CN208406524U - A kind of waste material waste gas recovery utilizes system - Google Patents
A kind of waste material waste gas recovery utilizes system Download PDFInfo
- Publication number
- CN208406524U CN208406524U CN201820437632.8U CN201820437632U CN208406524U CN 208406524 U CN208406524 U CN 208406524U CN 201820437632 U CN201820437632 U CN 201820437632U CN 208406524 U CN208406524 U CN 208406524U
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- CN
- China
- Prior art keywords
- waste gas
- coke
- adsorption tanks
- gas
- adsorbsion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000002912 waste gas Substances 0.000 title claims abstract description 31
- 239000002699 waste material Substances 0.000 title claims abstract description 22
- 238000011084 recovery Methods 0.000 title claims abstract description 21
- 239000007789 gas Substances 0.000 claims abstract description 58
- 239000000571 coke Substances 0.000 claims abstract description 38
- 238000001179 sorption measurement Methods 0.000 claims abstract description 34
- 239000011347 resin Substances 0.000 claims abstract description 23
- 229920005989 resin Polymers 0.000 claims abstract description 23
- 229910002804 graphite Inorganic materials 0.000 claims abstract description 22
- 239000010439 graphite Substances 0.000 claims abstract description 22
- 238000000746 purification Methods 0.000 claims abstract description 20
- 238000010521 absorption reaction Methods 0.000 claims abstract description 17
- 238000004140 cleaning Methods 0.000 claims abstract description 9
- 239000004744 fabric Substances 0.000 claims description 20
- 239000000428 dust Substances 0.000 claims description 16
- 238000009825 accumulation Methods 0.000 claims description 8
- 238000007789 sealing Methods 0.000 claims description 6
- 238000004064 recycling Methods 0.000 claims description 5
- 229920000742 Cotton Polymers 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims 1
- 239000002994 raw material Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 6
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 238000005538 encapsulation Methods 0.000 abstract description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 12
- 230000000694 effects Effects 0.000 description 9
- 230000008901 benefit Effects 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000006978 adaptation Effects 0.000 description 2
- 239000002956 ash Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000003831 antifriction material Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008450 motivation Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of waste material waste gas recoveries to utilize system, including Matter Transfer recovery pipe system and waste gas purification by adsorbsion system, the Matter Transfer pipe-line system and waste gas purification by adsorbsion system include the adsorption tanks for containing coke, the lhv gas that the waste gas purification by adsorbsion system is generated from the resin exhaust gas of the resin treatment device generation for encapsulation process carbon-graphite blank and absorption from coke device by being contained in the coke absorption cleaning recycled in the adsorption tanks, and discharged after deduster filters.Pitch exhaust gas and resin exhaust gas are filtered absorption using coke by the utility model, simultaneously, using the coke after absorption as the raw material for preparing carbon-graphite product, realize waste gas and wastes zero-emission, the buying for preparing carbon-graphite raw material can be reduced simultaneously, industrial application cost is reduced, is increased economic efficiency, realizes the beneficial effects obtained more.
Description
Technical field
The utility model relates to the processing of environmental protecting device or system regions more particularly to carbon-graphite blank and processing
Environmental protection or field of dust removal equipment are specifically that a kind of waste material waste gas recovery utilizes system.
Background technique
Carbon-graphite product is increasingly widely applied and favorable comment in mechanical seal field, since carbon seal ring has
It is resistant to high temperatures, high pressure, anti abrasive dynamic sealing performance and be widely applied.
With the raising of equipment parameters, the hard sealing ring made of carbon-graphite antifriction material is largely used,
To guarantee that equipment reliably works in unlubricated dose and high-speed and high-temperature or corrosive media.In steam turbine gas turbine, piston
Formula or turbo-compressor, steam engine, pump, gas compressor, immersible pump, fresh water pump, two pole of core pump, boiler feed pump are dry
Machine, textile printing and dyeing machine, water pump, heat setting machine, canned motor pump separator, deduster, steam-flow meter, high-temperature hot oil pump, aircraft hair
Motivation, printing machinery vacuum pressed air pump gas compressor, in rotary engine and various chemical industry equipments, carbon graphite sealing
Ring is widely used.But to reach excellent sealing effect, usual graphite annulus needs pair before being processed into finished product
Graphite blank carries out the processing of resin impregnation sealant, is filled resin by micropore existing in graphite blank, and be formed by curing
One achievees the purpose that remove pore defect.
But due in graphite product with a variety of additive components in addition to carbon be used for improve graphite cementability and
Intensity, meanwhile, a large amount of exhaust gas can be generated in the process for carrying out graphite series of products, is being added to improve graphite product
Environment-friendly type during work realizes that exhaust gas waste residue recycles, turns waste into wealth, reduces environmental pollution, need one kind that can recycle benefit
System achievees the purpose that recycle carbon-graphite powder raw material for coke preparation and resin treatment to be combined processing.
Utility model content
The purpose of this utility model is to provide a kind of waste material waste gas recoveries to utilize system, for recycling to graphite
Product carries out the coke in the exhaust gas in resin seal treatment process, and recycling coke device as preparing carbon-graphite blank
Raw material pulvis.Pitch exhaust gas and resin exhaust gas are filtered absorption using coke, meanwhile, using the coke after absorption as
The raw material of carbon-graphite product are prepared, realize waste gas and wastes zero-emission, while can reduce and prepare adopting for carbon-graphite raw material
Purchase reduces industrial application cost, increases economic efficiency, and realizes the beneficial effects obtained more.
The utility model is achieved through the following technical solutions:
A kind of waste material waste gas recovery utilizes system, including Matter Transfer recovery pipe system and waste gas purification by adsorbsion system,
The Matter Transfer pipe-line system and waste gas purification by adsorbsion system include the adsorption tanks for containing coke, the exhaust gas absorption
Purification system is by being contained in the coke absorption cleaning recycled in the adsorption tanks from for encapsulation process carbon-graphite blank
Resin treatment device the resin exhaust gas and the lhv gas that is generated from coke device of absorption that generate, and filter heel row through deduster
It puts.
In order to preferably realize the utility model, it is preferable that the Matter Transfer recovery system especially uses following connections
Structure setting, specifically: the Matter Transfer recovery system includes the coke device being sequentially communicated, delivery pipe, collecting bin, promotion
Machine, bolt riser, adsorption tanks, pulverizer and for collecting through the recycling feed bin of the smashed powder of pulverizer.
In order to preferably realize the utility model, it is preferable that the waste gas purification by adsorbsion system especially uses following connections
Structure setting, specifically: the waste gas purification by adsorbsion system includes the second gas gathering mask and peace being mounted on above the coke device
The first gas gathering mask above the resin treatment device；First gas gathering mask and the second gas gathering mask pass through splitter and institute
State the bottom connection of adsorption tanks；The top of the adsorption tanks is connected to the deduster；First gas gathering mask and splitter it
Between be provided with the first exhaust fan, be provided with the second exhaust fan between second gas gathering mask and splitter, the adsorption tanks with remove
Third exhaust fan is provided between dirt device.
Working principle summary:
Firstly, the utility model is the equipment and connection relationship described in scheme, formation one can be realized useless
Gas waste residue recycles, meanwhile, the device systems of low exhaust gas emission drop.Connection between pipeline is not limited to shown in attached drawing
Structure can be arranged according to actual place and workshop and carry out adaptation to local conditions, if what technical spirit was recorded according to the application
Scheme implement, this point be for those of ordinary skill in the art it is very comprehensible, just seldom do herein superfluous
It states.
Secondly, principle is as follows when actually using this system: the first gas gathering mask on the resin treatment device will lead to
Resin exhaust gas is drawn into adsorption tanks by the suction for crossing the first exhaust fan carries out adsorption cleaning；Similarly, it is generated in the coke device
Exhaust gas exhaust gas is drawn onto adsorption tanks by the second gas gathering mask and by the suction of the second exhaust fan carry out absorption exchange purification.
Due to that there can be part dust in coke, in order to avoid dust pollutes air as air-flow is discharged in atmosphere, removed by cloth bag
Dirt device is filtered the effect that can reach purification air.Meanwhile constantly recycle fresh coke is promoted of the elevator
Into adsorption tanks, the coke after swapping in adsorption tanks also constantly crush by pulverizer carries out benefit again in powdered
With so circulation can reach the purpose to turn waste into wealth.
In order to preferably realize the utility model, it is preferable that the deduster is bag filter, the bag filter
Including shell, the multiple filter net cloths vertical with wind direction are installed in the shell, the filter net cloth uses the harmless cotton of multilayer
Cloth.
In order to preferably realize the utility model, it is preferable that between the filter net cloth and shell or and adjacent head
There is dust accumulation chamber between screen cloth；Vibrator is fixedly installed on the shell.
Since the volume of bag filter is larger, it has not been convenient to filter net cloth is frequently replaced, therefore, in the vibration of vibrator
Under effect, most of dust will be fallen under gravity in the dust accumulation chamber, when deposited a large amount of ashes in dust accumulation chamber
Unified cleaning is carried out when dirt again, effective filter cycle of filter net cloth can either be extended in this way, meanwhile, it also can be avoided ash
Dirt, which is evenly arranged on filter net cloth, blocks hole, influences filter effect.
In order to preferably realize the utility model, it is preferable that the position inside the adsorption tanks close to lower section be provided with into
Gas manifold, the inlet manifold opening down are simultaneously connected to the splitter；The structure of the inlet manifold includes a pipe
Shape annulus be connected to multiple air inlet straight tubes below the tubular ring vertically.It is by the downward opening purpose of inlet manifold
It avoids coke from blocking inlet manifold in carrying out dropping process, influences the effect of air inlet.
The utility model compared with prior art, have the following advantages that and the utility model has the advantages that
Pitch exhaust gas and resin exhaust gas are filtered absorption using coke by the utility model, meanwhile, after absorption
Coke realizes waste gas and wastes zero-emission as the raw material for preparing carbon-graphite product, while can reduce and prepare carbon-graphite original
The buying of material reduces industrial application cost, increases economic efficiency, and realizes the beneficial effects obtained more.
Detailed description of the invention
Fig. 1 is the structure principle chart of the utility model；
Wherein: 1- bag filter；2- filter net cloth；3- vibrator；4- exhaust pipe；5- dust accumulation chamber；6- adsorption tanks；7- into
Gas manifold；8- splitter；The first gas gathering mask of 9-；10- resin treatment device；11- recycles feed bin；12- coke device；13- pulverizer；
The second gas gathering mask of 14-；15- elevator；16- delivery pipe；17- collecting bin；18- screw lifting pipe.
Specific embodiment
The utility model is described in further detail below with reference to embodiment, but the embodiments of the present invention is not
It is limited to this.
Embodiment 1:
In conjunction with shown in attached drawing 1, a kind of waste material waste gas recovery utilizes system, including Matter Transfer recovery pipe system and exhaust gas
Adsorption cleaning system, the Matter Transfer pipe-line system and waste gas purification by adsorbsion system include the adsorption tanks for containing coke
6, the waste gas purification by adsorbsion system is by being contained in the coke absorption cleaning recycled in the adsorption tanks 6 from for sealing
The pitch gas that the resin exhaust gas and absorption that the resin treatment device 10 of processing carbon-graphite blank generates are generated from coke device 12
Body, and discharged after deduster filters.
In order to preferably realize the utility model, it is preferable that the Matter Transfer recovery system especially uses following connections
Structure setting, specifically: the Matter Transfer recovery system includes the coke device 12 being sequentially communicated, delivery pipe 16, collecting bin 17,
Elevator 15, bolt riser 18, adsorption tanks 6, pulverizer 13 and for collect pass through the smashed powder of pulverizer 13 return
Receiving warehouse 11.
In order to preferably realize the utility model, it is preferable that the waste gas purification by adsorbsion system especially uses following connections
Structure setting, specifically: the waste gas purification by adsorbsion system includes the second gas gathering mask 14 for being mounted on 12 top of coke device
With the first gas gathering mask 9 for being mounted on 10 top of resin treatment device；First gas gathering mask 9 passes through with the second gas gathering mask 14
Splitter 8 is connected to the bottom of the adsorption tanks 6；The top of the adsorption tanks 6 is connected to the deduster；First gas collection
It is provided with the first exhaust fan between cover 9 and splitter 8, is provided with the second exhausting between second gas gathering mask 14 and splitter 8
Machine is provided with third exhaust fan between the adsorption tanks 6 and deduster.All exhaust fans are to show in figure.
Working principle summary:
Firstly, the utility model is the equipment and connection relationship described in scheme, formation one can be realized useless
Gas waste residue recycles, meanwhile, the device systems of low exhaust gas emission drop.Connection between pipeline is not limited to shown in attached drawing
Structure can be arranged according to actual place and workshop and carry out adaptation to local conditions, if what technical spirit was recorded according to the application
Scheme implement, this point be for those of ordinary skill in the art it is very comprehensible, just seldom do herein superfluous
It states.
Secondly, principle is as follows when actually using this system: the first gas gathering mask 9 on the resin treatment device 10
Adsorption cleaning is carried out by resin exhaust gas is drawn into adsorption tanks 6 by the suction of the first exhaust fan；Similarly, the coke device 12
The exhaust gas of middle generation, which passes through the second gas gathering mask 14 and exhaust gas is drawn onto adsorption tanks 6 by the suction of the second exhaust fan, to be adsorbed
Exchange purification.Due to that there can be part dust in coke, in order to avoid dust pollutes air as air-flow is discharged in atmosphere, lead to
Cloth bag deduster 1 is filtered the effect that can reach purification air.Meanwhile the elevator 15 constantly recycle will be fresh
Coke promoted into adsorption tanks 6, pulverizer 13 also constantly by the coke after being swapped in adsorption tanks 6 carry out crush is in
Powdered to be recycled, so circulation can reach the purpose to turn waste into wealth.
Embodiment 2:
In order to preferably realize the utility model, the present embodiment on the basis of embodiment 1, further combined with 1 institute of attached drawing
Show and following structures are further optimized, the deduster is bag filter, and the bag filter includes shell, institute
It states and the multiple filter net cloths 2 vertical with wind direction is installed in shell, the filter net cloth 2 uses the harmless cotton of multilayer.
In the present embodiment, there is dust accumulation chamber 5 between the filter net cloth 2 and shell or between adjacent head screen cloth 2；
Vibrator 3 is fixedly installed on the shell.
Since the volume of bag filter 1 is larger, it has not been convenient to frequent replacement filter net cloth 2, therefore, in vibrator 3
Under effect of vibration, most of dust will be fallen under gravity in the dust accumulation chamber 5, deposited when in dust accumulation chamber 5
Unified cleaning is carried out when a large amount of dusts again, effective filter cycle of filter net cloth 2 can either be extended in this way, meanwhile, also can
It enough avoids dust from being evenly arranged on filter net cloth 2 to block hole, influence filter effect.
In the present embodiment, 6 inside of adsorption tanks is provided with inlet manifold 7, the inlet manifold 7 close to the position of lower section
It is opening down and be connected to the splitter 8；The structure of the inlet manifold 7 includes tubular ring and be connected to vertically
Multiple air inlet straight tubes below the tubular ring.It is to avoid coke in the case where carrying out by the downward opening purpose of inlet manifold 7
Inlet manifold 7 is blocked during falling, and influences the effect of air inlet.
The above is only the preferred embodiment of the utility model, not does limit in any form to the utility model
System, any simple modification made by the above technical examples according to the technical essence of the present invention, equivalent variations, each falls within
Within the protection scope of the utility model.
Claims (6)
1. a kind of waste material waste gas recovery utilizes system, including Matter Transfer recovery pipe system and waste gas purification by adsorbsion system,
Be characterized in that: the Matter Transfer pipe-line system and waste gas purification by adsorbsion system include for containing the adsorption tanks of coke (6),
The waste gas purification by adsorbsion system is by being contained in the coke absorption cleaning recycled in the adsorption tanks (6) from for sealing
The pitch that the resin exhaust gas and absorption for handling resin treatment device (10) generation of carbon-graphite blank are generated from coke device (12)
Gas, and discharged after deduster filters.
2. a kind of waste material waste gas recovery according to claim 1 utilizes system, it is characterised in that: the Matter Transfer recycling
System includes the coke device (12) being sequentially communicated, delivery pipe (16), collecting bin (17), elevator (15), bolt riser (18),
Adsorption tanks (6), pulverizer (13) and for collecting through the recycling feed bin (11) of pulverizer (13) smashed powder.
3. a kind of waste material waste gas recovery according to claim 2 utilizes system, it is characterised in that: the waste gas purification by adsorbsion
System is including being mounted on the second gas gathering mask (14) above the coke device (12) and being mounted on the resin treatment device (10)
The first gas gathering mask (9) of top；First gas gathering mask (9) and the second gas gathering mask (14) pass through splitter (8) and the absorption
The bottom of tank (6) is connected to；The top of the adsorption tanks (6) is connected to the deduster；First gas gathering mask (9) and splitter
(8) it is provided with the first exhaust fan between, is provided with the second exhaust fan, institute between second gas gathering mask (14) and splitter (8)
It states and is provided with third exhaust fan between adsorption tanks (6) and deduster.
4. a kind of waste material waste gas recovery according to any one of claim 1-3 utilizes system, it is characterised in that: described to remove
Dirt device is bag filter, and the bag filter includes shell, and the multiple filterings vertical with wind direction are equipped in the shell
Screen cloth (2), the filter net cloth (2) use the harmless cotton of multilayer.
5. a kind of waste material waste gas recovery according to claim 4 utilizes system, it is characterised in that: the filter net cloth (2)
There are dust accumulation chamber (5) between shell or between adjacent head screen cloth (2)；Vibrator is fixedly installed on the shell
(3).
6. a kind of waste material waste gas recovery according to claim 3 utilizes system, it is characterised in that: in the adsorption tanks (6)
Portion is provided with inlet manifold (7) close to the position of lower section, the inlet manifold (7) opening down and with the splitter (8)
Connection；The structure of the inlet manifold (7) include a tubular ring be connected to vertically it is multiple below the tubular ring
Air inlet straight tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820437632.8U CN208406524U (en) | 2018-03-29 | 2018-03-29 | A kind of waste material waste gas recovery utilizes system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820437632.8U CN208406524U (en) | 2018-03-29 | 2018-03-29 | A kind of waste material waste gas recovery utilizes system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208406524U true CN208406524U (en) | 2019-01-22 |
Family
ID=65119034
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820437632.8U Expired - Fee Related CN208406524U (en) | 2018-03-29 | 2018-03-29 | A kind of waste material waste gas recovery utilizes system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208406524U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109908694A (en) * | 2019-04-19 | 2019-06-21 | 江苏徐工工程机械研究院有限公司 | Asphalt fume treatment system |
| CN111921682A (en) * | 2020-09-02 | 2020-11-13 | 浙江新豪吉电器有限公司 | Integrated wallboard waste gas sweeps collection processing apparatus |
| CN113713568A (en) * | 2021-08-17 | 2021-11-30 | 安徽紫朔环境工程技术有限公司 | Sintering flue gas desulfurization and denitrification method and device |
-
2018
- 2018-03-29 CN CN201820437632.8U patent/CN208406524U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109908694A (en) * | 2019-04-19 | 2019-06-21 | 江苏徐工工程机械研究院有限公司 | Asphalt fume treatment system |
| CN109908694B (en) * | 2019-04-19 | 2024-10-15 | 江苏徐工工程机械研究院有限公司 | Pitch cigarette processing system |
| CN111921682A (en) * | 2020-09-02 | 2020-11-13 | 浙江新豪吉电器有限公司 | Integrated wallboard waste gas sweeps collection processing apparatus |
| CN113713568A (en) * | 2021-08-17 | 2021-11-30 | 安徽紫朔环境工程技术有限公司 | Sintering flue gas desulfurization and denitrification method and device |
| CN113713568B (en) * | 2021-08-17 | 2023-07-07 | 安徽紫朔环境工程技术有限公司 | Sintering flue gas desulfurization and denitrification method and device thereof |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190122 |
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| CF01 | Termination of patent right due to non-payment of annual fee |