US20070209769A1 - Papermaking Machine And Papermaking Method - Google Patents
Papermaking Machine And Papermaking Method Download PDFInfo
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- US20070209769A1 US20070209769A1 US11/659,472 US65947204A US2007209769A1 US 20070209769 A1 US20070209769 A1 US 20070209769A1 US 65947204 A US65947204 A US 65947204A US 2007209769 A1 US2007209769 A1 US 2007209769A1
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- 238000000034 method Methods 0.000 title abstract description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 102
- 239000000725 suspension Substances 0.000 claims abstract description 17
- 230000005494 condensation Effects 0.000 claims abstract description 11
- 238000009833 condensation Methods 0.000 claims abstract description 11
- 238000011144 upstream manufacturing Methods 0.000 claims description 20
- 238000007789 sealing Methods 0.000 claims description 11
- 238000007664 blowing Methods 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 3
- 230000018044 dehydration Effects 0.000 description 77
- 238000006297 dehydration reaction Methods 0.000 description 77
- 230000000694 effects Effects 0.000 description 22
- 238000010276 construction Methods 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 238000010586 diagram Methods 0.000 description 7
- 238000005192 partition Methods 0.000 description 7
- 238000009434 installation Methods 0.000 description 3
- 239000012466 permeate Substances 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 229920001342 Bakelite® Polymers 0.000 description 1
- 239000004637 bakelite Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000013013 elastic material Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
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- 239000011148 porous material Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
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Classifications
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/48—Suction apparatus
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/48—Suction apparatus
- D21F1/50—Suction boxes with rolls
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F9/00—Complete machines for making continuous webs of paper
- D21F9/003—Complete machines for making continuous webs of paper of the twin-wire type
Definitions
- the present invention relates to a papermaking machine and papermaking method that make continuous paper by removing moisture while making it travel a layer of paper stock.
- patent document 1 discloses a papermaking machine equipped with a steam box 60 for supplying steam to the upper side of wet paper web 1 .
- the steam box 60 is arranged over a path of travel in the final part of a former (also referred to as a forming part or paper layer forming part).
- steam from a steam generator 10 is supplied to the steam box 60 through a steam conduit.
- the steam touches the wet paper web 1 held on a wire 30 and condenses, whereby heat is transferred to the wet paper 1 .
- the wet paper web 1 will be in a state before completion of dehydration, that is, a state in which minute interstices have been formed by dehydration, or a porous state.
- a suction box 70 By suctioning the under side of the wet paper web 1 through the wire 30 by a suction box 70 , steam enters such interstices or pores and permeates into the wet paper web 1 .
- the latent heat of the steam is converted to the sensible heat of water, whereby the wet paper web 1 is raised in temperature and the dehydration rate rises.
- the dehydration rate of the wet paper web 1 traveling through the former is not uniform.
- the widthwise central portion of the wet paper web 1 is lower in dehydration rate than the widthwise right and left end portions.
- FIG. 8 ( b ) there has been developed a technique in which, in order to cause the widthwise central portion of the wet paper web 1 whose dehydration rate is relatively low to touch more steam than the widthwise right and left portions, by widthwise dividing the steam box 60 into a plurality of steam supply chambers 61 , and suitably adjusting valves 11 corresponding to each steam supply chamber 61 , the widthwise central steam chambers 61 are supplied with more steam than the widthwise right and left steam chambers 61 .
- patent document 2 discloses a technique in which by causing steam to touch wet paper, the wet paper is raised in temperature.
- Patent document 1 Japanese patent laid-open publication No. Sho 55-137293
- Patent document 2 U.S. Pat. No. 5,149,401
- the inventors have made various investigations and experiments with respect to a mechanism of raising the dehydration rate of wet paper web by heating the wet paper web with steam and found the following facts. That is, there are cases where even if the supply of steam is increased in order to further raise the dehydration rate, conversely the dehydration rate will be reduced. A possible cause is that an increase in the supply of steam increases the quantity that steam condenses into water.
- the present invention has been made in view of the problem described above. Accordingly, it is the primary object of the present invention to provide a papermaking machine and papermaking method that are capable of dehydrating a layer of paper stock with better efficiency.
- the papermaking machine of the present invention as set forth in claim 1 is a papermaking machine for making paper web by holding a paper stock suspension jetted from a head box into the shape of a layer, and removing moisture while traveling the paper stock layer.
- the papermaking machine comprises: steam type heating means, provided in a moisture removing part as heating means for heating the paper stock layer (wet paper web) to accelerate the moisture removal, for supplying steam to the paper stock layer and heating the paper stock layer by condensation of the steam; and adjustment means for adjusting the supply of the steam performed by the steam type heating means, on the basis of a stock concentration of the paper stock layer detected when passing through the steam type heating means, so that the paper stock layer reaches a preset target temperature.
- the steam used herein is not limited to saturated steam, but may be heated steam, wet air, etc.
- the supply of steam may be adjusted based on the information detected.
- the supply of steam may be adjusted based on the stock concentration obtained beforehand.
- the papermaking machine of the present invention as set forth in claim 2 is characterized in that, in the construction as set forth in claim 1 , the moisture removing part is a former (also called a forming part or paper layer forming part) which forms a layer of paper by holding the paper stock suspension jetted from the head box into the shape of a layer, and removing moisture while traveling the paper stock layer, or a press part which further removes moisture by applying pressure to the paper stock layer formed into the paper layer by the former.
- a former also called a forming part or paper layer forming part
- the papermaking machine of the present invention as set forth in claim 3 is characterized in that, in the construction as set forth in claim 2 , the forming part is constructed as twin wire formers equipped with wires on both sides of the paper stock layer. Note that the present invention is not always limited to twin wires, but may be applied to a long wire former or on-top former which holds only one side of a paper stock layer.
- the papermaking machine of the present invention as set forth in claim 4 is characterized in that, in the construction as set forth in claim 3 , the steam type heating means is provided with a steam box for guiding the supply of steam to the paper stock layer.
- the steam box is arranged so that the fringe of its tip opening abuts the wire or is very near the wire.
- the papermaking machine of the present invention as set forth in claim 5 is characterized in that, in the construction as set forth in claim 4 , the fringe of the tip opening of the steam box is provided with seal means for sealing the steam box.
- the papermaking machine of the present invention as set forth in claim 6 is characterized in that, in the construction as set forth in claim 5 , the seal means is a seal member which is attached to the fringe of the tip opening of the steam box and abuts the wire.
- the papermaking machine of the present invention as set forth in claim 7 is characterized in that, in the construction as set forth in claim 5 , the seal means is a gas jet device which is provided upstream in the traveling direction of the paper stock layer relative to the fringe of the tip opening of the steambox, and suppresses incursion of wake of the paper stock layer into the steam box by jetting gas.
- the gas jet device preferably jets gas toward the upstream side at a jet angle which is about 15 to 40° to wet paper web.
- the papermaking machine of the present invention as set forth in claim 8 is characterized in that, in the construction as set forth in any one of claims 4 to 7 , it further includes a suction box for suctioning steam jetted from the steam box toward a side opposite to the steam box across the paper stock layer.
- the papermaking machine of the present invention as set forth in claim 9 is characterized in that, in the construction as set forth in claim 8 , a downstream end of the suction box in the traveling direction of the paper stock layer is arranged downstream relative to a downstream end of the steam box in the traveling direction of the paper stock layer.
- the papermaking machine of the present invention as set forth in claim 10 is characterized in that, in the construction as set forth in claim 8 or 9 , it further includes another suction box arranged on the side opposite to the steam box across the paper stock layer and downstream in the traveling direction of the paper stock layer.
- the papermaking machine of the present invention as set forth in claim 11 is characterized in that, in the construction as set forth in claim 10 , the suction force of the downstream suction box in the traveling direction of the paper stock layer is set larger than that of the upstream suction box.
- the papermaking machine of the present invention as set forth in claim 12 is characterized in that, in the construction as set forth in any one of claims 8 to 11 , the steam box is divided into a plurality of parts in the width direction of the paper stock layer and the suction box is divided into a plurality of parts so as to correspond to the divided parts of the steam box.
- a jet of steam and suction of steam are adjustable for each of the divided parts.
- the papermaking machine of the present invention as set forth in claim 13 is characterized in that, in the construction as set forth in any one of claims 1 to 12 , the steam supplied by the steam type heating means heats the paper stock layer by acting on the paper stock layer as a collision jet.
- the papermaking machine of the present invention as set forth in claim 14 is characterized in that, in the construction as set forth in any one of claims 1 to 13 , it further includes control means for automatically adjusting the adjustment means.
- the papermaking machine of the present invention as set forth in claim 15 is characterized in that, in the construction as set forth in claim 14 , it further includes stock concentration detecting means, provided in the vicinity of the steam type heating means, for detecting a stock concentration of the paper stock layer when passing through the steam type heating means.
- the control means controls the supply of steam performed by the steam type heating means, on the basis of information detected by the stock concentration detecting means, so that the paper stock layer is raised to the target temperature.
- the above-mentioned stock concentration detecting means is, for example, moisture percentage sensor, and the stock concentration can be estimated by moisture percentage of paper stock layer detected by the moisture percentage sensor.
- the papermaking machine of the present invention as set forth in claim 16 is characterized in that, in the construction as set forth in any one of claims 1 to 15 , it further includes air jet type heating means for blowing high-temperature air against the paper stock layer and heating the paper stock layer by a collision jet of the high-temperature air, provided as heating means for heating the paper stock layer, downstream in the traveling direction of the paper stock layer relative to a position at which the steam type heating means is installed.
- the papermaking machine of the present invention as set forth in claim 17 is characterized in that, in the construction as set forth in any one of claims 1 to 16 , the heating means comprises first heating means for performing heating on one side of the paper stock layer, and second heating means for performing heating on the other side of the paper stock layer.
- the papermaking method of the present invention as set forth in claim 18 is a papermaking method of making paper web by holding a paper stock suspension jetted from a head box into the shape of a layer, and removing moisture while traveling the paper stock layer.
- the papermaking method comprises a step of supplying steam to the paper stock layer at a heated position and heating the paper stock layer by condensation of the steam, in such a way that the paper stock layer reaches a preset target temperature, and a step of suctioning and removing moisture from the paper stock layer.
- the steam used in this method is not limited to saturated steam, but may be heated steam, wet air, etc.
- the adjustment means adjusts the supply of the steam performed by the steam type heating means, on the basis of a stock concentration of the paper stock layer detected when passing through the steam type heating means, so that the paper stock layer reaches a preset target temperature. Therefore, the paper stock layer can be raised in temperature and dehydrated with better efficiency. As a result of this, the dehydration rate can be raised.
- the steam type heating means is provided with a steam box for guiding the supply of steam to the paper stock layer.
- the steam box is arranged so that the fringe of its tip opening abuts the wire or is very near the wire. Therefore, steam can be supplied to the paper stock layer with good efficiency.
- the fringe of the tip opening of the steam box is provided with seal means for sealing the steam box. Therefore, steam can be supplied to the paper stock layer with better efficiency.
- the seal means is a seal member which is attached to the fringe of the tip opening of the steam box and abuts the wire. Therefore, sealing of the steam box can be enhanced, whereby steam can be supplied to the paper stock layer with good efficiency.
- the seal means is a gas jet device which is provided upstream in the traveling direction of the paper stock layer relative to the fringe of the tip opening of the steam box, and suppresses incursion of wake of the paper stock layer into the steam box by jetting gas. Therefore, incursion of wake into the steam box can be reliably suppressed, whereby steam can be supplied to the paper stock layer with good efficiency.
- the suction box suctions steam jetted from the steam box toward a side opposite to the steam box across the paper stock layer. Therefore, high-temperature water condensed on the surface of the paper stock layer is able to permeate through the paper stock layer. This makes it possible to reliably raise the temperature of the entire paper stock layer and dehydrate the entire paper stock layer.
- a downstream end of the suction box in the traveling direction of the paper stock layer is arranged downstream relative to a downstream end of the steam box in the traveling direction of the paper stock layer. Therefore, moisture in the paper stock layer raised in temperature can be further removed, resulting in a further rise in the dehydration rate.
- the papermaking machine of the present invention in addition to the above-mentioned suction box, the papermaking machine further includes another suction box arranged on the side opposite to the steam box across the paper stock layer and downstream in the traveling direction of the paper stock layer. Therefore, the dehydration rate can be further raised.
- the suction force of the downstream suction box is set larger than that of the upstream suction box. Therefore, water in the paper stock layer raised in temperature by the upstream steam box can be further removed, resulting in a further rise in the dehydration rate.
- the steam box is divided into a plurality of parts in the width direction of the paper stock layer and the suction box is divided into a plurality of parts so as to correspond to the divided parts of the steam box, and a jet of steam and a suction of steam are adjustable for each of the divided parts. Therefore, the dehydration rate can be adjusted for each of the divided parts.
- the steam supplied by the steam type heating means heats the paper stock layer by acting on the paper stock layer as a collision jet. Therefore, the paper stock layer can be raised in temperature and dehydrated with better efficiency.
- the papermaking machine further includes control means for automatically adjusting the adjustment means. Therefore, the supply of steam can be automatically adjusted.
- the control means controls the supply of steam performed by the steam type heating means, on the basis of information detected by the stock concentration detecting means, so that the paper stock layer is raised to the target temperature. Therefore, the supply of steam can be adjusted so that an optimum dehydration rate is obtained.
- the papermaking machine further includes air jet type heating means for blowing high-temperature air against the paper stock layer and heating the paper stock layer by a collision jet of the high-temperature air.
- the air jet type heating means is provided as heating means for heating the paper stock layer, downstream in the traveling direction of the paper stock layer from a position at which the steam type heating means is installed. Therefore, the paper stock layer raised in temperature by the steam type heating means can be further raised in temperature and dehydrated, resulting in a further rise in the dehydration rate.
- the heating means comprises first heating means for performing heating on one side of the paper stock layer, and second heating means for performing heating on the other side of the paper stock layer. Therefore, it is possible to evenly dehydrate both sides of the paper stock layer.
- the papermaking method of the present invention in such a way that the paper stock layer reaches a preset target temperature, steam is supplied to the paper stock layer at a heated position and the paper stock layer is heated by condensation of the steam. Thereafter, moisture is suctioned and removed from the paper stock layer. Therefore, the paper stock layer can be raised in temperature and dehydrated with better efficiency. This can raise the dehydration rate.
- FIG. 1 is a schematic diagram showing a papermaking machine according to a first embodiment of the present invention
- FIGS. 2 ( a ) and 2 ( b ) schematically show a steam box and a suction box according to the first embodiment of the present invention, FIG. 2 ( a ) being a sectional view taken along the direction in which wet paper web travels and FIG. 2 ( b ) being a sectional view taken along line A-A of FIG. 2 ( a );
- FIG. 3 is a graph showing how the dehydration rate (effect of accelerating dehydration) in the first embodiment of the present invention varies with respect to the stock concentration of wet paper web;
- FIG. 4 is a schematic diagram showing a papermaking machine according to a second embodiment of the present invention.
- FIG. 5 is a schematic diagram showing a papermaking machine according to a third embodiment of the present invention.
- FIG. 6 is a schematic diagram showing a papermaking machine according to a fourth embodiment of the present invention.
- FIG. 7 is a schematic diagram showing a papermaking machine according to a fifth embodiment of the present invention.
- FIGS. 8 ( a ) and 8 ( b ) schematically show a steam box and a suction box according to a conventional papermaking machine, FIG. 8 ( a ) being a sectional view taken along the direction in which wet paper web travels and FIG. 8 ( b ) being a sectional view taken along line A-A of FIG. 8 ( a ).
- FIGS. 1 to 3 are used for explaining a papermaking machine constructed in accordance with a first embodiment of the present invention.
- FIG. 1 is a schematic diagram showing the papermaking machine.
- FIGS. 2 ( a ) and 2 ( b ) are diagrams schematically showing a steam box and a suction box.
- FIG. 2 ( a ) is a sectional view taken along the direction in which wet paper web travels
- FIG. 2 ( b ) is a sectional view taken along line A-A of FIG. 2 ( a ).
- FIG. 3 is a graph showing how the dehydration rate (effect of accelerating dehydration) varies with respect to the stock concentration of wet paper web.
- the papermaking machine of the first embodiment adopts twin wire formers, as shown in FIG. 1 .
- a pulp suspension (paper stock suspension) 1 a is jetted and supplied from a head box 2 to a slit between twin wires 3 a and 3 b , the pulp suspension 1 a becomes a wet paper web (a paper stock layer) 1 by being held into the shape of layer between the twin wires 3 a and 3 b .
- This wet paper web 1 is dehydrated by a forming roll 4 which performs dehydration by tension of the wires 3 a and 3 b ; a blade shoe 5 which performs dehydration by curving a path of travel; and so forth.
- the wet paper web 1 Downstream of the blade shoe 5 , the wet paper web 1 is raised in temperature by a steam box 6 and is suctioned and dehydrated by a suction box 7 installed across the wet paper web 1 from the steam box 6 .
- a steam box 6 and suction box 7 in the first embodiment will be described in further detail.
- the steam box (steam type heating means) 6 as heating means is equipped with a steam box main body 6 a , a heat retaining body 6 b , and a seal member (seal means) 6 c.
- the steam box main body 6 a has, for example, a machine length of about 100 to 1000 mm in the traveling direction of the wet paper web 1 , and the internal space is divided into a plurality of steam supply chambers 6 e in the width direction of the wet paper web 1 by partition walls 6 d .
- Each of the steam supply chambers 6 e divided by the partition walls 6 d has a steam introducing port 6 f for taking in steam from a steam generator 10 , and a tip opening 6 g facing the wire 3 a .
- the tip opening 6 g of the steam box main body 6 a has a seal member 6 c attached thereto, which abuts the wire 3 a.
- the wires 3 a , 3 b and wet paper web 1 can be heated to about 40 to 100° C. Note that it is also possible to cause the supplied steam to act on the wet paper web 1 as a collision jet. This can heat the wet paper web 1 efficiently.
- the heat retaining body 6 b is, for example, a heat retaining structure with a heat insulating material or heat insulating layer, or a heating device such as an electric heater, a heating steam jacket, a high-temperature air jacket, etc., and is attached to the outside wall of the steam box main body 6 a so that it can retain the heat of the steam box main body 6 a .
- This can prevent steam condensation and dew condensation from occurring on the inside wall surface of the steam box main body 6 a (i.e., the inside wall surface of the steam supply chamber 6 e ).
- the seal member 6 c is attached to the fringe of the tip opening 6 g of the each of steam supply chambers 6 e so as to abut the wire 3 a , and functions to seal the steam box main body 6 a and each of the steam supply chambers 6 e . This ensures sealing of the interior of the steam box main body 6 a and interior of each of the steam supply chambers 6 e .
- an elastic material such as rubber is suitable from the viewpoint of sealing performance, but since heat-resisting property is required, a heating-resisting material such as bakelite is also suitable.
- a material, such as heat-resisting rubber, which has both elasticity and heat-resisting property is more suitable.
- Supply pipes connected to each of the steam supply chambers 6 e are provided with valves (adjustment means) 11 , through which steam is supplied from the steam generator 10 to the steambox 6 .
- valves (adjustment means) 11 By controlling the opening and closing operation of each valve 11 with a controller 12 , the supply of steam into the steam supply chambers 6 e can be separately adjusted.
- the steam used in the first embodiment may be any of saturated steam, heated steam, and wet air.
- the suction box 7 has, for example, the same machine length as the steambox 6 or a machine length shorter than the steam box 6 , and the interior space is divided into a plurality of suction chambers 7 e at intervals of the same width as the steam box main body 6 a in the width direction of the wet paper web 1 by partition walls 7 d .
- Each of the suction chambers 7 e divided by the partition walls 7 d has a suction port 7 f connected to a suction device (not shown), and an tip opening 7 g facing the wire 3 b .
- the suction box 7 is installed so that the tip opening 7 g abuts the surface of the wire 3 b.
- the width of the steam box 6 and the width of the wires 3 a , 3 b are set equal to each other.
- the width of the steam box 6 is larger than that of the wires 3 a and 3 b
- the width of the suction box 7 is approximately the same as the width of the steam box 6 , so this suction box 7 fulfills the function of the aforementioned member.
- the wet paper web 1 is heated and dehydrated. Specifically, the steam supplied into the steam box 6 is condensed into high-temperature water in the vicinity of the surface of the wire 3 a and surface of the wet paper web 1 . Then, the high-temperature water gets into the wet paper web 1 by the suction operation of the suction box 7 , the entire wet paper web 1 is raised in temperature by the heat transfer of the high-temperature water, and by suctioning the moisture in the wet paper web 1 by the suction box 7 , the wet paper web 1 is dehydrated.
- the temperature raising process is being performed and the wet paper web 1 entering the steam box 6 is progressively raised in temperature within the steam box 6 , but a time lag occurs until the whole of the wet paper web 1 is raised in temperature.
- the wet paper web 1 in which the effect of dehydration has become higher by being raised in temperature within the steam box 6 is further dehydrated by a suction roll 8 and a suction box 9 installed downstream of the steam box 6 . This makes it possible to perform dehydration with better efficiency, resulting in a rise in the dehydration rate.
- the inventors have investigated how the dehydration rate varies with respect to the paper stock concentration of the wet paper web 1 under a certain suction condition. The results are shown in FIG. 3 .
- FIG. 3 shows dehydration raising characteristics due to the temperature raising effect in the case of a large supply of steam and the case of a low supply of steam, and a dehydration reducing characteristic due to dehydration resistance in the case where suction pressure is fixed.
- the characteristics of the dehydration accelerating effect by steam supply are shown by lines M 1 and M 2 in FIG. 3 . That is, in both the case of a large supply of steam and the case of a low supply of steam, the higher the stock concentration, the less the moisture and the lower the mass of the wet paper web 1 , therefore the heat capacity becomes low, so that the temperature of the wet paper web 1 is considerably raised, resulting in a rise in the dehydration rate (i.e., the dehydration rate is raised by the temperature raising effect of the wet paper web 1 ). From the comparison of lines M 1 and M 2 it follows that the case of a large supply of steam (M 1 ) has a higher dehydration rate than the case of a low supply of steam (M 2 ).
- this dehydration accelerating effect has a mountainous characteristic that rises up to a certain stock concentration and then drops gradually.
- the dehydrating speed v has an inversely proportional relation to the water viscosity ⁇ .
- the water viscosity ⁇ becomes smaller as the temperature of the wet paper web becomes higher. That is, there is a relation in which the dehydrating speed v becomes faster as the temperature of the wet paper web becomes higher.
- the wet paper web 1 is raised in temperature by heated steam and therefore the dehydrating speed becomes faster and the dehydration rate becomes higher, but at the same time, an increase in the stock concentration increases resistance to dehydration.
- the dehydration accelerating effect has a mountainous characteristic shown in FIG. 3 , and the most efficient stock concentration exists according to the state of steam supply.
- the controller 12 adjusts the opening and closing operation of each valve 11 and controls the state of steam supplied to each steam supply chamber 6 e in real time, based on information detected by each moisture percentage sensor 13 , so that the temperature of the wet paper web 1 passing through each steam supply chamber 6 e becomes a target wet paper temperature (which is a target temperature set beforehand according to the stock concentration of the wet paper web 1 ).
- the steam supply chamber 6 e is disposed at a certain spot, and the reference stock concentration of the wet paper web 1 coming to this spot is assumed to be 12%. If the stock concentration of the wet paper web 1 detected by the moisture percentage sensor 13 is 10%, the controller 12 controls the valve 11 so that the supply of steam is increased. If the stock concentration of the wet paper web 1 detected by the moisture percentage sensor 13 is 14%, the controller 12 controls the valve 11 so that the supply of steam is reduced.
- both sides of the wet paper web 1 are supported by twin wires 3 a and 3 b and the steam box 6 touches the wire 3 a , whereby the aforementioned gap can be eliminated without damaging the wet paper web 1 and, compared with the prior art, the quantity of steam discharged can be suppressed. That is, since steam loss can be prevented, steam can be efficiently utilized.
- the steam box has to be installed at a position before completion of dehydration (i.e., near the former outlet), but according to the present invention, it is possible to install it more upstream. This makes it possible to accelerate the dehydration of the wet paper web 1 in the former from the upstream side. Moreover, as described above, because the papermaking machine of the first embodiment performs optimum steam supply according to the stock concentration of the wet paper web 1 , the heating and dehydration efficiency can be raised. Therefore, it becomes possible to perform the dehydration in the former with great efficiency, and consequently, the former can be made compact, whereby space to install the former can be saved.
- the heat transfer efficiency of the papermaking machine of the first embodiment by steam condensation is about 25 times as high as that of the conventional papermaking machine by steam permeation and is extremely high compared with the prior art. Therefore, a rise in the temperature of the wet paper web 1 by the conventional papermaking machine is so insufficient that even if the suction box 9 is provided downstream of the suction box 70 , a high effect of dehydration cannot be obtained. On the other hand, in the papermaking machine of the first embodiment, a rise in the temperature of the wet paper web 1 is so sufficient that a high effect of dehydration is obtained by the suction roll 8 and suction box 14 arranged downstream of the suction box 7 . Thus, it is possible to accelerate dehydration of the wet paper web 1 .
- the internal spaces of the steam box 6 and suction box 7 are divided into several parts so that the jetted state of steam and the suctioned state of steam can be adjusted for each of the divided regions.
- a stock concentration difference in the width direction of the wet paper web 1 is practically negligible, it is not necessary to divide these spaces (i.e., the partition walls 6 d and 7 d are not needed).
- a representative stock concentration e.g., at the laterally central portion of the wet paper web 1
- the supply of steam required for the wet paper web 1 to rise to the target wet paper web temperature may be set.
- a single moisture percentage sensor 13 may be installed at a single spot in the width direction of the wet paper web 1 (e.g., at the laterally central portion of the wet paper web 1 ), and based on a stock concentration obtained by this moisture percentage sensor 13 , the supply of steam required for the wet paper web 1 to rise to the target wet paper web temperature may be set.
- valve opening and closing operations of the valves 11 are automatically adjusted based on information detected from the moisture percentage sensors 13 by the controller 12
- the valve opening and closing operations may be manually performed by the operator, based on information detected from the moisture percentage sensors 13 .
- the first embodiment is constructed such that the steam box 6 and suction box 7 are provided in the former that forms a layer of paper, they may be provided in a press part (which applies pressure to the paper stock layer formed by the former to further remove moisture) arranged downstream of the former.
- the papermaking machine of the second embodiment in addition to the construction of the first embodiment, is equipped with another suction box 7 A, which is arranged in close proximity to the downstream side of the suction box 7 .
- the temperature raising process is being performed and the wet paper web 1 traveling through the steam box 6 is gradually raised in temperature within the steam box 6 , but a time lag occurs until the whole of the wet paper web 1 is raised in temperature.
- the suction box 7 A suctions the wet paper web 1 in which the effect of dehydration has become higher, further dehydration can be performed, even if its suction force is equal to that of the suction box 7 .
- the papermaking machine of the third embodiment is constructed such that in the construction of the first embodiment, the downstream end of the suction box 7 is arranged downstream relative to the downstream end of the steam box 6 .
- the suction box 7 according to the first embodiment is arranged so that it is shifted downstream by a predetermined distance.
- the upstream end of the suction box 7 of the first embodiment fixed at its original position, only the downstream end of the suction box 7 may be positioned downstream relative to the downstream end of the steam box 6 .
- the papermaking machine of the fourth embodiment is constructed such that in the construction of the first embodiment, it is further equipped with an air jet device (seal means) 14 that jets air toward the upstream side, in the vicinity of the upstream end of the steam box 6 . It is preferable that the air jet device 14 jet air toward the upstream side at an angle ⁇ of about 15 to 40 degrees relative to the wet paper web 1 .
- the upstream seal member 6 c of the steam box 6 may be omitted.
- the papermaking machine of the fifth embodiment is equipped with two sets of units comprising a steam box 6 and a suction box 7 of the first embodiment.
- the fifth embodiment is provided with a first unit comprising a steam box (first heating means) 6 and a suction box 7 , and a second unit comprising a steam box (second heating means) 6 ′ and a suction box 7 ′.
- the steam box 6 supplies steam to one side of the wet paper web 1
- the steam box 6 ′ supplies steam to the other side of the wet paper web 1 . This makes it possible to dehydrate both sides of the wet paper web 1 evenly, whereby it becomes possible to manufacture products in which both sides are so even that a difference between them is slight.
- the installation position of the steam box 6 can be determined beforehand in making a design, and the stock concentration (the reference stock concentration) of the wet paper web 1 at the installation position can also be predicted in the stage of the design. Therefore, in papermaking machines, steam supply may be performed so that the temperature of the wet paper web 1 becomes a target wet paper temperature which corresponds to the reference stock concentration.
- the actual stock concentration of the wet paper web 1 is detected by the moisture percentage sensor 13 , and when there is a difference between the stock concentration of the wet paper web 1 passing through the steam box 6 and the aforementioned reference stock concentration, the supply of steam to the steam box 6 is adjusted by feedback control in order to correct for this difference.
- a constant supply of steam may be continuously performed in an open loop without providing the moisture percentage sensor 13 .
- steam supply may be adjusted so that the wet paper web 1 reaches the target wet paper web temperature. Even in this case, the wet paper web 1 can be raised in temperature and dehydrated with good efficiency, resulting in arise in the dehydration rate.
- air jet type heating means for blowing high-temperature air against the wet paper web 1 and heating the wet paper web 1 by a collision jet of high-temperature air.
- the steam box 6 Since the steam box 6 has a higher effect if it is employed when the moisture percentage of the wet paper 1 is high, it is preferable to install the steam box 6 in the former in which the moisture percentage of the wet paper 1 is high, but it may be installed in the upstream portion (near the inlet) of the press part. Because the air jet type heating means has a higher effect if it is employed in a state lower than the moisture percentage of the wet paper web 1 in the former, it is preferable to install the air jet type heating means in the press part which is lower in the moisture percentage of the wet paper web 1 than the former, but it maybe installed in the downstream portion (near the outlet) of the former.
- the above-described embodiments are constructed such that the seal member 6 c abuts the wire 3 a in order to ensure sealing of the steam box 6 .
- the seal member 6 c may be provided in close proximity to the wire 3 a . If sealing of the steam box 6 is ensured by causing the tip opening 6 g of the steam box 6 to abut the wire 3 a or arranging the tip opening 6 g in close proximity to the wire 3 a , there is no need to provide the seal member 6 c.
- the present invention is not limited to twin wires, but may be applied to a long wire type former or on-top former which holds only one side of the paper stock layer.
- the present invention is applicable to a papermaking machine and papermaking method for making paper web by holding a paper stock suspension into the shape of a layer, and removing moisture while making this paper stock layer travel.
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Abstract
The present invention relates to a papermaking machine and papermaking method that make paper web by removing moisture while making a paper stock layer travel, and the object of the invention is to dehydrate the paper stock layer more efficiently.
A papermaking machine for making continuous paper web by holding a paper stock suspension 1 a jetted from a head box 2 into the shape of a layer, and removing moisture while making this paper stock layer 1 travel. The papermaking machine is provided with steam type heating means 6 and adjustment means 11. The steam type heating means 6 is provided in a moisture removing part as heating means for heating the paper stock layer 1 to accelerate the moisture removal, and supplies steam to the paper stock layer 1 and heats the paper stock layer 1 by condensation of the steam. The adjustment means 11 adjusts the supply of the steam performed by the steam type heating means 6, on the basis of a stock concentration of the paper stock layer 1 detected when passing through the steam type heating means 6, so that the paper stock layer 1 reaches a preset target temperature.
Description
- The present invention relates to a papermaking machine and papermaking method that make continuous paper by removing moisture while making it travel a layer of paper stock.
- Generally, in papermaking machines, by holding a suspension of pulp (suspension of paper stock) jetted from a head box into the shape of a layer by a wire, etc., and removing moisture while making this paper stock layer (also referred to as wet paper web) travel, a paper web is made.
- Various methods of dehydration for papermaking machines have been developed. For example, as shown in
FIG. 8 (a),patent document 1 discloses a papermaking machine equipped with asteam box 60 for supplying steam to the upper side ofwet paper web 1. Thesteam box 60 is arranged over a path of travel in the final part of a former (also referred to as a forming part or paper layer forming part). - In such a papermaking machine, steam from a
steam generator 10 is supplied to thesteam box 60 through a steam conduit. The steam touches thewet paper web 1 held on awire 30 and condenses, whereby heat is transferred to thewet paper 1. - It is conceivable that in the final part of the former, the
wet paper web 1 will be in a state before completion of dehydration, that is, a state in which minute interstices have been formed by dehydration, or a porous state. By suctioning the under side of thewet paper web 1 through thewire 30 by asuction box 70, steam enters such interstices or pores and permeates into thewet paper web 1. As a result, the latent heat of the steam is converted to the sensible heat of water, whereby thewet paper web 1 is raised in temperature and the dehydration rate rises. - The dehydration rate of the
wet paper web 1 traveling through the former is not uniform. In general, the widthwise central portion of thewet paper web 1 is lower in dehydration rate than the widthwise right and left end portions. Hence, as shown inFIG. 8 (b), there has been developed a technique in which, in order to cause the widthwise central portion of thewet paper web 1 whose dehydration rate is relatively low to touch more steam than the widthwise right and left portions, by widthwise dividing thesteam box 60 into a plurality ofsteam supply chambers 61, and suitably adjustingvalves 11 corresponding to eachsteam supply chamber 61, the widthwisecentral steam chambers 61 are supplied with more steam than the widthwise right andleft steam chambers 61. - Similarly,
patent document 2 discloses a technique in which by causing steam to touch wet paper, the wet paper is raised in temperature. - Patent document 1: Japanese patent laid-open publication No. Sho 55-137293
- Patent document 2: U.S. Pat. No. 5,149,401
- The inventors have made various investigations and experiments with respect to a mechanism of raising the dehydration rate of wet paper web by heating the wet paper web with steam and found the following facts. That is, there are cases where even if the supply of steam is increased in order to further raise the dehydration rate, conversely the dehydration rate will be reduced. A possible cause is that an increase in the supply of steam increases the quantity that steam condenses into water.
- However, in the conventional papermaking machine described above, such a change in the dehydration rate with respect to the supply of steam is not taken into account and an optimum supply of steam is not always set. Thus, the problem of performing dehydration with good efficiency remains unsolved.
- The present invention has been made in view of the problem described above. Accordingly, it is the primary object of the present invention to provide a papermaking machine and papermaking method that are capable of dehydrating a layer of paper stock with better efficiency.
- To achieve the aforementioned object, the papermaking machine of the present invention as set forth in
claim 1 is a papermaking machine for making paper web by holding a paper stock suspension jetted from a head box into the shape of a layer, and removing moisture while traveling the paper stock layer. The papermaking machine comprises: steam type heating means, provided in a moisture removing part as heating means for heating the paper stock layer (wet paper web) to accelerate the moisture removal, for supplying steam to the paper stock layer and heating the paper stock layer by condensation of the steam; and adjustment means for adjusting the supply of the steam performed by the steam type heating means, on the basis of a stock concentration of the paper stock layer detected when passing through the steam type heating means, so that the paper stock layer reaches a preset target temperature. - The steam used herein is not limited to saturated steam, but may be heated steam, wet air, etc. By detecting the above-mentioned stock concentration of the paper stock layer in real time, the supply of steam may be adjusted based on the information detected. In addition, by obtaining a stock concentration of the paper stock layer beforehand, the supply of steam may be adjusted based on the stock concentration obtained beforehand.
- The papermaking machine of the present invention as set forth in
claim 2 is characterized in that, in the construction as set forth inclaim 1, the moisture removing part is a former (also called a forming part or paper layer forming part) which forms a layer of paper by holding the paper stock suspension jetted from the head box into the shape of a layer, and removing moisture while traveling the paper stock layer, or a press part which further removes moisture by applying pressure to the paper stock layer formed into the paper layer by the former. - The papermaking machine of the present invention as set forth in claim 3 is characterized in that, in the construction as set forth in
claim 2, the forming part is constructed as twin wire formers equipped with wires on both sides of the paper stock layer. Note that the present invention is not always limited to twin wires, but may be applied to a long wire former or on-top former which holds only one side of a paper stock layer. - The papermaking machine of the present invention as set forth in claim 4 is characterized in that, in the construction as set forth in claim 3, the steam type heating means is provided with a steam box for guiding the supply of steam to the paper stock layer. In this case, the steam box is arranged so that the fringe of its tip opening abuts the wire or is very near the wire.
- The papermaking machine of the present invention as set forth in
claim 5 is characterized in that, in the construction as set forth in claim 4, the fringe of the tip opening of the steam box is provided with seal means for sealing the steam box. - The papermaking machine of the present invention as set forth in
claim 6 is characterized in that, in the construction as set forth inclaim 5, the seal means is a seal member which is attached to the fringe of the tip opening of the steam box and abuts the wire. - The papermaking machine of the present invention as set forth in
claim 7 is characterized in that, in the construction as set forth inclaim 5, the seal means is a gas jet device which is provided upstream in the traveling direction of the paper stock layer relative to the fringe of the tip opening of the steambox, and suppresses incursion of wake of the paper stock layer into the steam box by jetting gas. In this case, the gas jet device preferably jets gas toward the upstream side at a jet angle which is about 15 to 40° to wet paper web. - The papermaking machine of the present invention as set forth in
claim 8 is characterized in that, in the construction as set forth in any one of claims 4 to 7, it further includes a suction box for suctioning steam jetted from the steam box toward a side opposite to the steam box across the paper stock layer. - The papermaking machine of the present invention as set forth in
claim 9 is characterized in that, in the construction as set forth inclaim 8, a downstream end of the suction box in the traveling direction of the paper stock layer is arranged downstream relative to a downstream end of the steam box in the traveling direction of the paper stock layer. - The papermaking machine of the present invention as set forth in
claim 10 is characterized in that, in the construction as set forth inclaim - The papermaking machine of the present invention as set forth in
claim 11 is characterized in that, in the construction as set forth inclaim 10, the suction force of the downstream suction box in the traveling direction of the paper stock layer is set larger than that of the upstream suction box. - The papermaking machine of the present invention as set forth in
claim 12 is characterized in that, in the construction as set forth in any one ofclaims 8 to 11, the steam box is divided into a plurality of parts in the width direction of the paper stock layer and the suction box is divided into a plurality of parts so as to correspond to the divided parts of the steam box. In this case, a jet of steam and suction of steam are adjustable for each of the divided parts. - The papermaking machine of the present invention as set forth in
claim 13 is characterized in that, in the construction as set forth in any one ofclaims 1 to 12, the steam supplied by the steam type heating means heats the paper stock layer by acting on the paper stock layer as a collision jet. - The papermaking machine of the present invention as set forth in
claim 14 is characterized in that, in the construction as set forth in any one ofclaims 1 to 13, it further includes control means for automatically adjusting the adjustment means. - The papermaking machine of the present invention as set forth in claim 15 is characterized in that, in the construction as set forth in
claim 14, it further includes stock concentration detecting means, provided in the vicinity of the steam type heating means, for detecting a stock concentration of the paper stock layer when passing through the steam type heating means. In this case, the control means controls the supply of steam performed by the steam type heating means, on the basis of information detected by the stock concentration detecting means, so that the paper stock layer is raised to the target temperature. - In addition, the above-mentioned stock concentration detecting means is, for example, moisture percentage sensor, and the stock concentration can be estimated by moisture percentage of paper stock layer detected by the moisture percentage sensor.
- The papermaking machine of the present invention as set forth in claim 16 is characterized in that, in the construction as set forth in any one of
claims 1 to 15, it further includes air jet type heating means for blowing high-temperature air against the paper stock layer and heating the paper stock layer by a collision jet of the high-temperature air, provided as heating means for heating the paper stock layer, downstream in the traveling direction of the paper stock layer relative to a position at which the steam type heating means is installed. - The papermaking machine of the present invention as set forth in claim 17 is characterized in that, in the construction as set forth in any one of
claims 1 to 16, the heating means comprises first heating means for performing heating on one side of the paper stock layer, and second heating means for performing heating on the other side of the paper stock layer. - The papermaking method of the present invention as set forth in claim 18 is a papermaking method of making paper web by holding a paper stock suspension jetted from a head box into the shape of a layer, and removing moisture while traveling the paper stock layer. The papermaking method comprises a step of supplying steam to the paper stock layer at a heated position and heating the paper stock layer by condensation of the steam, in such a way that the paper stock layer reaches a preset target temperature, and a step of suctioning and removing moisture from the paper stock layer. As described above, the steam used in this method is not limited to saturated steam, but may be heated steam, wet air, etc.
- According to the papermaking machine of the present invention as set forth in
claims 1 to 3, in the moisture removing part, the adjustment means adjusts the supply of the steam performed by the steam type heating means, on the basis of a stock concentration of the paper stock layer detected when passing through the steam type heating means, so that the paper stock layer reaches a preset target temperature. Therefore, the paper stock layer can be raised in temperature and dehydrated with better efficiency. As a result of this, the dehydration rate can be raised. - According to the papermaking machine of the present invention as set forth in claim 4, the steam type heating means is provided with a steam box for guiding the supply of steam to the paper stock layer. The steam box is arranged so that the fringe of its tip opening abuts the wire or is very near the wire. Therefore, steam can be supplied to the paper stock layer with good efficiency.
- According to the papermaking machine of the present invention as set forth in
claim 5, the fringe of the tip opening of the steam box is provided with seal means for sealing the steam box. Therefore, steam can be supplied to the paper stock layer with better efficiency. - According to the papermaking machine of the present invention as set forth in
claim 6, the seal means is a seal member which is attached to the fringe of the tip opening of the steam box and abuts the wire. Therefore, sealing of the steam box can be enhanced, whereby steam can be supplied to the paper stock layer with good efficiency. - According to the papermaking machine of the present invention as set forth in
claim 7, the seal means is a gas jet device which is provided upstream in the traveling direction of the paper stock layer relative to the fringe of the tip opening of the steam box, and suppresses incursion of wake of the paper stock layer into the steam box by jetting gas. Therefore, incursion of wake into the steam box can be reliably suppressed, whereby steam can be supplied to the paper stock layer with good efficiency. - According to the papermaking machine of the present invention as set forth in
claim 8, the suction box suctions steam jetted from the steam box toward a side opposite to the steam box across the paper stock layer. Therefore, high-temperature water condensed on the surface of the paper stock layer is able to permeate through the paper stock layer. This makes it possible to reliably raise the temperature of the entire paper stock layer and dehydrate the entire paper stock layer. - According to the papermaking machine of the present invention as set forth in
claim 9, a downstream end of the suction box in the traveling direction of the paper stock layer is arranged downstream relative to a downstream end of the steam box in the traveling direction of the paper stock layer. Therefore, moisture in the paper stock layer raised in temperature can be further removed, resulting in a further rise in the dehydration rate. - According to the papermaking machine of the present invention as set forth in
claim 10, in addition to the above-mentioned suction box, the papermaking machine further includes another suction box arranged on the side opposite to the steam box across the paper stock layer and downstream in the traveling direction of the paper stock layer. Therefore, the dehydration rate can be further raised. - According to the papermaking machine of the present invention as set forth in
claim 11, the suction force of the downstream suction box is set larger than that of the upstream suction box. Therefore, water in the paper stock layer raised in temperature by the upstream steam box can be further removed, resulting in a further rise in the dehydration rate. - According to the papermaking machine of the present invention as set forth in
claim 12, the steam box is divided into a plurality of parts in the width direction of the paper stock layer and the suction box is divided into a plurality of parts so as to correspond to the divided parts of the steam box, and a jet of steam and a suction of steam are adjustable for each of the divided parts. Therefore, the dehydration rate can be adjusted for each of the divided parts. - According to the papermaking machine of the present invention as set forth in
claim 13, the steam supplied by the steam type heating means heats the paper stock layer by acting on the paper stock layer as a collision jet. Therefore, the paper stock layer can be raised in temperature and dehydrated with better efficiency. - According to the papermaking machine of the present invention as set forth in
claim 14, the papermaking machine further includes control means for automatically adjusting the adjustment means. Therefore, the supply of steam can be automatically adjusted. - According to the papermaking machine of the present invention as set forth in claim 15, the control means controls the supply of steam performed by the steam type heating means, on the basis of information detected by the stock concentration detecting means, so that the paper stock layer is raised to the target temperature. Therefore, the supply of steam can be adjusted so that an optimum dehydration rate is obtained.
- According to the papermaking machine of the present invention as set forth in claim 16, the papermaking machine further includes air jet type heating means for blowing high-temperature air against the paper stock layer and heating the paper stock layer by a collision jet of the high-temperature air. The air jet type heating means is provided as heating means for heating the paper stock layer, downstream in the traveling direction of the paper stock layer from a position at which the steam type heating means is installed. Therefore, the paper stock layer raised in temperature by the steam type heating means can be further raised in temperature and dehydrated, resulting in a further rise in the dehydration rate.
- According to the papermaking machine of the present invention as set forth in claim 17, the heating means comprises first heating means for performing heating on one side of the paper stock layer, and second heating means for performing heating on the other side of the paper stock layer. Therefore, it is possible to evenly dehydrate both sides of the paper stock layer.
- According to the papermaking method of the present invention as set forth in claim 18, in such a way that the paper stock layer reaches a preset target temperature, steam is supplied to the paper stock layer at a heated position and the paper stock layer is heated by condensation of the steam. Thereafter, moisture is suctioned and removed from the paper stock layer. Therefore, the paper stock layer can be raised in temperature and dehydrated with better efficiency. This can raise the dehydration rate.
-
FIG. 1 is a schematic diagram showing a papermaking machine according to a first embodiment of the present invention; - FIGS. 2(a) and 2(b) schematically show a steam box and a suction box according to the first embodiment of the present invention,
FIG. 2 (a) being a sectional view taken along the direction in which wet paper web travels andFIG. 2 (b) being a sectional view taken along line A-A ofFIG. 2 (a); -
FIG. 3 is a graph showing how the dehydration rate (effect of accelerating dehydration) in the first embodiment of the present invention varies with respect to the stock concentration of wet paper web; -
FIG. 4 is a schematic diagram showing a papermaking machine according to a second embodiment of the present invention; -
FIG. 5 is a schematic diagram showing a papermaking machine according to a third embodiment of the present invention; -
FIG. 6 is a schematic diagram showing a papermaking machine according to a fourth embodiment of the present invention; -
FIG. 7 is a schematic diagram showing a papermaking machine according to a fifth embodiment of the present invention; and - FIGS. 8(a) and 8(b) schematically show a steam box and a suction box according to a conventional papermaking machine,
FIG. 8 (a) being a sectional view taken along the direction in which wet paper web travels andFIG. 8 (b) being a sectional view taken along line A-A ofFIG. 8 (a). - 1 Wet paper web(paper stock layer)
- 1 a Pulp suspension (paper stock suspension)
- 2 Head box
- 3 a, 3 b Wire
- 4 Forming roll
- 5 Blade shoe
- 6, 6′, 60 Steam box (steam type heating means)
- 6 a Steam box main body
- 6 b Heat retaining body
- 6 c Seal member (seal means)
- 6 d Partition wall
- 6 e Steam supply chamber
- 6 f Steam introducing port
- 6 g Tip opening
- 7, 7A, 7′, 70 Suction box
- 7 d Partition wall
- 7 e Suction chamber
- 7 f Suction port
- 7 g Tip opening
- 8 Suction roll
- 9 Suction box
- 10 Steam generator
- 11 Valve (adjustment means)
- 12 Controller (control means)
- 13 Moisture percentage sensor (stock concentration detecting means)
- 14 Gas jet device (Seal means)
- Embodiments of the present invention will hereinafter be described with reference to the drawings.
- FIGS. 1 to 3 are used for explaining a papermaking machine constructed in accordance with a first embodiment of the present invention.
FIG. 1 is a schematic diagram showing the papermaking machine. FIGS. 2(a) and 2(b) are diagrams schematically showing a steam box and a suction box.FIG. 2 (a) is a sectional view taken along the direction in which wet paper web travels, andFIG. 2 (b) is a sectional view taken along line A-A ofFIG. 2 (a).FIG. 3 is a graph showing how the dehydration rate (effect of accelerating dehydration) varies with respect to the stock concentration of wet paper web. - The papermaking machine of the first embodiment adopts twin wire formers, as shown in
FIG. 1 . When a pulp suspension (paper stock suspension) 1 a is jetted and supplied from ahead box 2 to a slit betweentwin wires pulp suspension 1 a becomes a wet paper web (a paper stock layer) 1 by being held into the shape of layer between thetwin wires wet paper web 1 is dehydrated by a forming roll 4 which performs dehydration by tension of thewires blade shoe 5 which performs dehydration by curving a path of travel; and so forth. - Downstream of the
blade shoe 5, thewet paper web 1 is raised in temperature by asteam box 6 and is suctioned and dehydrated by asuction box 7 installed across thewet paper web 1 from thesteam box 6. Now, thesteam box 6 andsuction box 7 in the first embodiment will be described in further detail. - As shown in FIGS. 2(a) and 2(b), the steam box (steam type heating means) 6 as heating means is equipped with a steam box
main body 6 a, aheat retaining body 6 b, and a seal member (seal means) 6 c. - The steam box
main body 6 a has, for example, a machine length of about 100 to 1000 mm in the traveling direction of thewet paper web 1, and the internal space is divided into a plurality ofsteam supply chambers 6 e in the width direction of thewet paper web 1 bypartition walls 6 d. Each of thesteam supply chambers 6 e divided by thepartition walls 6 d has asteam introducing port 6 f for taking in steam from asteam generator 10, and a tip opening 6 g facing thewire 3 a. In the first embodiment, the tip opening 6 g of the steam boxmain body 6 a has aseal member 6 c attached thereto, which abuts thewire 3 a. - By supplying steam from the
steam generator 10 to each of thesteam supply chambers 6 e, thewires wet paper web 1 can be heated to about 40 to 100° C. Note that it is also possible to cause the supplied steam to act on thewet paper web 1 as a collision jet. This can heat thewet paper web 1 efficiently. - The
heat retaining body 6 b is, for example, a heat retaining structure with a heat insulating material or heat insulating layer, or a heating device such as an electric heater, a heating steam jacket, a high-temperature air jacket, etc., and is attached to the outside wall of the steam boxmain body 6 a so that it can retain the heat of the steam boxmain body 6 a. This can prevent steam condensation and dew condensation from occurring on the inside wall surface of the steam boxmain body 6 a (i.e., the inside wall surface of thesteam supply chamber 6 e). - The
seal member 6 c is attached to the fringe of the tip opening 6 g of the each ofsteam supply chambers 6 e so as to abut thewire 3 a, and functions to seal the steam boxmain body 6 a and each of thesteam supply chambers 6 e. This ensures sealing of the interior of the steam boxmain body 6 a and interior of each of thesteam supply chambers 6 e. As to theseal member 6 c, an elastic material such as rubber is suitable from the viewpoint of sealing performance, but since heat-resisting property is required, a heating-resisting material such as bakelite is also suitable. Of course, a material, such as heat-resisting rubber, which has both elasticity and heat-resisting property is more suitable. - In the case where there is no
seal member 6 c, wake intrudes through the gap between the upstream side of the tip opening 6 g and thewire 3 a and may disturb the touch of steam with thewet paper web 1, but the installation of theseal member 6 c enables steam to touch the whole of thewet paper web 1 located within each of thesteam supply chambers 6 e. Therefore, a reduction in the efficiency at which steam condenses and adheres to the wet paper web 1 (condensation and adhesion efficiency) can be prevented. - Supply pipes connected to each of the
steam supply chambers 6 e are provided with valves (adjustment means) 11, through which steam is supplied from thesteam generator 10 to thesteambox 6. By controlling the opening and closing operation of eachvalve 11 with acontroller 12, the supply of steam into thesteam supply chambers 6 e can be separately adjusted. Note that the steam used in the first embodiment may be any of saturated steam, heated steam, and wet air. - The
suction box 7 has, for example, the same machine length as thesteambox 6 or a machine length shorter than thesteam box 6, and the interior space is divided into a plurality ofsuction chambers 7 e at intervals of the same width as the steam boxmain body 6 a in the width direction of thewet paper web 1 bypartition walls 7 d. Each of thesuction chambers 7 e divided by thepartition walls 7 d has asuction port 7 f connected to a suction device (not shown), and an tip opening 7 g facing thewire 3 b. Thesuction box 7 is installed so that the tip opening 7 g abuts the surface of thewire 3 b. - Generally, the width of the
steam box 6 and the width of thewires steam box 6 is larger than that of thewires suction box 7 is approximately the same as the width of thesteam box 6, so thissuction box 7 fulfills the function of the aforementioned member. - By the
steam box 6 andsuction box 7, thewet paper web 1 is heated and dehydrated. Specifically, the steam supplied into thesteam box 6 is condensed into high-temperature water in the vicinity of the surface of thewire 3 a and surface of thewet paper web 1. Then, the high-temperature water gets into thewet paper web 1 by the suction operation of thesuction box 7, the entirewet paper web 1 is raised in temperature by the heat transfer of the high-temperature water, and by suctioning the moisture in thewet paper web 1 by thesuction box 7, thewet paper web 1 is dehydrated. - Within the
steam box 6 the temperature raising process is being performed and thewet paper web 1 entering thesteam box 6 is progressively raised in temperature within thesteam box 6, but a time lag occurs until the whole of thewet paper web 1 is raised in temperature. Hence, in the papermaking machine of the first embodiment, as shown inFIG. 1 , thewet paper web 1 in which the effect of dehydration has become higher by being raised in temperature within thesteam box 6 is further dehydrated by asuction roll 8 and asuction box 9 installed downstream of thesteam box 6. This makes it possible to perform dehydration with better efficiency, resulting in a rise in the dehydration rate. - As previously mentioned, the inventors have found that there are cases where, even if the supply of steam is increased to further raise the dehydration rate, conversely the dehydration rate will be reduced. A possible reason is that an increase in the supply of steam increases the quantity of heat supplied, but the quantity that steam condenses into water is increased and causes an increase in the moisture percentage. Therefore, in order to raise the dehydration rate, how to set the supply of steam becomes important.
- Hence, the inventors have investigated how the dehydration rate varies with respect to the paper stock concentration of the
wet paper web 1 under a certain suction condition. The results are shown inFIG. 3 . -
FIG. 3 shows dehydration raising characteristics due to the temperature raising effect in the case of a large supply of steam and the case of a low supply of steam, and a dehydration reducing characteristic due to dehydration resistance in the case where suction pressure is fixed. - For example, the characteristics of the dehydration accelerating effect by steam supply are shown by lines M1 and M2 in
FIG. 3 . That is, in both the case of a large supply of steam and the case of a low supply of steam, the higher the stock concentration, the less the moisture and the lower the mass of thewet paper web 1, therefore the heat capacity becomes low, so that the temperature of thewet paper web 1 is considerably raised, resulting in a rise in the dehydration rate (i.e., the dehydration rate is raised by the temperature raising effect of the wet paper web 1). From the comparison of lines M1 and M2 it follows that the case of a large supply of steam (M1) has a higher dehydration rate than the case of a low supply of steam (M2). - On the other hand, in the case where the suction pressure is fixed, the characteristic of the dehydration accelerating effect by suction is shown by line S in
FIG. 3 . That is, the higher the stock concentration the larger the dehydration resistance, so that the dehydration rate is reduced. - Therefore, in the case of a large supply of steam, a practical dehydration accelerating effect is obtained by adding the dehydration accelerating effect by steam supply shown by the line M1 and the dehydration accelerating effect by suction shown by the line S together. As shown by line L1 in
FIG. 3 , this dehydration accelerating effect has a mountainous characteristic that rises up to a certain stock concentration and then drops gradually. - Similarly, in the case of a low supply of steam, a practical dehydration accelerating effect is obtained by adding the dehydration accelerating effect by steam supply shown by the line M2 and the dehydration accelerating effect by suction shown by the line S. That is to say, the practical dehydration accelerating effect is represented by line L2.
- Generally, the dehydrating speed v equivalent to the dehydration raising rate is expressed according to Darcy's rule by the following equation (1):
- [Formula 1]
v=ΔP/(R mat+2R w)μ (1)
in which - v=dehydrating speed,
- ΔP=vertical differential pressure,
- Rmat=dehydration resistance coefficient of the wet Paper web,
- Rw=dehydration resistance coefficient of the wire,
- μ=water viscosity.
- In the aforementioned equation (1), assuming that the vertical differential pressure ΔP, the dehydration resistance coefficient Rmat of the wet paper web, and the dehydration resistance coefficient Rw of the wire are constant, and directing attention to the relation of the dehydrating speed v and water viscosity μ, the dehydrating speed v has an inversely proportional relation to the water viscosity μ. In addition, between the water viscosity μ and the temperature of the wet paper web, there is a relation in which the water viscosity μ becomes smaller as the temperature of the wet paper web becomes higher. That is, there is a relation in which the dehydrating speed v becomes faster as the temperature of the wet paper web becomes higher.
- Normally, according to Darcy' rule, the
wet paper web 1 is raised in temperature by heated steam and therefore the dehydrating speed becomes faster and the dehydration rate becomes higher, but at the same time, an increase in the stock concentration increases resistance to dehydration. As a result, the dehydration accelerating effect has a mountainous characteristic shown inFIG. 3 , and the most efficient stock concentration exists according to the state of steam supply. - Therefore, to raise the dehydration rate, it is preferable to set an optimum steam supply according to the stock concentration of the
wet paper web 1, taking such a characteristic into account. Because of this, the papermaking machine of the first embodiment, as shown inFIG. 1 , is provided with moisture percentage sensors (stock concentration detecting means) 13 for detecting the moisture percentage (which corresponds to the stock concentration (%)=100− moisture percentage (%)) of the wet paper web 1 (inFIG. 1 there is shown only one), which are disposed near the upstream end of thesteam box 6 and at the positions corresponding to the position of each of thesteam supply chambers 6 e in the width direction of the wet paper web 1 (i.e., at spots where thewet paper web 1 is heated). - The
controller 12 adjusts the opening and closing operation of eachvalve 11 and controls the state of steam supplied to eachsteam supply chamber 6 e in real time, based on information detected by eachmoisture percentage sensor 13, so that the temperature of thewet paper web 1 passing through eachsteam supply chamber 6 e becomes a target wet paper temperature (which is a target temperature set beforehand according to the stock concentration of the wet paper web 1). For example, thesteam supply chamber 6 e is disposed at a certain spot, and the reference stock concentration of thewet paper web 1 coming to this spot is assumed to be 12%. If the stock concentration of thewet paper web 1 detected by themoisture percentage sensor 13 is 10%, thecontroller 12 controls thevalve 11 so that the supply of steam is increased. If the stock concentration of thewet paper web 1 detected by themoisture percentage sensor 13 is 14%, thecontroller 12 controls thevalve 11 so that the supply of steam is reduced. - In addition, since the steam jetted state and steam suctioned state can be adjusted for each of the divided regions in the
steam box 6 andsuction box 7, the adjustment of dehydration in the width direction of thewet paper web 1 can be easily performed. - Besides, because steam is supplied to the
wet paper web 1 through thewire 3 a, there is no possibility that the fringe of the tip opening 6 g of thesteam box 6 will touch thewet paper web 1 and destroy it. In addition, property and color changes of pulp that occur when high-temperature steam directly touches thewet paper web 1 can be prevented. That is, like prior art, in the case where steam is blown directly against thewet paper web 1, it is necessary to provide a gap between thesteam box 6 and thewet paper web 1 to prevent damage to thewet paper web 1, and consequently, a large quantity of steam is discharged. However, in the papermaking machine of the first embodiment, both sides of thewet paper web 1 are supported bytwin wires steam box 6 touches thewire 3 a, whereby the aforementioned gap can be eliminated without damaging thewet paper web 1 and, compared with the prior art, the quantity of steam discharged can be suppressed. That is, since steam loss can be prevented, steam can be efficiently utilized. - Because sealing of the
steam box 6 is ensured by theseal member 6 c of thesteam box 6, the discharge of steam from inside thesteam box 6 to outside thesteam box 6 can be further suppressed. - In the conventional papermaking machine, the focus of attention is that steam permeating into the
wet paper web 1 raises the temperature of thewet paper web 1 and dehydrates thewet paper web 1. Because of this, it is necessary to install thesteam box 60 and suction box 70 (see FIGS. 8(a) and 8(b)) at positions where steam is in a permeable state, that is, a state before completion of dehydration of thewet paper web 1 of the former final part, and where thewet paper web 1 is caused to be in a porous state or a state in which interstices are formed. On the other hand, in the papermaking machine of the first embodiment, attention is further directed to the following points. That is, by the suction operation of thesuction box 7, the moisture in thewet paper web 1 is replaced with the high-temperature water condensed near the surface of thewet paper web 1, whereby thewet paper web 1 is raised in temperature and dehydrated. Therefore, steam does not always need to permeate into thewet paper web 1, as is done in prior art. - That is, in prior art, the steam box has to be installed at a position before completion of dehydration (i.e., near the former outlet), but according to the present invention, it is possible to install it more upstream. This makes it possible to accelerate the dehydration of the
wet paper web 1 in the former from the upstream side. Moreover, as described above, because the papermaking machine of the first embodiment performs optimum steam supply according to the stock concentration of thewet paper web 1, the heating and dehydration efficiency can be raised. Therefore, it becomes possible to perform the dehydration in the former with great efficiency, and consequently, the former can be made compact, whereby space to install the former can be saved. - The heat transfer efficiency of the papermaking machine of the first embodiment by steam condensation is about 25 times as high as that of the conventional papermaking machine by steam permeation and is extremely high compared with the prior art. Therefore, a rise in the temperature of the
wet paper web 1 by the conventional papermaking machine is so insufficient that even if thesuction box 9 is provided downstream of thesuction box 70, a high effect of dehydration cannot be obtained. On the other hand, in the papermaking machine of the first embodiment, a rise in the temperature of thewet paper web 1 is so sufficient that a high effect of dehydration is obtained by thesuction roll 8 andsuction box 14 arranged downstream of thesuction box 7. Thus, it is possible to accelerate dehydration of thewet paper web 1. - In the first embodiment, the internal spaces of the
steam box 6 andsuction box 7 are divided into several parts so that the jetted state of steam and the suctioned state of steam can be adjusted for each of the divided regions. However, in the case where a stock concentration difference in the width direction of thewet paper web 1 is practically negligible, it is not necessary to divide these spaces (i.e., thepartition walls moisture percentage sensor 13, and based on this representative stock concentration, the supply of steam required for thewet paper web 1 to rise to the target wet paper web temperature may be set. Alternatively, a singlemoisture percentage sensor 13 may be installed at a single spot in the width direction of the wet paper web 1 (e.g., at the laterally central portion of the wet paper web 1), and based on a stock concentration obtained by thismoisture percentage sensor 13, the supply of steam required for thewet paper web 1 to rise to the target wet paper web temperature may be set. - While the first embodiment is constructed such that the opening and closing operations of the
valves 11 are automatically adjusted based on information detected from themoisture percentage sensors 13 by thecontroller 12, the valve opening and closing operations may be manually performed by the operator, based on information detected from themoisture percentage sensors 13. - While the first embodiment is constructed such that the
steam box 6 andsuction box 7 are provided in the former that forms a layer of paper, they may be provided in a press part (which applies pressure to the paper stock layer formed by the former to further remove moisture) arranged downstream of the former. - Next, a papermaking machine according to a second embodiment of the present invention will be described.
- As shown in
FIG. 4 , the papermaking machine of the second embodiment, in addition to the construction of the first embodiment, is equipped with anothersuction box 7A, which is arranged in close proximity to the downstream side of thesuction box 7. - As described in the first embodiment, within the
steam box 6 the temperature raising process is being performed and thewet paper web 1 traveling through thesteam box 6 is gradually raised in temperature within thesteam box 6, but a time lag occurs until the whole of thewet paper web 1 is raised in temperature. Hence, in the papermaking machine of the second embodiment, thewet paper web 1 in which the effect of dehydration has become higher by being raised in temperature within thesteam box 6 is further dehydrated by thesuction box 7A. Since thesuction box 7A suctions thewet paper web 1 in which the effect of dehydration has become higher, further dehydration can be performed, even if its suction force is equal to that of thesuction box 7. However, it is preferable to set the suction force of thesuction box 7A larger than that of thesuction box 7. This makes it possible to perform dehydration more efficiently, whereby the dehydration rate can be raised. - Next, a papermaking machine according to a third embodiment of the present invention will be described.
- As shown in
FIG. 5 , the papermaking machine of the third embodiment is constructed such that in the construction of the first embodiment, the downstream end of thesuction box 7 is arranged downstream relative to the downstream end of thesteam box 6. - As described above, a time lag occurs until the whole of the
wet paper web 1 is raised in temperature within thesuction box 6. Therefore, by arranging thesuction box 7 so as to be shifted downstream, thewet paper web 1 can be dehydrated with better efficiency, resulting in a further rise in the dehydration rate. - In the third embodiment, the
suction box 7 according to the first embodiment is arranged so that it is shifted downstream by a predetermined distance. However, with the upstream end of thesuction box 7 of the first embodiment fixed at its original position, only the downstream end of thesuction box 7 may be positioned downstream relative to the downstream end of thesteam box 6. - Next, a papermaking machine according to a fourth embodiment of the present invention will be described.
- As shown in
FIG. 6 , the papermaking machine of the fourth embodiment is constructed such that in the construction of the first embodiment, it is further equipped with an air jet device (seal means) 14 that jets air toward the upstream side, in the vicinity of the upstream end of thesteam box 6. It is preferable that theair jet device 14 jet air toward the upstream side at an angle θ of about 15 to 40 degrees relative to thewet paper web 1. - This can suppress incursion of wake into the
steam box 6 more reliably. In the case where wake can be sufficiently suppressed by theair jet device 14, theupstream seal member 6 c of thesteam box 6 may be omitted. - Next, a papermaking machine according to a fifth embodiment of the present invention will be described.
- As shown in
FIG. 7 , the papermaking machine of the fifth embodiment is equipped with two sets of units comprising asteam box 6 and asuction box 7 of the first embodiment. Specifically, the fifth embodiment is provided with a first unit comprising a steam box (first heating means) 6 and asuction box 7, and a second unit comprising a steam box (second heating means) 6′ and asuction box 7′. Thesteam box 6 supplies steam to one side of thewet paper web 1, while thesteam box 6′ supplies steam to the other side of thewet paper web 1. This makes it possible to dehydrate both sides of thewet paper web 1 evenly, whereby it becomes possible to manufacture products in which both sides are so even that a difference between them is slight. - While the present invention has been described with reference to the preferred embodiments thereof, the invention is not to be limited to the details given herein, but may be modified within the scope of the invention hereinafter claimed.
- The installation position of the
steam box 6 can be determined beforehand in making a design, and the stock concentration (the reference stock concentration) of thewet paper web 1 at the installation position can also be predicted in the stage of the design. Therefore, in papermaking machines, steam supply may be performed so that the temperature of thewet paper web 1 becomes a target wet paper temperature which corresponds to the reference stock concentration. In the above-described embodiments, the actual stock concentration of thewet paper web 1 is detected by themoisture percentage sensor 13, and when there is a difference between the stock concentration of thewet paper web 1 passing through thesteam box 6 and the aforementioned reference stock concentration, the supply of steam to thesteam box 6 is adjusted by feedback control in order to correct for this difference. However, in the case where such a concentration difference is almost negligible, a constant supply of steam may be continuously performed in an open loop without providing themoisture percentage sensor 13. - By providing means for detecting the temperature of the
wet paper web 1 and performing feedback control based on the detected information, steam supply may be adjusted so that thewet paper web 1 reaches the target wet paper web temperature. Even in this case, thewet paper web 1 can be raised in temperature and dehydrated with good efficiency, resulting in arise in the dehydration rate. - Downstream of the
steam box 6, there may be provided air jet type heating means for blowing high-temperature air against thewet paper web 1 and heating thewet paper web 1 by a collision jet of high-temperature air. With this configuration, thewet paper web 1 raised in temperature within thesteam box 6 can be further raised in temperature, whereby it becomes possible to further raise the dehydration rate by thesuction roll 8,suction box 9, etc. - Since the
steam box 6 has a higher effect if it is employed when the moisture percentage of thewet paper 1 is high, it is preferable to install thesteam box 6 in the former in which the moisture percentage of thewet paper 1 is high, but it may be installed in the upstream portion (near the inlet) of the press part. Because the air jet type heating means has a higher effect if it is employed in a state lower than the moisture percentage of thewet paper web 1 in the former, it is preferable to install the air jet type heating means in the press part which is lower in the moisture percentage of thewet paper web 1 than the former, but it maybe installed in the downstream portion (near the outlet) of the former. - The above-described embodiments are constructed such that the
seal member 6 c abuts thewire 3 a in order to ensure sealing of thesteam box 6. However, if sealing of thesteam box 6 can be ensured, theseal member 6 c may be provided in close proximity to thewire 3 a. If sealing of thesteam box 6 is ensured by causing the tip opening 6 g of thesteam box 6 to abut thewire 3 a or arranging the tip opening 6 g in close proximity to thewire 3 a, there is no need to provide theseal member 6 c. - The present invention is not limited to twin wires, but may be applied to a long wire type former or on-top former which holds only one side of the paper stock layer.
- The present invention is applicable to a papermaking machine and papermaking method for making paper web by holding a paper stock suspension into the shape of a layer, and removing moisture while making this paper stock layer travel.
Claims (29)
1-18. (canceled)
19. A papermaking machine for making paper web by holding a paper stock suspension jetted from a head box into the shape of a layer, and removing moisture while traveling the paper stock layer, comprising:
steam type heating means, provided in a moisture removing part as heating means for heating said paper stock layer to accelerate said moisture removal, for supplying steam to said paper stock layer and heating said paper stock layer by condensation of said steam; and
adjustment means for adjusting the supply of said steam performed by said steam type heating means, on the basis of a stock concentration of said paper stock layer detected when passing through said steam type heating means, so that said paper stock layer reaches a preset target temperature;
wherein said moisture removing part is a former which forms a layer of paper by holding said paper stock suspension jetted from said head box into the shape of a layer, and removes moisture while traveling the paper stock layer, or a press part which further removes moisture by applying pressure to said paper stock layer formed into the paper layer by said former;
said former is constructed as twin wire formers equipped with wires on both sides of said paper stock layer;
said steam type heating means is provided with a steam box for guiding the supply of steam to said paper stock layer, and said steam box is arranged so that the fringe of its tip opening abuts said wire or is very near said wire;
further comprising a suction box for suctioning steam jetted from said steam box toward a side opposite to said steam box across said paper stock layer; and
another suction box besides to said suction box arranged on said side opposite to said steam box across said paper stock layer and downstream in the traveling direction of said paper stock layer;
wherein suction force of the downstream suction box is set larger than that of the upstream suction box.
20. The papermaking machine as set forth in claim 19 , wherein the fringe of the tip opening of said steam box is provided with seal means for sealing said steam box.
21. The papermaking machine as set forth in claim 20 , wherein said seal means is a seal member which is attached to the fringe of the tip opening of said steam box and abuts said wire.
22. The papermaking machine as set forth in claim 20 , wherein said seal means is a gas jet device which is provided upstream in the traveling direction of said paper stock layer relative to the fringe of the tip opening of said steam box, and suppresses incursion of wake of said paper stock layer into said steam box by jetting gas.
23. The papermaking machine as set forth in claim 19 , wherein a downstream end of said suction box in the traveling direction of said paper stock layer is arranged downstream relative to a downstream end of said steam box in the traveling direction of said paper stock layer.
24. The papermaking machine as set forth in claim 19 , wherein said steam box is divided into a plurality of parts in the width direction of said paper stock layer and said suction box is divided into a plurality of parts so as to correspond to the divided parts of said steam box, and wherein a jet of steam and suction of steam are adjustable for each of the divided parts of said steam box and said suction box.
25. The papermaking machine as set forth in claim 19 , wherein said steam supplied by said steam type heating means heats said paper stock layer by acting on said paper stock layer as a collision jet.
26. The papermaking machine as set forth in claim 19 , further comprising control means for automatically adjusting said adjustment means.
27. The papermaking machine as set forth in claim 26 , further comprising:
stock concentration detecting means, provided in the vicinity of said steam type heating means, for detecting a stock concentration of said paper stock layer when passing through said steam type heating means;
wherein said control means controls the supply of steam performed by said steam type heating means, on the basis of information detected by said stock concentration detecting means, so that said paper stock layer is raised to said target temperature.
28. The papermaking machine as set forth in claim 19 , further comprising:
air jet type heating means for blowing high-temperature air against said paper stock layer and heating said paper stock layer by a collision jet of said high-temperature air, provided as heating means for heating said paper stock layer, downstream in the traveling direction of said paper stock layer relative to a position at which said steam type heating means is installed.
29. The papermaking machine as set forth in claim 28 , wherein said heating means comprises first heating means for performing heating on one side of said paper stock layer, and second heating means for performing heating on the other side of said paper stock layer.
30. A papermaking method of making paper web by holding a paper stock suspension jetted from a head box into the shape of a layer, and removing moisture while making the paper stock layer travel, comprising the steps of:
supplying steam to said paper stock layer at a heating position and heating said paper stock layer by condensation of said steam, in such a way that said paper stock layer reaches a preset target temperature; and
suctioning and removing moisture from said paper stock layer.
31. A papermaking machine for making paper web by holding a paper stock suspension jetted from a head box into the shape of a layer, and removing moisture while traveling the paper stock layer, comprising:
steam type heating means, provided in a moisture removing part as heating means for heating said paper stock layer to accelerate said moisture removal, for supplying steam to said paper stock layer and heating said paper stock layer by condensation of said steam;
adjustment means for adjusting the supply of said steam performed by said steam type heating means, on the basis of a stock concentration of said paper stock layer detected when passing through said steam type heating means, so that said paper stock layer reaches a preset target temperature; and
air jet type heating means for blowing high-temperature air against said paper stock layer and heating said paper stock layer by a collision jet of said high-temperature air, provided as heating means for heating said paper stock layer, downstream in the traveling direction of said paper stock layer relative to a position at which said steam type heating means is installed.
32. The papermaking machine as set forth in claim 31 , wherein said moisture removing part is a former which forms a layer of paper by holding said paper stock suspension jetted from said head box into the shape of a layer, and removes moisture while traveling the paper stock layer, or a press part which further removes moisture by applying pressure to said paper stock layer formed into the paper layer by said former.
33. The papermaking machine as set forth in claim 32 , wherein said former is constructed as twin wire formers equipped with wires on both sides of said paper stock layer.
34. The papermaking machine as set forth in claim 33 , wherein said steam type heating means is provided with a steam box for guiding the supply of steam to said paper stock layer, and said steam box is arranged so that the fringe of its tip opening abuts said wire or is very near said wire.
35. The papermaking machine as set forth in claim 34 , wherein the fringe of the tip opening of said steam box is provided with seal means for sealing said steam box.
36. The papermaking machine as set forth in claim 35 , wherein said seal means is a seal member which is attached to the fringe of the tip opening of said steam box and abuts said wire.
37. The papermaking machine as set forth in claim 35 , wherein said seal means is a gas jet device which is provided upstream in the traveling direction of said paper stock layer relative to the fringe of the tip opening of said steam box, and suppresses incursion of wake of said paper stock layer into said steam box by jetting gas.
38. The papermaking machine as set forth in claim 34 , further comprising a suction box for suctioning steam jetted from said steam box toward a side opposite to said steam box across said paper stock layer.
39. The papermaking machine as set forth in claim 38 , wherein a downstream end of said suction box in the traveling direction of said paper stock layer is arranged downstream relative to a downstream end of said steam box in the traveling direction of said paper stock layer.
40. The papermaking machine as set forth in claim 38 , further comprising another suction box besides to said suction box, arranged on said side opposite to said steam box across said paper stock layer and downstream in the traveling direction of said paper stock layer.
41. The papermaking machine as set forth in claim 39 , wherein suction force of the downstream suction box is set larger than that of the upstream suction box.
42. The papermaking machine as set forth in claim 38 , wherein said steam box is divided into a plurality of parts in the width direction of said paper stock layer and said suction box is divided into a plurality of parts so as to correspond to the divided parts of said steam box, and wherein a jet of steam and suction of steam are adjustable for each of the divided parts of said steam box and said suction box.
43. The papermaking machine as set forth in claim 31 , wherein said steam supplied by said steam type heating means heats said paper stock layer by acting on said paper stock layer as a collision jet.
44. The papermaking machine as set forth in claim 31 , further comprising control means for automatically adjusting said adjustment means.
45. The papermaking machine as set forth in claim 44 , further comprising:
stock concentration detecting means, provided in the vicinity of said steam type heating means, for detecting a stock concentration of said paper stock layer when passing through said steam type heating means;
wherein said control means controls the supply of steam performed by said steam type heating means, on the basis of information detected by said stock concentration detecting means, so that said paper stock layer is raised to said target temperature.
46. The papermaking machine as set forth in claim 45 , wherein said heating means comprises first heating means for performing heating on one side of said paper stock layer, and second heating means for performing heating on the other side of said paper stock layer.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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PCT/JP2004/013544 WO2006030507A1 (en) | 2004-09-16 | 2004-09-16 | Papermaking machine and papermaking method |
Publications (1)
Publication Number | Publication Date |
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US20070209769A1 true US20070209769A1 (en) | 2007-09-13 |
Family
ID=36059774
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US11/659,472 Abandoned US20070209769A1 (en) | 2004-09-16 | 2004-09-16 | Papermaking Machine And Papermaking Method |
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US (1) | US20070209769A1 (en) |
CN (1) | CN101010459A (en) |
WO (1) | WO2006030507A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090188128A1 (en) * | 2008-01-29 | 2009-07-30 | Klaus Gissing | Utilization of waste heat in the dryer section of paper machines |
WO2011133332A3 (en) * | 2010-04-20 | 2012-02-23 | Honeywell International Inc. | Proactive steam and mist removal system |
US20130269734A1 (en) * | 2012-04-11 | 2013-10-17 | Georgia-Pacific Consumer Products Lp | Process for cleaning a transport belt for manufacturing a paper web |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55137293A (en) * | 1979-04-05 | 1980-10-25 | Tadao Imagawa | Sheet dehydrating method in paper making machine |
JPS56169896A (en) * | 1980-05-31 | 1981-12-26 | Haiku Japan Kk | Wet paper heating apparatus in papermaking machine |
JPS5887400A (en) * | 1981-11-12 | 1983-05-25 | 大建工業株式会社 | Production of mineral fiberboard |
JPS5876592A (en) * | 1982-09-24 | 1983-05-09 | 今川 忠雄 | Dehydration of sheet in paper making machine |
US5149401A (en) * | 1990-03-02 | 1992-09-22 | Thermo Electron Web Systems, Inc. | Simultaneously controlled steam shower and vacuum apparatus and method of using same |
JP2884696B2 (en) * | 1990-04-27 | 1999-04-19 | 横河電機株式会社 | Apparatus and method for changing and changing papermaking speed of paper machine |
JPH05321184A (en) * | 1992-05-12 | 1993-12-07 | Yokogawa Electric Corp | Operation controller of drier |
FR2786509A1 (en) * | 1998-11-30 | 2000-06-02 | Kimberly Clark Co | APPARATUS AND METHOD FOR SPINNING A PAPER TABLECLOTH |
JP3891955B2 (en) * | 2003-04-30 | 2007-03-14 | 三菱重工業株式会社 | Paper machine and paper making method |
-
2004
- 2004-09-16 US US11/659,472 patent/US20070209769A1/en not_active Abandoned
- 2004-09-16 WO PCT/JP2004/013544 patent/WO2006030507A1/en active Application Filing
- 2004-09-16 CN CNA2004800438773A patent/CN101010459A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090188128A1 (en) * | 2008-01-29 | 2009-07-30 | Klaus Gissing | Utilization of waste heat in the dryer section of paper machines |
US8429832B2 (en) * | 2008-01-29 | 2013-04-30 | Andritz Ag | Utilization of waste heat in the dryer section of paper machines |
WO2011133332A3 (en) * | 2010-04-20 | 2012-02-23 | Honeywell International Inc. | Proactive steam and mist removal system |
US8506662B2 (en) | 2010-04-20 | 2013-08-13 | Honeywell International Inc. | Proactive steam and mist removal system |
US20130269734A1 (en) * | 2012-04-11 | 2013-10-17 | Georgia-Pacific Consumer Products Lp | Process for cleaning a transport belt for manufacturing a paper web |
US10201840B2 (en) * | 2012-04-11 | 2019-02-12 | Gpcp Ip Holdings Llc | Process for cleaning a transport belt for manufacturing a paper web |
US10744545B2 (en) | 2012-04-11 | 2020-08-18 | Gpcp Ip Holdings Llc | Process for cleaning a transport belt for manufacturing a paper web |
Also Published As
Publication number | Publication date |
---|---|
WO2006030507A1 (en) | 2006-03-23 |
CN101010459A (en) | 2007-08-01 |
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