearth 138 is integrally laminated on the outer peripheral surface of the ceramic filter 136 over almost the entire surface. Here, the diatomaceous earth 138 is baked on the ceramic filter 136.
ここでセラミックスフィルタ136は0.5μmの大きさまでの粒子を濾過によって除去可能である。
このセラミックスフィルタ136の外周面には珪藻土138がほぼ全面に亘って一体に積層されている。ここで珪藻土138はセラミックスフィルタ136に対して焼き付けられている。 At the center of the second activated
Here, the
Diatomaceous
本実施形態において、セラミックスフィルタ136は抗菌性を有している。
具体的には、本実施形態においてセラミックスフィルタ136はアルミノケイ酸カルシウムの多孔質の焼結体から成っている。
詳しくは、質量%でSiO2:75~85%,Al2O3:5~10%,及びCaO:10~20%の組成を有するアルミノケイ酸カルシウムの多孔質焼結体から成っており、水分が付着したり水中に浸漬されたりしたときにCa2+イオンを抗菌成分として除々に放出することで抗菌作用を行う。 In the present embodiment, theceramic filter 136 has antibacterial properties.
Specifically, in the present embodiment, theceramic filter 136 is made of a porous sintered body of calcium aluminosilicate.
Specifically, it is composed of a porous sintered body of calcium aluminosilicate having a composition of SiO 2 : 75 to 85%, Al 2 O 3 : 5 to 10%, and CaO: 10 to 20% in terms of mass%. When it adheres or is immersed in water, it releases antibacterial effects by gradually releasing Ca 2+ ions as antibacterial components.
具体的には、本実施形態においてセラミックスフィルタ136はアルミノケイ酸カルシウムの多孔質の焼結体から成っている。
詳しくは、質量%でSiO2:75~85%,Al2O3:5~10%,及びCaO:10~20%の組成を有するアルミノケイ酸カルシウムの多孔質焼結体から成っており、水分が付着したり水中に浸漬されたりしたときにCa2+イオンを抗菌成分として除々に放出することで抗菌作用を行う。 In the present embodiment, the
Specifically, in the present embodiment, the
Specifically, it is composed of a porous sintered body of calcium aluminosilicate having a composition of SiO 2 : 75 to 85%, Al 2 O 3 : 5 to 10%, and CaO: 10 to 20% in terms of mass%. When it adheres or is immersed in water, it releases antibacterial effects by gradually releasing Ca 2+ ions as antibacterial components.
このアルミノケイ酸カルシウムは、珪質蝋石,石灰石,粘土をSiO2,Al2O3,CaOが上記の比率となるように配合し、これを焼成し焼結することで得られる。
この組成のアルミノケイ酸カルシウムは、焼成によりβ-ワラストナイト(CaO・SiO2)を効果的に多く生成する。このβ-ワラストナイトはCa2+イオンを除々に且つ長時間に亘って溶出させて弱アルカリ状態となし、そのことによって抗菌の働きをなす。 This calcium aluminosilicate is obtained by blending siliceous wax, limestone, and clay such that SiO 2 , Al 2 O 3 , and CaO have the above ratios, and firing and sintering the mixture.
The calcium aluminosilicate having this composition effectively produces a large amount of β-wollastonite (CaO · SiO 2 ) by firing. This β-wollastonite gradually dissolves Ca 2+ ions over a long period of time to form a weakly alkaline state, thereby acting as an antibacterial.
この組成のアルミノケイ酸カルシウムは、焼成によりβ-ワラストナイト(CaO・SiO2)を効果的に多く生成する。このβ-ワラストナイトはCa2+イオンを除々に且つ長時間に亘って溶出させて弱アルカリ状態となし、そのことによって抗菌の働きをなす。 This calcium aluminosilicate is obtained by blending siliceous wax, limestone, and clay such that SiO 2 , Al 2 O 3 , and CaO have the above ratios, and firing and sintering the mixture.
The calcium aluminosilicate having this composition effectively produces a large amount of β-wollastonite (CaO · SiO 2 ) by firing. This β-wollastonite gradually dissolves Ca 2+ ions over a long period of time to form a weakly alkaline state, thereby acting as an antibacterial.
この組成のアルミノケイ酸カルシウムは公知(日本国特許第3612766号に開示)のもので、本発明ではこの日本国特許第3612766号に開示のものを好適に用いることができる。
尚このアルミノケイ酸カルシウムについては同特許において開示された公知のものであるので、ここでは更に詳しい説明は省略する。 The calcium aluminosilicate having this composition is known (disclosed in Japanese Patent No. 3612766), and in the present invention, the one disclosed in Japanese Patent No. 3612766 can be suitably used.
Since this calcium aluminosilicate is a known one disclosed in the patent, further detailed explanation is omitted here.
尚このアルミノケイ酸カルシウムについては同特許において開示された公知のものであるので、ここでは更に詳しい説明は省略する。 The calcium aluminosilicate having this composition is known (disclosed in Japanese Patent No. 3612766), and in the present invention, the one disclosed in Japanese Patent No. 3612766 can be suitably used.
Since this calcium aluminosilicate is a known one disclosed in the patent, further detailed explanation is omitted here.
尚セラミックスフィルタ136は、図中上端と下端とが第2の活性炭層132から微小寸法上向きと下向きとに突出している。
そしてその上端部が上キャップ120の雄嵌合部126内部に嵌め入れられている。
また下端部が後述の下キャップ118の中央の嵌合穴140(図6中の(A)~(C)参照)に嵌め入れられている。 The upper and lower ends of theceramic filter 136 in the figure protrude from the second activated carbon layer 132 in a minute dimension upward and downward.
The upper end of theupper cap 120 is fitted into the male fitting portion 126.
Further, the lower end portion is fitted into a fitting hole 140 (see (A) to (C) in FIG. 6) in the center of thelower cap 118 described later.
そしてその上端部が上キャップ120の雄嵌合部126内部に嵌め入れられている。
また下端部が後述の下キャップ118の中央の嵌合穴140(図6中の(A)~(C)参照)に嵌め入れられている。 The upper and lower ends of the
The upper end of the
Further, the lower end portion is fitted into a fitting hole 140 (see (A) to (C) in FIG. 6) in the center of the
上記の下キャップ118は非透水性のもので(この点は上キャップ120,フィルタケース80,活性炭ケース82についても同様)、図6中の(A)~(C)に示しているように本体を構成する板状部154と、その外周部に沿って図中上向きに起立する円形の立上り部142とを有している。そして立上り部142の内側に第2の活性炭層132の下端を嵌入させる状態に、かかる下キャップ118が第2の活性炭層132の端部に装着されている。
The lower cap 118 is water-impermeable (this also applies to the upper cap 120, the filter case 80, and the activated carbon case 82), and the main body as shown in FIGS. 6A to 6C. And a circular rising portion 142 that rises upward in the drawing along the outer peripheral portion thereof. The lower cap 118 is attached to the end of the second activated carbon layer 132 so that the lower end of the second activated carbon layer 132 is fitted inside the rising portion 142.
この下キャップ118には、周方向に90°ごと隔たった4個所において、径方向外方に突出する突出部144が設けられており、これら突出部144が、図3中の(A)に示しているように活性炭ケース82の内周面に当接している。
そしてその当接によって、下キャップ118が活性炭ケース82に対して、即ち第2の活性炭層132の図中下端部が活性炭ケース82に対して、径方向に位置決状態に固定されている。
また同時に、これら突出部144の活性炭ケース82への当接によって、活性炭ケース82と第2の活性炭層132との間に環状且つ円形の通水空間148が、第2の活性炭層132周りに形成されている。 Thelower cap 118 is provided with projecting portions 144 projecting radially outward at four locations separated by 90 ° in the circumferential direction. These projecting portions 144 are shown in FIG. As shown in FIG. 2, the activated carbon case 82 is in contact with the inner peripheral surface.
By the contact, thelower cap 118 is fixed to the activated carbon case 82, that is, the lower end portion of the second activated carbon layer 132 in the figure is fixed in a radial position relative to the activated carbon case 82.
At the same time, an annular and circularwater passage space 148 is formed around the second activated carbon layer 132 between the activated carbon case 82 and the second activated carbon layer 132 by the abutment of the protrusions 144 on the activated carbon case 82. Has been.
そしてその当接によって、下キャップ118が活性炭ケース82に対して、即ち第2の活性炭層132の図中下端部が活性炭ケース82に対して、径方向に位置決状態に固定されている。
また同時に、これら突出部144の活性炭ケース82への当接によって、活性炭ケース82と第2の活性炭層132との間に環状且つ円形の通水空間148が、第2の活性炭層132周りに形成されている。 The
By the contact, the
At the same time, an annular and circular
これら突出部144には、下向きに突出して上記の中空糸膜フィルタ130の上面に当接するスペーサ部としての脚146が設けられており、それら脚146の当接により、中空糸膜フィルタ130側と下キャップ118の間、即ち第2の活性炭層132側との間に通水用の間隙150が形成されている。
更に、上記突出部144によってこの間隙150と環状の通水空間148とが、突出部144と144との間において連通している。
即ち、中空糸膜フィルタ130から流出した水が間隙150,突出部144と144との間の、図3中の(B)に示す連通路152を通じて通水空間148へと流入可能とされている。 These protrudingportions 144 are provided with legs 146 as spacer portions that protrude downward and come into contact with the upper surface of the hollow fiber membrane filter 130, and by the contact of the legs 146, the hollow fiber membrane filter 130 side is provided. A gap 150 for passing water is formed between the lower cap 118, that is, between the second activated carbon layer 132 side.
Further, thegap 150 and the annular water passage 148 communicate with each other between the protrusions 144 and 144 by the protrusion 144.
That is, the water flowing out of the hollowfiber membrane filter 130 can flow into the water flow space 148 through the communication path 152 shown in FIG. 3B between the gap 150 and the protrusions 144 and 144. .
更に、上記突出部144によってこの間隙150と環状の通水空間148とが、突出部144と144との間において連通している。
即ち、中空糸膜フィルタ130から流出した水が間隙150,突出部144と144との間の、図3中の(B)に示す連通路152を通じて通水空間148へと流入可能とされている。 These protruding
Further, the
That is, the water flowing out of the hollow
この実施形態において、第2の活性炭層132及びセラミックスフィルタ136は、原水を径方向に通過させて浄化を行う。
第2の活性炭層132は、その上端部が上キャップ120における第2の嵌合部124内部に嵌め入れられており、これにより第2の活性炭層132の上端部が上キャップ120の板状部156への当接状態で径方向に位置決めされている。
尚、第2の活性炭層132の下端部は下キャップ118の板状部154に対して当接せしめられている。 In this embodiment, the second activatedcarbon layer 132 and the ceramic filter 136 perform purification by passing raw water in the radial direction.
The upper end portion of the second activatedcarbon layer 132 is fitted into the second fitting portion 124 of the upper cap 120, whereby the upper end portion of the second activated carbon layer 132 is the plate-like portion of the upper cap 120. Positioned in the radial direction in a contact state with 156.
Note that the lower end portion of the second activatedcarbon layer 132 is brought into contact with the plate-like portion 154 of the lower cap 118.
第2の活性炭層132は、その上端部が上キャップ120における第2の嵌合部124内部に嵌め入れられており、これにより第2の活性炭層132の上端部が上キャップ120の板状部156への当接状態で径方向に位置決めされている。
尚、第2の活性炭層132の下端部は下キャップ118の板状部154に対して当接せしめられている。 In this embodiment, the second activated
The upper end portion of the second activated
Note that the lower end portion of the second activated
この実施形態では、中空糸膜フィルタ130及び第2の活性炭層132を、フィルタケース80及び活性炭ケース82とともにケース本体66の内部且つその中央部にセットした状態で、蓋体68をケース本体66に対して図中下向きにねじ込み、軸方向に組み付けると、自動的にそれらがケース本体66の底部64と蓋体68とによって、下プレート90及び上プレート104を介して軸方向に拘束され固定状態となる。即ちケース62に対して組付状態となる。
In this embodiment, the lid 68 is attached to the case body 66 in a state where the hollow fiber membrane filter 130 and the second activated carbon layer 132 are set in the center of the case body 66 together with the filter case 80 and the activated carbon case 82. On the other hand, when screwed downward in the figure and assembled in the axial direction, they are automatically restrained in the axial direction by the bottom portion 64 and the lid body 68 of the case main body 66 via the lower plate 90 and the upper plate 104 to be in a fixed state. Become. That is, it is in an assembled state with respect to the case 62.
尚、図中上プレート104と上キャップ120との間には微小な隙間が生じているが、この隙間は寸法公差によるばらつきを吸収するもので、その隙間は活性炭ケース82の嵌合部116とフィルタケース80との嵌合深さ(軸方向の深さ)よりも微小なものであり、蓋体68を組み付けた後においては、フィルタケース80と活性炭ケース82とが互いに分離することはなく、嵌合状態即ち組付状態に維持される。
In the drawing, there is a minute gap between the upper plate 104 and the upper cap 120, but this gap absorbs variation due to dimensional tolerance, and the gap is formed between the fitting portion 116 of the activated carbon case 82 and the gap. The fitting depth (depth in the axial direction) with the filter case 80 is minute, and after the lid 68 is assembled, the filter case 80 and the activated carbon case 82 are not separated from each other. The fitting state, that is, the assembled state is maintained.
本実施形態の浄水器40では、原水入口76から流入した原水は先ず第1の活性炭層88を軸方向に通過し、その後下プレート90の開口98を通過して下プレート90の下側の通水空間96へと流出する。
その通水空間96に流れ込んだ原水は、下プレート90の中央部の開口100を通過してフィルタケース80内部に流入し、そして中空糸膜を外側から内側に通過して流れ、その後中空糸膜130の上端と第2の活性炭層132、詳しくはその下端部に装着された下キャップ118との間の間隙150に流出する。
そして更に図3中の(B)に示す連通路152を通過して活性炭ケース82の内側の環状の通水空間148へと流れ込み、その後続いて第2の活性炭層132を径方向に通過して流れた後、その中心部に配置してあるセラミックスフィルタ136を同じく径方向に通過し、セラミックスフィルタ136の内側の空間へと流れ出る。
そしてこれら第1の活性炭層88,中空糸膜フィルタ130,第2の活性炭層132及びセラミックスフィルタ136を通過することによって浄化された後の浄水が、浄水出口78から流出する。 In thewater purifier 40 of the present embodiment, the raw water flowing from the raw water inlet 76 first passes through the first activated carbon layer 88 in the axial direction, and then passes through the opening 98 of the lower plate 90 and passes through the lower plate 90. It flows out into the water space 96.
The raw water that has flowed into thewater flow space 96 passes through the opening 100 at the center of the lower plate 90, flows into the filter case 80, flows through the hollow fiber membrane from the outside to the inside, and then flows through the hollow fiber membrane. It flows out to the gap 150 between the upper end of 130 and the second activated carbon layer 132, specifically, the lower cap 118 attached to the lower end portion thereof.
Further, it passes through thecommunication passage 152 shown in FIG. 3B and flows into the annular water passage space 148 inside the activated carbon case 82, and then passes through the second activated carbon layer 132 in the radial direction. After flowing, it passes through the ceramic filter 136 disposed at the center thereof in the same radial direction and flows out into the space inside the ceramic filter 136.
The purified water after being purified by passing through the first activatedcarbon layer 88, the hollow fiber membrane filter 130, the second activated carbon layer 132, and the ceramic filter 136 flows out from the purified water outlet 78.
その通水空間96に流れ込んだ原水は、下プレート90の中央部の開口100を通過してフィルタケース80内部に流入し、そして中空糸膜を外側から内側に通過して流れ、その後中空糸膜130の上端と第2の活性炭層132、詳しくはその下端部に装着された下キャップ118との間の間隙150に流出する。
そして更に図3中の(B)に示す連通路152を通過して活性炭ケース82の内側の環状の通水空間148へと流れ込み、その後続いて第2の活性炭層132を径方向に通過して流れた後、その中心部に配置してあるセラミックスフィルタ136を同じく径方向に通過し、セラミックスフィルタ136の内側の空間へと流れ出る。
そしてこれら第1の活性炭層88,中空糸膜フィルタ130,第2の活性炭層132及びセラミックスフィルタ136を通過することによって浄化された後の浄水が、浄水出口78から流出する。 In the
The raw water that has flowed into the
Further, it passes through the
The purified water after being purified by passing through the first activated
以上のように本実施形態においては、浄水器40内部に流入した原水が先ず第1の活性炭層88を通過して流れ、このとき原水中に含まれていた残留塩素が、第1の活性炭層88による吸着によって除去される。
従ってその下流側に配置してある中空糸膜フィルタ160に対し、原水中の残留塩素が作用してしまうのを防ぐことができる。 As described above, in this embodiment, the raw water that has flowed into thewater purifier 40 first flows through the first activated carbon layer 88, and the residual chlorine contained in the raw water at this time is the first activated carbon layer. It is removed by adsorption by 88.
Accordingly, it is possible to prevent residual chlorine in the raw water from acting on the hollowfiber membrane filter 160 disposed on the downstream side.
従ってその下流側に配置してある中空糸膜フィルタ160に対し、原水中の残留塩素が作用してしまうのを防ぐことができる。 As described above, in this embodiment, the raw water that has flowed into the
Accordingly, it is possible to prevent residual chlorine in the raw water from acting on the hollow
それ故中空糸膜フィルタ130Aを最も上流側に配置した従来の浄水器40Aのように原水中の残留塩素が中空糸膜に作用してその劣化を早め、中空糸膜フィルタ130Aによる濾過精度を低下せしめてしまう問題を解決でき、中空糸膜フィルタ130Aによる濾過精度を高精度に維持することができる。
Therefore, the residual chlorine in the raw water acts on the hollow fiber membrane and accelerates its deterioration as in the conventional water purifier 40A in which the hollow fiber membrane filter 130A is arranged on the most upstream side, and the filtration accuracy by the hollow fiber membrane filter 130A is reduced. The problem of damaging can be solved, and the filtration accuracy by the hollow fiber membrane filter 130A can be maintained with high accuracy.
本実施形態においては、第1の活性炭層88を通過して流れて来た原水を中空糸膜フィルタ130に通して、中空糸膜フィルタ130の濾過作用で原水中の粒子物等の濁り粒子を除去する。
第2の活性炭層132は、その中空糸膜フィルタ130を通過し粒子物等の濁り粒子の除去された原水を通過させて、吸着により原水中に含まれている有害成分を除去する。 In the present embodiment, the raw water flowing through the first activatedcarbon layer 88 is passed through the hollow fiber membrane filter 130, and turbid particles such as particles in the raw water are removed by the filtration action of the hollow fiber membrane filter 130. Remove.
The second activatedcarbon layer 132 passes through the hollow fiber membrane filter 130 and passes the raw water from which turbid particles such as particulate matter are removed, and removes harmful components contained in the raw water by adsorption.
第2の活性炭層132は、その中空糸膜フィルタ130を通過し粒子物等の濁り粒子の除去された原水を通過させて、吸着により原水中に含まれている有害成分を除去する。 In the present embodiment, the raw water flowing through the first activated
The second activated
その際、第2の活性炭層132まで流れて来た原水には粒子物が含まれておらず、活性炭86-2の表面が粒子物の付着により覆われてしまうことがないため、第2の活性炭層132は本来の浄化性能を最大限発揮することができる。
At that time, the raw water flowing to the second activated carbon layer 132 contains no particulate matter, and the surface of the activated carbon 86-2 is not covered by the adhesion of the particulate matter. The activated carbon layer 132 can maximize the original purification performance.
また第2の活性炭層132に到った原水は、第1の活性炭層88を通過した段階で残留塩素が吸着によって既に取り除かれているため、第2の活性炭層132においてはトリハロメタンやトリクロロエタンの吸着が残留塩素にて阻害されることがなく、それらの有害成分が良好に吸着されて原水中から除去される。
In addition, since the residual chlorine that has reached the second activated carbon layer 132 has already been removed by adsorption after passing through the first activated carbon layer 88, the second activated carbon layer 132 adsorbs trihalomethane or trichloroethane. Are not inhibited by residual chlorine and their harmful components are well adsorbed and removed from the raw water.
即ち、原水中に含まれているトリハロメタン,トリクロロエタン等は、浄水器40の使用初期においては第1の活性炭層88でも吸着により除去されるが、浄水器40の使用を長期間使用すると第1の活性炭層88の活性炭86-1表面が粒子物により覆われて吸着能が低下することで、更には残留塩素の吸着により、吸着力の弱いトリハロメタンやトリクロロエタンに対する吸着性能が低下することで、トリハロメタンやトリクロロエタン等の成分を第1の活性炭層88で除去し切れずに、それらが後段の中空糸膜フィルタ130を通過して下流側へと流れてしまう。
本実施形態ではその中空糸膜フィルタ130の更に下流側に、第2の活性炭層132が設けてあるため、第1の活性炭層88で取り切れなかったトリハロメタンやトリクロロエタンを第2の活性炭層132で良好に吸着し原水中から除去することができる。 That is, trihalomethane, trichloroethane, and the like contained in the raw water are removed by adsorption in the first activatedcarbon layer 88 in the initial stage of use of the water purifier 40, but if the use of the water purifier 40 is used for a long time, the first The surface of the activated carbon 86-1 of the activated carbon layer 88 is covered with particles to reduce the adsorption capacity, and further, the adsorption performance for trihalomethane and trichloroethane having a weak adsorption force due to the adsorption of residual chlorine decreases. Components such as trichloroethane are not completely removed by the first activated carbon layer 88, but they flow downstream through the hollow fiber membrane filter 130 at the subsequent stage.
In the present embodiment, since the second activatedcarbon layer 132 is provided further downstream of the hollow fiber membrane filter 130, trihalomethane and trichloroethane that cannot be removed by the first activated carbon layer 88 are removed by the second activated carbon layer 132. Adsorbs well and can be removed from raw water.
本実施形態ではその中空糸膜フィルタ130の更に下流側に、第2の活性炭層132が設けてあるため、第1の活性炭層88で取り切れなかったトリハロメタンやトリクロロエタンを第2の活性炭層132で良好に吸着し原水中から除去することができる。 That is, trihalomethane, trichloroethane, and the like contained in the raw water are removed by adsorption in the first activated
In the present embodiment, since the second activated
このように本実施形態では、前段の第1の活性炭層88と後段の第2の活性炭層132とでそれぞれ役割分担して原水中に溶存している有害成分を除去するようにしてあり、その結果本実施形態の浄水器40は、使用初期から高い浄化性能を発揮するとともに、長期に亘ってその高い浄化性能を維持することができる。
As described above, in this embodiment, the first activated carbon layer 88 in the former stage and the second activated carbon layer 132 in the latter stage each share a role and remove harmful components dissolved in the raw water. As a result, the water purifier 40 according to the present embodiment exhibits a high purification performance from the beginning of use, and can maintain the high purification performance over a long period of time.
また第2の活性炭層132は高い浄化性能を長期間維持するため、通常は、第2の活性炭層132の浄化性能が低下する以前に、これよりも前段にある中空糸膜フィルタ130が目詰まりを起し、浄水器40を流れる水の流量が少なくなる。
従って、使用者が浄水器40の目詰まりによる流量の減少を寿命の目安として浄水器40を使った場合、浄化性能が低下しているにも拘らず目詰まりを起していないことによって、浄水器40をそのまま使用し続けてしまうといったことを防ぐことができる。 In addition, since the second activatedcarbon layer 132 maintains high purification performance for a long period of time, the hollow fiber membrane filter 130 in the preceding stage is usually clogged before the purification performance of the second activated carbon layer 132 decreases. The flow rate of water flowing through the water purifier 40 is reduced.
Accordingly, when the user uses thewater purifier 40 with the decrease in the flow rate due to the clogging of the water purifier 40 as a guide for the life, the clogging is not caused even though the purifying performance is lowered. It is possible to prevent the device 40 from being used as it is.
従って、使用者が浄水器40の目詰まりによる流量の減少を寿命の目安として浄水器40を使った場合、浄化性能が低下しているにも拘らず目詰まりを起していないことによって、浄水器40をそのまま使用し続けてしまうといったことを防ぐことができる。 In addition, since the second activated
Accordingly, when the user uses the
また本実施形態では第2の活性炭層132として、粒状の活性炭86-2を接着剤等で固め成形した成形活性炭を用いており、この場合第2の活性炭層132全体を円筒形状を保持するための保持部材を不要化でき、形状保持のための部品を削減することができる。
In this embodiment, as the second activated carbon layer 132, molded activated carbon obtained by solidifying granular activated carbon 86-2 with an adhesive or the like is used. In this case, the entire second activated carbon layer 132 is maintained in a cylindrical shape. This eliminates the need for the holding member and reduces the number of parts for holding the shape.
また第2の活性炭層132の中心部には、円筒形状のセラミックスフィルタ136が支持部材として配置してあるため、成形活性炭から成る第2の活性炭層132が中心側で破壊するのを防止できるとともに、たとえその一部が崩れたとしても、セラミックスフィルタ136によってそれが浄水器40から流出してしまうのを防止することができる。
In addition, since a cylindrical ceramic filter 136 is disposed as a support member at the center of the second activated carbon layer 132, the second activated carbon layer 132 made of molded activated carbon can be prevented from being broken on the center side. Even if a part of the filter collapses, the ceramic filter 136 can prevent the ceramic filter 136 from flowing out of the water purifier 40.
更に本実施形態ではケース62を円筒形状となして、ケース62内空間の外周側の部分に第1の活性炭層88をケース62の内周面に沿って軸方向に配置するとともに、ケース内空間における第1の活性炭層88の内側の中央部に中空糸膜フィルタ130と第2の活性炭層132とを、中空糸膜フィルタ130が第1の活性炭層88における下流側部分に径方向に隣接して位置し、また第2の活性炭層132が第1の活性炭層88における上流側部分に径方向に隣接して位置するように軸方向に並べて配置し、原水入口76から流入した原水を第1の活性炭層88内部をケース62のほぼ全長に亘って軸方向に流通移動させた後、その流れを底部64近傍で折り返して中空糸膜フィルタ130へと流入させ、そしてこれを通過して第2の活性炭層132に流入及び通過させて浄化し、浄水を浄水出口78から流出させるようになしていることから、限られた大きさのケース62内で原水が浄化材を通過する距離を長くとること(接触時間を長くすること)ができ、浄水器40をコンパクト化しつつ浄化能力を高めることができる。
Further, in the present embodiment, the case 62 has a cylindrical shape, and the first activated carbon layer 88 is disposed in the axial direction along the inner peripheral surface of the case 62 in a portion on the outer peripheral side of the inner space of the case 62. The hollow fiber membrane filter 130 and the second activated carbon layer 132 are disposed in the central portion inside the first activated carbon layer 88, and the hollow fiber membrane filter 130 is adjacent to the downstream portion of the first activated carbon layer 88 in the radial direction. The second activated carbon layer 132 is arranged in the axial direction so that the second activated carbon layer 132 is positioned adjacent to the upstream side portion of the first activated carbon layer 88 in the radial direction. After the inside of the activated carbon layer 88 is axially distributed and moved over substantially the entire length of the case 62, the flow is folded back in the vicinity of the bottom 64 to flow into the hollow fiber membrane filter 130, and pass through this to pass through the second Life Since it purifies by flowing in and through the coal bed 132 and purifies the purified water through the purified water outlet 78, the distance through which the raw water passes through the purification material in the case 62 of a limited size is increased ( The contact time can be lengthened), and the purification capacity can be enhanced while making the water purifier 40 compact.
またケース62内空間の外周側部分に第1の活性炭層88をケース62の内周面に沿って軸方向に配置することで、第1の活性炭層88の容量を大とすることができるとともに軸方向長さを長く取ることができ、第1の活性炭層88による残留塩素の除去性能を長期間保持することができる。
Further, by disposing the first activated carbon layer 88 in the axial direction along the inner circumferential surface of the case 62 in the outer peripheral side portion of the inner space of the case 62, the capacity of the first activated carbon layer 88 can be increased. The axial length can be increased, and the residual chlorine removal performance by the first activated carbon layer 88 can be maintained for a long time.
また本実施形態ではケース本体66に蓋体68を組み付けることで、ケース62の内部の中空糸膜フィルタ130と第2の活性炭層132とを底部64と蓋体68とで軸方向に拘束し固定することができるため、中空糸膜フィルタ130及び第2の活性炭層132を固定するための部品数を減らすことができ、浄水器40のコンパクト化、低コスト化に寄与するとともに、それら中空糸膜フィルタ130及び第2の活性炭層132の組付けを簡単に行うことができる。
In this embodiment, the lid body 68 is assembled to the case body 66, so that the hollow fiber membrane filter 130 and the second activated carbon layer 132 inside the case 62 are axially restrained and fixed by the bottom portion 64 and the lid body 68. Therefore, the number of parts for fixing the hollow fiber membrane filter 130 and the second activated carbon layer 132 can be reduced, contributing to the downsizing and cost reduction of the water purifier 40 and the hollow fiber membranes. The filter 130 and the second activated carbon layer 132 can be easily assembled.
その他本実施形態では、円筒状に設けた第2の活性炭層132の中空糸膜フィルタ130側の端部に下キャップ118を装着し、そして下キャップ118に複数の脚146を設けて、その脚146により、中空糸膜フィルタ130側と第2の活性炭層132側との間に通水用の間隙150を形成しているため、その間隙150を形成するための特別のスペーサ部材を別途に必要とせず、所要部品数を少なくすることができる。
In addition, in this embodiment, the lower cap 118 is attached to the end of the second activated carbon layer 132 provided in a cylindrical shape on the hollow fiber membrane filter 130 side, and a plurality of legs 146 are provided on the lower cap 118. 146, a water passage gap 150 is formed between the hollow fiber membrane filter 130 side and the second activated carbon layer 132 side. Therefore, a special spacer member for forming the gap 150 is required separately. The required number of parts can be reduced.
また上記下キャップ118に設けた複数の突出部144によって第2の活性炭層132の端部を活性炭ケース82に径方向に位置決状態に固定するとともに、活性炭ケース82と第2の活性炭層132との間に環状の通水空間148を形成し、且つ通水空間148と上記の間隙150とを連通させる連通路152を、突出部144と突出部144との間に形成していることから、活性炭ケース82への第2の活性炭層132端部の固定、第2の活性炭層132周りの環状の通水空間148の形成及び上記間隙150とその通水空間148との連通路152の形成のために特別な部材を別途に必要とせず、部品点数を少なくすることができる。
In addition, the end portions of the second activated carbon layer 132 are fixed to the activated carbon case 82 in a radially positioned state by the plurality of protrusions 144 provided on the lower cap 118, and the activated carbon case 82, the second activated carbon layer 132, An annular water passage space 148 is formed between the projection portion 144 and the projection portion 144, and a communication passage 152 that connects the water passage space 148 and the gap 150 is formed. The end of the second activated carbon layer 132 is fixed to the activated carbon case 82, the annular water passage space 148 around the second activated carbon layer 132 is formed, and the communication path 152 between the gap 150 and the water passage space 148 is formed. Therefore, a special member is not required separately, and the number of parts can be reduced.
また中空糸膜フィルタ130から流出した水を間隙150へと流出させ、更にこれを連通路152を通じて第2の活性炭層132周りの環状の通水空間148へと導入するようにしていることから、中空糸膜フィルタ130からの水の流出に対する圧力抵抗を高めることなく、円滑に中空糸膜フィルタ130からの水を第2の活性炭層132周りの環状の通水空間148に導入することができる。
Further, the water flowing out from the hollow fiber membrane filter 130 is allowed to flow into the gap 150, and further introduced into the annular water passage space 148 around the second activated carbon layer 132 through the communication path 152. Water from the hollow fiber membrane filter 130 can be smoothly introduced into the annular water passage space 148 around the second activated carbon layer 132 without increasing the pressure resistance against the outflow of water from the hollow fiber membrane filter 130.
更に、第2の活性炭層132の支持部材を成す流れの末端側のセラミックスフィルタ136が抗菌性を有しているため、浄水器40外部から浄水出口78を通じて雑菌が内部に侵入する逆汚染を有効に防止することができる。
Furthermore, since the ceramic filter 136 at the end of the flow that forms the support member of the second activated carbon layer 132 has antibacterial properties, it is effective for back-contamination in which bacteria enter the inside through the water purification outlet 78 from the outside of the water purifier 40. Can be prevented.
<実験例>
上記実施形態の浄水器40と、図7(B)に示す比較例の浄水器40Aとを用いて浄水性能の比較試験を行った。
尚図7(A)に示す浄水器40は、上記図2~図6に示した浄水器と同じもので、比較例40Aの浄水器との比較のために図7(A)に併せて示したものである。 <Experimental example>
A comparative test of water purification performance was performed using thewater purifier 40 of the above embodiment and the water purifier 40A of the comparative example shown in FIG.
Thewater purifier 40 shown in FIG. 7 (A) is the same as the water purifier shown in FIGS. 2 to 6, and is shown in FIG. 7 (A) for comparison with the water purifier of Comparative Example 40A. It is a thing.
上記実施形態の浄水器40と、図7(B)に示す比較例の浄水器40Aとを用いて浄水性能の比較試験を行った。
尚図7(A)に示す浄水器40は、上記図2~図6に示した浄水器と同じもので、比較例40Aの浄水器との比較のために図7(A)に併せて示したものである。 <Experimental example>
A comparative test of water purification performance was performed using the
The
ここでは試験用の原水として、遊離残留塩素が1.0mg/L,全炭素濃度が1.0mg/L,総トリハロメタン0.1mg/Lのものを用い、そして流量2.5L/minで浄水器40,40Aに原水を流して、積算流量に対する総トリハロメタンの除去率を調べた。
Here, as raw water for testing, free residual chlorine is 1.0 mg / L, total carbon concentration is 1.0 mg / L, total trihalomethane is 0.1 mg / L, and a water purifier at a flow rate of 2.5 L / min. The raw water was poured into 40 and 40A, and the removal rate of total trihalomethane with respect to the integrated flow rate was examined.
ここで図7(B)に示す比較例の浄水器40Aでは、中空糸膜フィルタ130Aと第2活性炭層132A及びセラミックスフィルタ136Aの配置が本実施形態の浄水器40、即ち図7(A)に示す浄水器40と上下逆となっている。
また比較例の浄水器40Aでは、第1の活性炭層88Aを通過した水が、非透水性の活性炭ケース82Aの図中下部に設けた貫通の通水孔を通じて、内側の環状の通水空間148Aに流入する構成である。
尚この試験において、本実施形態の浄水器40は第1の活性炭層88における活性炭量を350cc,第2の活性炭層132の活性炭量を90ccとしている。 Here, in thewater purifier 40A of the comparative example shown in FIG. 7B, the arrangement of the hollow fiber membrane filter 130A, the second activated carbon layer 132A, and the ceramic filter 136A is the water purifier 40 of this embodiment, that is, FIG. 7A. It is upside down with the water purifier 40 shown.
Further, in thewater purifier 40A of the comparative example, the water that has passed through the first activated carbon layer 88A passes through the through water passage hole provided in the lower part of the non-permeable activated carbon case 82A in the drawing, and the inner annular water passage space 148A. It is the structure which flows into.
In this test, thewater purifier 40 of the present embodiment sets the amount of activated carbon in the first activated carbon layer 88 to 350 cc and the amount of activated carbon in the second activated carbon layer 132 to 90 cc.
また比較例の浄水器40Aでは、第1の活性炭層88Aを通過した水が、非透水性の活性炭ケース82Aの図中下部に設けた貫通の通水孔を通じて、内側の環状の通水空間148Aに流入する構成である。
尚この試験において、本実施形態の浄水器40は第1の活性炭層88における活性炭量を350cc,第2の活性炭層132の活性炭量を90ccとしている。 Here, in the
Further, in the
In this test, the
図7(B)に示す比較例の浄水器40Aにおいても、第1の活性炭層88Aの活性炭量を350ccとし、第2の活性炭層132Aの活性炭量を90ccとしている。
即ち活性炭の量は、本実施形態のものも比較例のものも同じであり、その配置が両者で異なっている。 Also in thewater purifier 40A of the comparative example shown in FIG. 7B, the activated carbon amount of the first activated carbon layer 88A is 350 cc, and the activated carbon amount of the second activated carbon layer 132A is 90 cc.
That is, the amount of activated carbon is the same in this embodiment and in the comparative example, and the arrangement differs between the two.
即ち活性炭の量は、本実施形態のものも比較例のものも同じであり、その配置が両者で異なっている。 Also in the
That is, the amount of activated carbon is the same in this embodiment and in the comparative example, and the arrangement differs between the two.
尚図7(B)に示す比較例の浄水器40Aでは、原水入口76Aから流入した原水が、先ず第1の活性炭層88Aを軸方向に通過した後、次いで第2の活性炭層132A及びその中心部のセラミックスフィルタ136Aを通過し、その後図中上側に配置してある中空糸膜フィルタ130Aを通過して、浄水出口78Aから流出する。
In the water purifier 40A of the comparative example shown in FIG. 7B, the raw water flowing in from the raw water inlet 76A first passes through the first activated carbon layer 88A in the axial direction, and then the second activated carbon layer 132A and its center. Part of the ceramic filter 136A, and then passes through the hollow fiber membrane filter 130A disposed on the upper side in the drawing, and flows out from the purified water outlet 78A.
また本実施形態の浄水器40において、第1の活性炭層88,第2の活性炭層132における粒状の活性炭は何れも粒度分布が0.15mm~0.30mmの同じものを用いた。
また中空糸膜は膜面積が0.75m2である。
一方比較例の浄水器40Aでは、第1の活性炭層88A,第2の活性炭層132Aの粒状の活性炭として、本実施形態のものと同じ粒度のものを用い、同様に中空糸膜についても本実施形態のものと同様のものを用いた。 Further, in thewater purifier 40 of the present embodiment, the granular activated carbon in the first activated carbon layer 88 and the second activated carbon layer 132 is the same having a particle size distribution of 0.15 mm to 0.30 mm.
The hollow fiber membrane has a membrane area of 0.75 m 2 .
On the other hand, in thewater purifier 40A of the comparative example, as the granular activated carbon of the first activated carbon layer 88A and the second activated carbon layer 132A, the activated carbon having the same particle size as that of the present embodiment is used. The thing of the form was used.
また中空糸膜は膜面積が0.75m2である。
一方比較例の浄水器40Aでは、第1の活性炭層88A,第2の活性炭層132Aの粒状の活性炭として、本実施形態のものと同じ粒度のものを用い、同様に中空糸膜についても本実施形態のものと同様のものを用いた。 Further, in the
The hollow fiber membrane has a membrane area of 0.75 m 2 .
On the other hand, in the
結果が図8に示してある。
このうち図8中の(A)が本実施形態の浄水器40を用いた場合の結果で、図8中の(B)が比較例の浄水器40Aを用いた場合の結果である。
尚比較例の浄水器40Aを用いたものについては、同一のものについて3回の試験を行い、それぞれの結果が示してある。 The result is shown in FIG.
Among these, (A) in FIG. 8 is a result at the time of using thewater purifier 40 of this embodiment, (B) in FIG. 8 is a result at the time of using the water purifier 40A of a comparative example.
In addition, about what used thewater purifier 40A of the comparative example, the test was performed 3 times about the same thing, and each result is shown.
このうち図8中の(A)が本実施形態の浄水器40を用いた場合の結果で、図8中の(B)が比較例の浄水器40Aを用いた場合の結果である。
尚比較例の浄水器40Aを用いたものについては、同一のものについて3回の試験を行い、それぞれの結果が示してある。 The result is shown in FIG.
Among these, (A) in FIG. 8 is a result at the time of using the
In addition, about what used the
図7(B)に示す比較例の浄水器40Aを用いた場合には、原水の積算流量10000Lの時点で、総トリハロメタン除去率が80%強であり、また10000Lに到るまでの間もその除去率は十分には高くない。
また積算流量が12000Lを超えた辺りで、総トリハロメタン除去率が急激に低下している。 When thewater purifier 40A of the comparative example shown in FIG. 7 (B) is used, the total trihalomethane removal rate is slightly over 80% at the time of the accumulated flow rate of the raw water of 10000L, and the time until it reaches 10000L. The removal rate is not high enough.
In addition, the total trihalomethane removal rate rapidly decreases when the integrated flow rate exceeds 12000 L.
また積算流量が12000Lを超えた辺りで、総トリハロメタン除去率が急激に低下している。 When the
In addition, the total trihalomethane removal rate rapidly decreases when the integrated flow rate exceeds 12000 L.
これに対して本実施形態の浄水器40を用いた場合、積算流量10000Lでなお95%以上の高い総トリハロメタン除去率を維持しており、またそこに到るまでの間も総トリハロメタン除去率が高い値を示している。
更に積算流量12000リットルを超えた辺りから総トリハロメタン除去率は低下する傾向を示すが、その低下傾向は図8中の(B)に示すものほど顕著ではない。
このことから、本実施形態の浄水器40を用いた場合、通水初期から高い浄水性能を発揮し、且つその高い浄水性能を長期間維持することが見て取れる。 On the other hand, when thewater purifier 40 of this embodiment is used, a high total trihalomethane removal rate of 95% or more is maintained at an integrated flow rate of 10000 L, and the total trihalomethane removal rate is also reached until reaching this point. It shows a high value.
Furthermore, although the total trihalomethane removal rate tends to decrease from around 12,000 liters of the integrated flow rate, the decreasing tendency is not as remarkable as that shown in FIG.
From this, when thewater purifier 40 of this embodiment is used, it can be seen that high water purification performance is exhibited from the beginning of water flow and that the high water purification performance is maintained for a long time.
更に積算流量12000リットルを超えた辺りから総トリハロメタン除去率は低下する傾向を示すが、その低下傾向は図8中の(B)に示すものほど顕著ではない。
このことから、本実施形態の浄水器40を用いた場合、通水初期から高い浄水性能を発揮し、且つその高い浄水性能を長期間維持することが見て取れる。 On the other hand, when the
Furthermore, although the total trihalomethane removal rate tends to decrease from around 12,000 liters of the integrated flow rate, the decreasing tendency is not as remarkable as that shown in FIG.
From this, when the
以上本発明の実施形態を詳述したがこれはあくまで本発明の一例示である。
例えば上記実施形態では原水入口76,浄水出口78をケース62の同じ軸方向端に設けており、このようにすることでケース62に対し軸方向の同じ側でホースの接続を行うことができ、ホースの取回しが容易で、またホースが図1に示すキャビネット2内部で広い空間を占めてしまうのを防ぐことができるといった利点が得られるが、本発明では、原水入口76と浄水出口78とをケース62の互いに軸方向の反対側に同軸上に配置するといったことも可能であり、この場合、直線上の配管途中に浄水器を接続し易い利点が得られる。 Although the embodiment of the present invention has been described in detail above, this is merely an example of the present invention.
For example, in the above embodiment, theraw water inlet 76 and the purified water outlet 78 are provided at the same axial end of the case 62. By doing so, the hose can be connected to the case 62 on the same axial side, Although the hose can be easily routed and the hose can be prevented from occupying a large space inside the cabinet 2 shown in FIG. 1, the present invention can provide advantages such as the raw water inlet 76 and the purified water outlet 78. Can be arranged coaxially on the opposite sides of the case 62 in the axial direction. In this case, an advantage of easily connecting the water purifier in the middle of the straight line is obtained.
例えば上記実施形態では原水入口76,浄水出口78をケース62の同じ軸方向端に設けており、このようにすることでケース62に対し軸方向の同じ側でホースの接続を行うことができ、ホースの取回しが容易で、またホースが図1に示すキャビネット2内部で広い空間を占めてしまうのを防ぐことができるといった利点が得られるが、本発明では、原水入口76と浄水出口78とをケース62の互いに軸方向の反対側に同軸上に配置するといったことも可能であり、この場合、直線上の配管途中に浄水器を接続し易い利点が得られる。 Although the embodiment of the present invention has been described in detail above, this is merely an example of the present invention.
For example, in the above embodiment, the
また図9に示しているように、原水入口76に逆流防止用の逆止弁160を設け、原水入口76から原水が流入するときには逆止弁160を開弁させ、逆方向の流れに対して逆止弁160を閉弁させることで、浄水器40内部の水が原水入口76から流出するのを防止することができる。
As shown in FIG. 9, a check valve 160 for preventing a backflow is provided at the raw water inlet 76, and when the raw water flows from the raw water inlet 76, the check valve 160 is opened to prevent a reverse flow. By closing the check valve 160, it is possible to prevent the water inside the water purifier 40 from flowing out from the raw water inlet 76.
このようにしておけば、原水入口76に接続すべきホース38Aを誤って浄水出口78に接続し、また浄水出口78に接続すべきホース38Bを原水入口76に接続するといった逆接続の接続ミスを防止することができる。
In this way, a connection error of reverse connection such as connecting the hose 38A to be connected to the raw water inlet 76 to the purified water outlet 78 by mistake, and connecting the hose 38B to be connected to the purified water outlet 78 to the raw water inlet 76 is avoided. Can be prevented.
このように逆接続をすると、逆止弁160の働きにより浄水器40から水が流出せず、従って万が一逆接続の接続ミスを犯した場合でも、そのことに気が付くことができ、安心して浄水器40を使用できるようになる。
If the reverse connection is made in this way, the water does not flow out of the water purifier 40 due to the function of the check valve 160. Therefore, even if a connection error is made in the reverse connection, it can be noticed, and the water purifier can be relieved. 40 can be used.
その他、本発明は上例以外の様々な形態で浄水器を構成することも可能である。
図10はその一例を示している。
この例では、上記雌嵌合部128のケース内への突出量を図2中の(A)に示すものよりも多くするとともに、上キャップ120と上プレート104との間にスポンジ162を挟み込む。またケース62の底部64から、フィルタケース80よりも外周側の位置において円筒状のリブ164を、図2中の(A)に示すリブ94よりも高く立ち上げて、その円筒状のリブ164に矩形状の切欠部166を周方向複数個所に設け、開口98から図中下向きに流出した水を、この切欠部166を通過して径方向内方に移動させる。
更にここでは第1の活性炭層88,第2の活性炭層132,セラミックスフィルタ136及び珪藻土138の高さをそれぞれ図2中の(A)に示すものよりも低くし、更に珪藻土138の厚みを図2中の(A)に示すものよりも厚くし、その外径を大径化している。 In addition, this invention can also comprise a water purifier with various forms other than an example.
FIG. 10 shows an example.
In this example, the amount of protrusion of the femalefitting portion 128 into the case is made larger than that shown in FIG. 2A, and the sponge 162 is sandwiched between the upper cap 120 and the upper plate 104. Further, a cylindrical rib 164 is raised from the bottom 64 of the case 62 at a position on the outer peripheral side of the filter case 80 so as to be higher than the rib 94 shown in FIG. Rectangular cutouts 166 are provided at a plurality of locations in the circumferential direction, and water that has flowed downward from the opening 98 in the figure is moved radially inward through the cutouts 166.
Further, the height of the first activatedcarbon layer 88, the second activated carbon layer 132, the ceramic filter 136 and the diatomaceous earth 138 is set lower than that shown in FIG. 2A, and the thickness of the diatomaceous earth 138 is further illustrated. 2 is thicker than that shown in (A), and its outer diameter is increased.
図10はその一例を示している。
この例では、上記雌嵌合部128のケース内への突出量を図2中の(A)に示すものよりも多くするとともに、上キャップ120と上プレート104との間にスポンジ162を挟み込む。またケース62の底部64から、フィルタケース80よりも外周側の位置において円筒状のリブ164を、図2中の(A)に示すリブ94よりも高く立ち上げて、その円筒状のリブ164に矩形状の切欠部166を周方向複数個所に設け、開口98から図中下向きに流出した水を、この切欠部166を通過して径方向内方に移動させる。
更にここでは第1の活性炭層88,第2の活性炭層132,セラミックスフィルタ136及び珪藻土138の高さをそれぞれ図2中の(A)に示すものよりも低くし、更に珪藻土138の厚みを図2中の(A)に示すものよりも厚くし、その外径を大径化している。 In addition, this invention can also comprise a water purifier with various forms other than an example.
FIG. 10 shows an example.
In this example, the amount of protrusion of the female
Further, the height of the first activated
以上の他、本発明では活性炭として繊維状活性炭その他のものを用いることも可能であるし、更に第1及び第2の活性炭層の間に配置されるフィルタとして中空糸膜フィルタのみならず、セラミックスフィルタを用いることも可能である。但しこの場合には、セラミックスフィルタとして0.1μmの小さな粒子までも除去可能なものを用いるのが好ましい。
その他本発明はその趣旨を逸脱しない範囲において種々変更を加えた形態で構成可能である。 In addition to the above, in the present invention, it is also possible to use fibrous activated carbon or the like as the activated carbon. Further, as a filter disposed between the first and second activated carbon layers, not only the hollow fiber membrane filter but also ceramics. It is also possible to use a filter. However, in this case, it is preferable to use a ceramic filter capable of removing even small particles of 0.1 μm.
In addition, this invention can be comprised in the form which added the various change in the range which does not deviate from the meaning.
その他本発明はその趣旨を逸脱しない範囲において種々変更を加えた形態で構成可能である。 In addition to the above, in the present invention, it is also possible to use fibrous activated carbon or the like as the activated carbon. Further, as a filter disposed between the first and second activated carbon layers, not only the hollow fiber membrane filter but also ceramics. It is also possible to use a filter. However, in this case, it is preferable to use a ceramic filter capable of removing even small particles of 0.1 μm.
In addition, this invention can be comprised in the form which added the various change in the range which does not deviate from the meaning.
本発明を詳細にまた特定の実施態様を参照して説明したが、本発明の精神と範囲を逸脱することなく様々な変更や修正を加えることができることは当業者にとって明らかである。
本出願は、2010年07月02日出願の日本特許出願・出願番号2010-152253に基づくものであり、その内容はここに参照として取り込まれる。 Although the present invention has been described in detail and with reference to specific embodiments, it will be apparent to those skilled in the art that various changes and modifications can be made without departing from the spirit and scope of the invention.
This application is based on Japanese Patent Application No. 2010-152253 filed on Jul. 2, 2010, the contents of which are incorporated herein by reference.
本出願は、2010年07月02日出願の日本特許出願・出願番号2010-152253に基づくものであり、その内容はここに参照として取り込まれる。 Although the present invention has been described in detail and with reference to specific embodiments, it will be apparent to those skilled in the art that various changes and modifications can be made without departing from the spirit and scope of the invention.
This application is based on Japanese Patent Application No. 2010-152253 filed on Jul. 2, 2010, the contents of which are incorporated herein by reference.
40 浄水器
62 ケース
64 底部
66 ケース本体
68 蓋体
76 原水入口
78 浄水出口
82 活性炭ケース
84 収容空間
86-1,86-2 活性炭
88 第1の活性炭層
118 下キャップ
120 上キャップ
130 中空糸膜フィルタ
132 第2の活性炭層
136 セラミックスフィルタ
144 突出部
146 脚
148 通水空間
150 間隙
152 連通路 40Water Purifier 62 Case 64 Bottom 66 Case Body 68 Lid 76 Raw Water Inlet 78 Purified Water Outlet 82 Activated Carbon Case 84 Storage Space 86-1, 86-2 Activated Carbon 88 First Activated Carbon Layer 118 Lower Cap 120 Upper Cap 130 Hollow Fiber Membrane Filter 132 Second activated carbon layer 136 Ceramic filter 144 Protruding portion 146 Leg 148 Water passing space 150 Gap 152 Communication path
62 ケース
64 底部
66 ケース本体
68 蓋体
76 原水入口
78 浄水出口
82 活性炭ケース
84 収容空間
86-1,86-2 活性炭
88 第1の活性炭層
118 下キャップ
120 上キャップ
130 中空糸膜フィルタ
132 第2の活性炭層
136 セラミックスフィルタ
144 突出部
146 脚
148 通水空間
150 間隙
152 連通路 40
Claims (12)
- 原水入口と浄水出口とを備えたケースの内部に浄化材を収容し、該原水入口から流入した原水を該浄化材に通して浄化し、浄水を該浄水出口から流出させる浄水器において、
前記浄化材として、前記原水入口から流入した原水の流れの上流側から下流側に第1の活性炭層,分散形成された貫通孔に原水を通して濾過作用により水中粒子を除去するフィルタ,第2の活性炭層の順序で配置し、原水を該第1の活性炭層,フィルタ,第2の活性炭層の順に通して浄化することを特徴とする浄水器。 In a water purifier that contains a purification material inside a case having a raw water inlet and a purified water outlet, purifies the raw water flowing in from the raw water inlet through the purified material, and flows purified water out of the purified water outlet.
As the purification material, a first activated carbon layer from the upstream side to the downstream side of the flow of raw water flowing in from the raw water inlet, a filter that removes underwater particles by filtration through raw water through the formed through holes, a second activated carbon It arrange | positions in the order of a layer, and purifies raw water through the order of this 1st activated carbon layer, a filter, and a 2nd activated carbon layer. - 請求項1において、前記ケースを筒状として、ケース内空間の外周側の筒状の収容空間に前記第1の活性炭層を該ケースの内周面に沿って軸方向に配置するとともに、該ケース内空間の該第1の活性炭層の内側の中央部に前記フィルタと前記第2の活性炭層とを、該フィルタを該第1の活性炭層における下流側部分に対し径方向に隣接する位置に、また第2の活性炭層を第1の活性炭層における上流側部分に対し径方向に隣接する位置に軸方向に並べて配置し、
前記原水入口から流入した原水を前記第1の活性炭層の内部を軸方向に流通移動させた後、前記フィルタを通過して前記第2の活性炭層に流入及び通過させて浄化し、浄水を前記浄水出口から流出させることを特徴とする浄水器。 2. The case according to claim 1, wherein the case is cylindrical, and the first activated carbon layer is disposed in an axial direction along an inner peripheral surface of the case in a cylindrical accommodation space on an outer peripheral side of the case inner space. The filter and the second activated carbon layer at the central portion of the inner space inside the first activated carbon layer, and the filter at a position adjacent to the downstream portion of the first activated carbon layer in the radial direction, Further, the second activated carbon layer is arranged in the axial direction at a position adjacent to the upstream side portion in the first activated carbon layer in the radial direction,
The raw water flowing in from the raw water inlet is circulated in the axial direction inside the first activated carbon layer and then purified by passing through the filter and flowing into and passing through the second activated carbon layer. A water purifier characterized by being discharged from a water purification outlet. - 請求項1,2の何れか一項において、前記ケースは、軸方向一端側に底部を、他端側に開口を有する筒状のケース本体と、該開口を閉鎖する状態に該ケース本体に軸方向に組み付けられる蓋体とに軸方向に分割してあり、該ケース本体に該蓋体を組み付けることで、該ケースの内部の前記フィルタと第2の活性炭層とを前記底部と蓋体とで軸方向に拘束し固定することを特徴とする浄水器。 The case according to any one of claims 1 and 2, wherein the case has a cylindrical case body having a bottom portion at one end in the axial direction and an opening at the other end, and the case body is pivoted to the case body in a state in which the opening is closed. The cover is assembled in the axial direction, and the cover is assembled to the case main body so that the filter and the second activated carbon layer inside the case are separated by the bottom and the cover. A water purifier characterized by being restrained and fixed in the axial direction.
- 請求項1~3の何れか一項において、前記第2の活性炭層が筒状に設けてあって、該第2の活性炭層の前記フィルタ側の端部にキャップが装着してあり、
該キャップには周方向の複数個所で外周部から該フィルタ側に突出して該フィルタの軸方向の端面に当接するスペーサ部としての複数の脚が設けてあって、該脚により、軸方向において該フィルタ側と前記第2の活性炭層側との間に通水用の間隙が形成してあることを特徴とする浄水器。 The second activated carbon layer according to any one of claims 1 to 3, wherein the second activated carbon layer is provided in a cylindrical shape, and a cap is attached to an end of the second activated carbon layer on the filter side,
The cap is provided with a plurality of legs as spacer portions that protrude from the outer peripheral portion to the filter side at a plurality of locations in the circumferential direction and abut against the axial end surface of the filter. A water purifier, wherein a water passage is formed between the filter side and the second activated carbon layer side. - 請求項4において、前記第2の活性炭層の外周側には、該第2の活性炭層を内部に収容する活性炭ケースが設けてあるとともに、前記キャップの外周部には径方向外方に突出して該活性炭ケースの内周面に当接する突出部が周方向の複数個所に設けてあって、該突出部に前記脚部が設けてあり、
該複数の突出部の前記活性炭ケースへの当接により、前記第2の活性炭層の前記端部を該活性炭ケースに対し径方向に位置決状態に固定するとともに、該活性炭ケースと該第2の活性炭層との間に環状の通水空間を形成し、且つ該通水空間と前記間隙とを連通させる連通路を該突出部と突出部との間に形成してあることを特徴とする浄水器。 5. The activated carbon case for housing the second activated carbon layer therein is provided on the outer peripheral side of the second activated carbon layer, and the outer peripheral portion of the cap protrudes radially outward. Protrusions that come into contact with the inner peripheral surface of the activated carbon case are provided at a plurality of locations in the circumferential direction, and the legs are provided at the protrusions,
The abutment of the plurality of protrusions to the activated carbon case fixes the end of the second activated carbon layer in a radially positioned state with respect to the activated carbon case, and the activated carbon case and the second activated carbon case A water purification system characterized in that an annular water passage space is formed between the activated carbon layer and a communication passage that connects the water passage space and the gap is formed between the protrusion and the protrusion. vessel. - 請求項5において、前記第2の活性炭層の中心部には、多孔質の焼結体から成る筒状のセラミックスフィルタが、内部を前記浄水出口に連通させる状態で該第2の活性炭層に対する支持部材として設けてあり、該第2の活性炭層及びセラミックスフィルタが径方向に水を通過させて浄化を行うことを特徴とする浄水器。 In Claim 5, the cylindrical ceramic filter which consists of porous sintered bodies in the center part of the said 2nd activated carbon layer is a support with respect to this 2nd activated carbon layer in the state which connected the said water purification outlet. A water purifier provided as a member, wherein the second activated carbon layer and the ceramic filter perform purification by passing water in a radial direction.
- 請求項6において、前記セラミックスフィルタが抗菌性を備えたものであることを特徴とする浄水器。 The water purifier according to claim 6, wherein the ceramic filter has antibacterial properties.
- 請求項1~7の何れか一項において、前記フィルタが0.1μmの微細な粒子まで濾過可能なものであることを特徴とする浄水器。 The water purifier according to any one of claims 1 to 7, wherein the filter is capable of filtering fine particles of 0.1 µm.
- 請求項1~8の何れか一項において、前記フィルタが中空糸膜フィルタであることを特徴とする浄水器。 The water purifier according to any one of claims 1 to 8, wherein the filter is a hollow fiber membrane filter.
- 原水入口と浄水出口とを有するケースと、
前記ケースの内部において、前記浄水出口よりも前記原水入口に近い位置に配置される第1の活性炭層と、
前記ケースの内部において、前記原水入口よりも前記浄水出口に近い位置に配置される第2の活性炭層と、
前記第1の活性炭層と前記第2の活性炭層との間に配置されるフィルタと、
を備える浄水器。 A case having a raw water inlet and a purified water outlet;
In the inside of the case, a first activated carbon layer disposed closer to the raw water inlet than the water purification outlet,
Inside the case, a second activated carbon layer disposed at a position closer to the water purification outlet than the raw water inlet,
A filter disposed between the first activated carbon layer and the second activated carbon layer;
Water purifier with - 前記第1の活性炭層は中空形状であり、
前記第2の活性炭層と前記フィルタは、前記中空形状の内部に配置されていることを特徴とする請求項10に記載の浄水器。 The first activated carbon layer has a hollow shape,
The water purifier according to claim 10, wherein the second activated carbon layer and the filter are disposed inside the hollow shape. - 前記第2の活性炭層と前記フィルタとの間には、第1の面と前記第1の面とは反対側の第2の面とを有するキャップが配置されており、
前記第1の面は前記第2の活性炭層を支持し、
前記第2の面は脚部を有し、
前記脚部が前記フィルタの端部と接触し、前記第2の活性炭層と前記フィルタとの間に通水用の間隙が形成されていることを特徴とする請求項11に記載の浄水器。 A cap having a first surface and a second surface opposite to the first surface is disposed between the second activated carbon layer and the filter,
The first surface supports the second activated carbon layer;
The second surface has legs;
The water purifier according to claim 11, wherein the leg portion is in contact with an end portion of the filter, and a gap for water passage is formed between the second activated carbon layer and the filter.
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Also Published As
Publication number | Publication date |
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CN102510836B (en) | 2014-05-28 |
CN102510836A (en) | 2012-06-20 |
JP5807258B2 (en) | 2015-11-10 |
JP2012030218A (en) | 2012-02-16 |
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