CN109224754A - Volatile organic matter condensate recycling device and its recovery method based on macroreticular resin - Google Patents
Volatile organic matter condensate recycling device and its recovery method based on macroreticular resin Download PDFInfo
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- CN109224754A CN109224754A CN201811203081.XA CN201811203081A CN109224754A CN 109224754 A CN109224754 A CN 109224754A CN 201811203081 A CN201811203081 A CN 201811203081A CN 109224754 A CN109224754 A CN 109224754A
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- 239000005416 organic matter Substances 0.000 title claims abstract description 62
- 239000011347 resin Substances 0.000 title claims abstract description 53
- 229920005989 resin Polymers 0.000 title claims abstract description 53
- 238000004064 recycling Methods 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 23
- 238000011084 recovery Methods 0.000 title abstract description 8
- 238000001179 sorption measurement Methods 0.000 claims abstract description 150
- 239000007788 liquid Substances 0.000 claims abstract description 113
- 238000000926 separation method Methods 0.000 claims abstract description 69
- 238000010521 absorption reaction Methods 0.000 claims abstract description 61
- 239000007921 spray Substances 0.000 claims abstract description 36
- 239000012530 fluid Substances 0.000 claims abstract description 13
- 239000011435 rock Substances 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 239000000203 mixture Substances 0.000 claims description 21
- 238000005507 spraying Methods 0.000 claims description 11
- -1 polytetrafluoroethylene Polymers 0.000 claims description 10
- 238000009833 condensation Methods 0.000 claims description 9
- 230000005494 condensation Effects 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 6
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 6
- 239000003381 stabilizer Substances 0.000 claims description 6
- 230000005611 electricity Effects 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- 229910001220 stainless steel Inorganic materials 0.000 claims description 5
- 239000010935 stainless steel Substances 0.000 claims description 5
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 239000010963 304 stainless steel Substances 0.000 claims description 3
- 239000004793 Polystyrene Substances 0.000 claims description 3
- 229910000589 SAE 304 stainless steel Inorganic materials 0.000 claims description 3
- 239000011152 fibreglass Substances 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 3
- 239000003365 glass fiber Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 150000007522 mineralic acids Chemical class 0.000 claims description 3
- 239000004745 nonwoven fabric Substances 0.000 claims description 3
- 229920002223 polystyrene Polymers 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 2
- 238000012423 maintenance Methods 0.000 claims description 2
- 229920000573 polyethylene Polymers 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims 1
- 239000012855 volatile organic compound Substances 0.000 abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 3
- 239000003463 adsorbent Substances 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 229910021536 Zeolite Inorganic materials 0.000 abstract description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract description 2
- 239000002808 molecular sieve Substances 0.000 abstract description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 abstract description 2
- 239000010457 zeolite Substances 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 11
- 239000000126 substance Substances 0.000 description 7
- 239000002250 absorbent Substances 0.000 description 4
- 230000002745 absorbent Effects 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 4
- 238000006731 degradation reaction Methods 0.000 description 4
- 238000003795 desorption Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000003694 hair properties Effects 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 210000003850 cellular structure Anatomy 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 238000004737 colorimetric analysis Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
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- 238000001816 cooling Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
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- 239000000835 fiber Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
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- 230000035943 smell Effects 0.000 description 1
- 238000002336 sorption--desorption measurement Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1493—Selection of liquid materials for use as absorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2252/00—Absorbents, i.e. solvents and liquid materials for gas absorption
- B01D2252/10—Inorganic absorbents
- B01D2252/103—Water
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/106—Silica or silicates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/20—Organic adsorbents
- B01D2253/202—Polymeric adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
- B01D2257/406—Ammonia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40088—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
- B01D2259/4009—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating using hot gas
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses volatile organic matter condensate recycling devices and its recovery method based on macroreticular resin.As VOCs adsorbent, it is smaller that there are adsorption capacities for active carbon and zeolite molecular sieve, easy adsorption saturation, regenerates difficult problem.The present invention is based on the volatile organic matter condensate recycling devices of macroreticular resin, including gas adsorption modules, liquid separation loop module and vapor to provide device.Gas adsorption modules include capturing tower, dry filter and parallel macroporous resin adsorption tank.Parallel macroporous resin adsorption tank includes tank body, spray head and Multi-layer absorption component.Multi-layer absorption component includes the first grid being sequentially stacked from the bottom to top, the first separation strainer, the first macroreticular resin layer, the second grid, the second macropore resin layer, the second separation strainer, bright rock layers.Liquid separation loop module includes condenser, Gas and liquid flow diverter, Liquid liquid Separation device and fluid reservoir.Adsorption condensing of the present invention is high-efficient, adaptable, being capable of daily 24 continuous throughout the twenty-four hour24.
Description
Technical field
The invention belongs to chemical industry exhaust-gas treatment recovery technology fields, and in particular to a kind of volatilization based on macroreticular resin
Property organic matter condensate recycling device and its recovery method.
Background technique
Chemical industry VOCs (volatile organic compounds volatile organic matter) has the characteristics that following two:
First is that the exhaust gas generated in production technology discharges, pollutant and chemical production technology process and process operating condition item in discharge gas
Part is related, and type is more and nature difference is larger, and this discharge is organized, and discharge amount can be evaluated whether.Second is that passing through other links
Volatilization generates, and the VOCS of generation due to that can pass through various multiple with very strong diffusivity and reactivity under certain condition
Miscellaneous chemical reaction converts, and the discharge amount for the VOCs that such form generates can not accurately estimate that the analysis of generating source is also deposited
In difficulty.Instantly two classes can be divided into the administering method of VOCS, one kind is recovery technology, and another kind of is degradation technique.Recycle skill
The core concept of art is that the VOCs generated in chemical company is absorbed, filtered and separated first, next purify etc.
Reason is finally unfolded resource recycling and is utilized, and traditional recovery technology includes: absorption techniques, adsorption technology and membrane separation technique etc..
Degradation technique is then to convert other nontoxic substances by different chemical reactions for VOCs and be discharged, reach the mesh of emission reduction
's.Traditional degradation technique refers mainly to combustion technology, and catalytic combustion technology and new technology developed in recent years include leakage
The technologies such as detection and (LDAR) technology of reparation, plasma technique, biotechnology and photocatalysis.
High, the small feature of air quantity for chemical industry VCOs concentration, adsorption condensing recycling can not only effectively reduce VOCs row
Concentration is put, while being also able to achieve raw material and recycling.Active carbon and zeolite molecular sieve as the VOCs adsorbent generally used,
There are aperture smaller (< 2nm), specific surface area are relatively small, temperature tolerance is low (active carbon is no more than 130 DEG C or more), strong moisture absorption
Property the features such as, cause its adsorption capacity in industrial application smaller, easy adsorption saturation, regeneration is difficult, and (its desorption temperature is generally wanted
At 250 DEG C or more) and there is limitation etc. to macromolecules adsorption.Therefore, absorption resin is as high molecular polymer adsorbent, by
In having the characteristics that physicochemical properties are stable, chemical structure and pore structure are adjustable, are easy desorption, it has been widely used in removal
The absorption research of organic pollutant in aqueous solution.
Summary of the invention
The volatile organic matter condensate recycling device and its return that the purpose of the present invention is to provide a kind of based on macroreticular resin
Receiving method.
The present invention is based on the volatile organic matter condensate recycling devices of macroreticular resin, including gas adsorption modules, liquid separation to follow
Ring moulds block and vapor provide device.The gas adsorption modules include capturing tower, dry filter and parallel macropore tree
Rouge adsorption tanks.The parallel macroporous resin adsorption tank includes the first adsorption tanks and the second adsorption tanks.It is described to capture going out for tower
The connection of the air inlet of air port and dry filter.The air outlet of the dry filter is connect with the air inlet of the first air-introduced machine.
The air outlet of first air-introduced machine is connected to the air inlet of the first electromagnetism on-off valve.The gas outlet of first electromagnetism on-off valve and the second electricity
The connection of the air inlet of magnetic on-off valve and third electromagnetism on-off valve.Second electromagnetism on-off valve, third electromagnetism on-off valve gas outlet with
First adsorption tanks, the second adsorption tanks air inlet be separately connected.
The liquid separation loop module includes condenser, Gas and liquid flow diverter, Liquid liquid Separation device and fluid reservoir.Condenser it is defeated
Entrance is connect with the liquid outlet of the first adsorption tanks by the 6th electromagnetism on-off valve, passes through the with the liquid outlets of the second adsorption tanks
The connection of seven electromagnetism on-off valves.The delivery outlet of condenser and the input port of Gas and liquid flow diverter connect.The liquid of Gas and liquid flow diverter exports
Mouth is connect with the inlet of Liquid liquid Separation device, and gas delivery port is connect with the air inlet of the 8th electromagnetism on-off valve.8th electromagnetism is logical
The gas outlet of disconnected valve is connect with the air inlet of the 9th electromagnetism on-off valve.The gas outlet of 9th electromagnetism on-off valve and the second electromagnetism on-off
The connection of the air inlet of valve and third electromagnetism on-off valve.Second liquid outlet of Liquid liquid Separation device is connect with fluid reservoir.Liquid liquid Separation device
The first liquid outlet connect with fluid reservoir.The air inlet of gas vent and the 9th electromagnetism on-off valve on Liquid liquid Separation device passes through the
The connection of ten electromagnetism on-off valves.
The steam outlet that the vapor provides device is connect with the first adsorption tanks by the 12nd electromagnetism on-off valve,
It is connect with the second adsorption tanks by the 13rd electromagnetism on-off valve.
First adsorption tanks and the second adsorption tanks are identical equipment, including tank body, spray head and Multi-layer absorption group
Part.Spray head is provided at the top of the tank inner chamber.The middle part of tank inner chamber is arranged in the Multi-layer absorption component, and
Tank inner chamber is divided into filter ante-chamber and filter back cavity.Multi-layer absorption component include the first grid being sequentially stacked from the bottom to top,
First separation strainer, the first macroreticular resin layer, the second grid, the second macropore resin layer, the second separation strainer, bright rock layers.Tank body
Air inlet be connected to the intracorporal filter ante-chamber of tank, gas vent is connected to the intracorporal filter back cavity of tank.The liquid outlet of tank body is arranged
It is connected in the bottom of tank body, and with filter back cavity.
Further, the capture tower includes reservoir bed from bottom to up, gas enters layer, level-one removes wet layer, level-one is sprayed
Drenching layer, second level remove wet layer, second level spraying layer, demisting layer；Gas enters layer equipped with gas feed；Level-one dehumidifies except wet layer, second level
The filler of layer is one of stainless steel, polypropylene, polytetrafluoroethylene (PTFE) or a variety of；The top of level-one spraying layer, second level spraying layer
Spray system is added with the aqueous solution of inorganic acid.Air outlet is provided at the top of demisting layer.
Further, the dry filter includes low efficient filter, medium effeciency filter and high efficiency particulate air filter.Described
Low efficient filter, medium effeciency filter, high efficiency particulate air filter are arranged successively to the direction of air outlet along the air inlet of dry filter and set
It sets.Low efficient filter uses 304 stainless steel cloths.Medium effeciency filter is using non-woven fabrics or glass fibre as filter medium, mistake
Filtering partial size is 1~5 μm.High efficiency filter using porous ultra-fine fibre glass paper be used as filter medium, filtering partial size be 0.1~
0.5μm.The condenser uses the stainless steel with a thickness of 0.5~1.0mm as chief series pipe.The shell of condenser is by by swollen
Two half-shells composition of swollen section connection.Condenser uses shell-and-tube exchanger, and the baffle plate in condenser twist, and is opened
Equipped with multiple through-holes.
Further, first adsorption tanks and the second adsorption tanks further include stabilizer blade.The bottom of two stabilizer blades and tank body
Portion is fixed.Maintenance personal's import is offered at the top of the tank body.The both ends of the tank body are respectively provided with there are two sensor pocket
Pipeline.The inner end of four sensor pocket pipelines is connected to tank inner chamber, and outer end is closed by end cap.Four sensors hold
It receives and is provided with temperature sensor in pipeline.
Further, the liquid separation loop module further includes drip tray and measuring tank.The drip tray and liquid liquid point
The second liquid outlet connection from device.Measuring tank is arranged between Liquid liquid Separation device and fluid reservoir.Gas vent on measuring tank with
The air inlet of 9th electromagnetism on-off valve is connected by the 11st electromagnetism on-off valve.
Further, the metal bar of more perforation Multi-layer absorption components is provided on the Multi-layer absorption component.
All metal bars are grounded.The first macroreticular resin layer and the second macropore resin layer is all made of polydivinylbenezene, poly- second
Alkene, polystyrene, any one or two kinds in poly- phenolic aldehyde.The first separation strainer and the second separation strainer is using multistage
Strainer.
Further, the gas vent of first adsorption tanks passes through the 4th electromagnetism on-off valve, exhaust outlet pipeline and the external world
Environmental communication.The gas vent of second adsorption tanks is connected to by the 5th electromagnetism on-off valve, exhaust outlet pipeline with external environment.
The 12nd electromagnetism on-off valve and the 13rd electromagnetism on-off valve and vapor provide and are provided with air filter between device.
It further, further include fresh air system the present invention is based on the volatile organic matter condensate recycling device of macroreticular resin.
The air outlet of the fresh air system is connect with the first adsorption tanks by the 14th electromagnetism on-off valve, passes through the tenth with the second adsorption tanks
The connection of five electromagnetism on-off valves.
The condensation recycling method of the volatile organic matter condensate recycling device based on macroreticular resin is specific as follows:
Step 1: the first electromagnetism on-off valve, the second electromagnetism on-off valve, the 12nd electromagnetism on-off valve, the 8th electromagnetism on-off valve
And the tenth electromagnetism on-off valve open.The air inlet for capturing tower is continually fed into the exhaust gas processed containing volatile organic matter.It captures
Tower absorbs the component that water is dissolved in exhaust gas processed.
Step 2: the exhaust gas processed for capturing tower output is passed through dry filter, dry filter filters out exhaust gas processed
In solid particle.
Step 3: the exhaust gas processed of dry filter output enters the first adsorption tanks, the multiple field in the first adsorption tanks
Absorbent module absorbs the volatile organic matter in exhaust gas processed.Later, gas vent of the exhaust gas processed from the first adsorption tanks
Discharge.
Step 4: 2~4 as a child after, the second electromagnetism on-off valve close, third electromagnetism on-off valve open, dry filter
The exhaust gas processed of output enters the second adsorption tanks, and the Multi-layer absorption component in the second adsorption tanks absorbs in exhaust gas processed
Volatile organic matter.
7th electromagnetism on-off valve and the 13rd electromagnetism on-off valve are closed, the 6th electromagnetism on-off valve and the 12nd electromagnetism on-off valve
It opens, the spray head in the first adsorption tanks is opened, and the spray head in the second adsorption tanks is closed.Spray head in first adsorption tanks to
Multi-layer absorption component is sprayed water in first adsorption tanks, and vapor provides Multi-layer absorption component of the device into the first adsorption tanks and blows
Steam out.In first adsorption tanks Multi-layer absorption component absorption volatile organic matter after eluting with Multi-layer absorption component
Separation, the condenser into liquid separation loop module.Liquid separation loop module to the mixture of volatile organic matter and water at
Reason and recycling.
Step 5: 2~4 as a child after, third electromagnetism on-off valve close, the second electromagnetism on-off valve open, dry filter
The exhaust gas processed of output enters the first adsorption tanks, and the Multi-layer absorption component in the first adsorption tanks absorbs to be waved in exhaust gas processed
Hair property organic matter.6th electromagnetism on-off valve and the 12nd electromagnetism on-off valve are closed, and the 7th electromagnetism on-off valve and the 13rd electromagnetism are logical
Disconnected valve is opened, and the spray head in the first adsorption tanks is closed, and the spray head in the second adsorption tanks is opened.Spray in second adsorption tanks
Head Multi-layer absorption component into the second adsorption tanks is sprayed water, and vapor provides Multi-layer absorption group of the device into the second adsorption tanks
Part blows out steam.In second adsorption tanks Multi-layer absorption component absorption volatile organic matter after eluting with Multi-layer absorption
Component separation, the condenser into liquid separation loop module.Liquid separation loop module to the mixture of volatile organic matter and water into
Row processing and recycling.
Step 6: circulation executes step 4 and five.
Further, the method tool that liquid separation loop module is handled and recycled to the mixture of volatile organic matter and water
Body is as follows:
Step 1: condenser starts, the condensation flow quantity of condenser and the volatile organic matter and water of input condenser are mixed
The volume ratio for closing logistics capacity is a:1,15≤a≤35, so that the volatile organic matter in mixture liquefies.
Step 2: Gas and liquid flow diverter transmits the gas contained in mixture that condenser exports through the 9th electromagnetism on-off valve
To the first adsorption tanks or the second adsorption tanks.
Step 3: Liquid liquid Separation device separates the water in mixture that Gas and liquid flow diverter exports with volatile organic matter, and
Drip tray is delivered water into, the property of will volatilize organic matter is transported to fluid reservoir through measuring tank.
The invention has the advantages that:
1, adsorption condensing is high-efficient.
The present invention can efficiently go volatile organic matter (VOCs), inorganic matter, ammonia, organic amine in removing exhaust gas etc. main
Pollutant and various foul smells, adsorption efficiency is up to 90% or more, and condensing recovery efficiency is up to 95% or more, exhaust emissions
Substantially exceed " emission standard for odor pollutants " (GB14554-93) and " discharge standard of air pollutants " (GB 16297-
1996) discharge standard.
2, adaptable.
Multi-layer absorption component in the present invention by grid, separation strainer, macroreticular resin layer, grid, macroreticular resin layer,
The volatility that the structure that separation strainer, bright rock layers are sequentially stacked is capable of efficient absorption chemical industry high concentration difficulty catalytic degradation is organic
Object, and cryogenic condensation recycling is carried out, it is suitable for middle low concentration, atm number, the purified treatment of different VOCs gaseous matters
3, the present invention is by the modes of two adsorption tanks alternate runs, can daily 24 continuous throughout the twenty-four hour24, it is stable
Reliably.
4, the present invention recycles VOCs gas by cryogenic condensation, and in such a way that 150 DEG C of hot steams purge macroreticular resin
VOCs gas is desorbed, can be avoided the secondary pollution waste water that traditional macroreticular resin steam temperature-switching method desorption generates a large amount of high COD
The problem of.
Detailed description of the invention
Fig. 1 is overall structure diagram of the invention；
Fig. 2 is the connection schematic diagram of parallel macroporous resin adsorption tank in the present invention；
Fig. 3 is the structural schematic diagram of the first adsorption tanks and the second adsorption tanks in the present invention.
Specific embodiment
Below in conjunction with attached drawing, the invention will be further described.
As illustrated in fig. 1 and 2, the volatile organic matter condensate recycling device based on macroreticular resin, including gas adsorption modules,
Liquid separation loop module, fresh air system 14 and vapor provide device 13.Gas adsorption modules include capturing tower 1, dry filter 2
With parallel macroporous resin adsorption tank.Parallel macroporous resin adsorption tank includes the first adsorption tanks 3 and the second adsorption tanks 4.It captures
The air outlet of tower 1 is connect with the air inlet of dry filter 2.The air inlet of the air outlet of dry filter 2 and the first air-introduced machine 12
Mouth connection.The air outlet of first air-introduced machine 12 is connected to the air inlet of the first electromagnetism on-off valve 5-1.First electromagnetism on-off valve 5-1
Gas outlet be connected to the air inlet of the second electromagnetism on-off valve 5-2 and third electromagnetism on-off valve 5-3.Second electromagnetism on-off valve 5-2,
The gas outlet of third electromagnetism on-off valve 5-3 and the air inlet of the first adsorption tanks 3, the second adsorption tanks 4 are separately connected.First adsorption tanks
3 gas vent is connected to by the 4th electromagnetism on-off valve 5-4, exhaust outlet pipeline with external environment.The gas of second adsorption tanks 4 goes out
Mouth is connected to by the 5th electromagnetism on-off valve 5-5, exhaust outlet pipeline with external environment.
Liquid separation loop module includes condenser 6, Gas and liquid flow diverter 7, Liquid liquid Separation device 8, drip tray 10, measuring tank 9 and storage
Flow container 11.The liquid outlet of the input port of condenser 6 and the first adsorption tanks 3 passes through the 6th electromagnetism on-off valve 5-6 and the second air inducing
Machine 16 connects, and is connect with the liquid outlet of the second adsorption tanks 4 by the 7th electromagnetism on-off valve 5-7 and third air-introduced machine 17.Condensation
The delivery outlet of device 6 is connect with the input port of Gas and liquid flow diverter 7.The liquid outlet of Gas and liquid flow diverter 7 and Liquid liquid Separation device 8 into
The connection of liquid mouth, gas delivery port are connect with the air inlet of the 8th electromagnetism on-off valve 5-8.The gas outlet of 8th electromagnetism on-off valve 5-8
It is connect with the air inlet of the 9th electromagnetism on-off valve 5-9.The gas outlet of 9th electromagnetism on-off valve 5-9 and the second electromagnetism on-off valve 5-2
And the air inlet connection of third electromagnetism on-off valve 5-3.First liquid outlet of Liquid liquid Separation device 8 is connect with the inlet of measuring tank 9,
Second liquid outlet is connect with the entrance of drip tray 10.The liquid outlet of measuring tank 9 is connect with the inlet of fluid reservoir 11.Liquid liquid Separation
The top of device 8 and measuring tank 9 offers gas vent.Gas vent and the 9th electromagnetism on-off valve 5-9 on Liquid liquid Separation device 8
Air inlet pass through the tenth electromagnetism on-off valve 5-10 connection.Gas vent and the 9th electromagnetism on-off valve 5-9 on measuring tank 9 into
Port passes through the 11st electromagnetism on-off valve 5-11 connection.
As shown in Fig. 2, vapor provides the steam outlet of device 13 and the first adsorption tanks 3 pass through the 12nd electromagnetism on-off
Valve 5-12 connection is connect with the second adsorption tanks 4 by the 13rd electromagnetism on-off valve 5-13.12nd electromagnetism on-off valve 5-12 and
13 electromagnetism on-off valve 5-13 and vapor provide and are provided with air filter 15 between device 13.The air outlet of fresh air system 14
It is connect with the first adsorption tanks 3 by the 14th electromagnetism on-off valve 5-14, passes through the 15th electromagnetism on-off valve 5- with the second adsorption tanks 4
15 connections.Vapor provides device 13 and is used to input vapor to the first adsorption tanks 3 and the second adsorption tanks 4.Fresh air system 14 is used
In to 4 air blast of the first adsorption tanks 3 and the second adsorption tanks, to control in adsorption process in the first adsorption tanks 3 and the second adsorption tanks 4
Temperature is maintained between 0~40 DEG C.
Tower 1 is captured, from bottom to up includes reservoir bed, gas enters layer, level-one removes wet layer, level-one spraying layer, second level dehumidifying
Layer, second level spraying layer, demisting layer；Gas enters layer equipped with gas feed；Level-one is stainless except the filler that wet layer, second level remove wet layer
One of steel, polypropylene, polytetrafluoroethylene (PTFE) are a variety of；Level-one spraying layer, second level spraying layer roof spray system be added with
The aqueous solution of inorganic acid, for effectively absorbing dimethylamine exhaust gas；The steam and do not locate that demisting layer is taken out of after handling for removal
Manage complete particulate solid；Air outlet is provided at the top of demisting layer.
Dry filter 2 includes low efficient filter, medium effeciency filter and high efficiency particulate air filter.Low efficient filter, medium air filtration
Device, high efficiency particulate air filter are arranged successively setting to the direction of air outlet along the air inlet of dry filter 2.Low efficient filter uses can
304 stainless steel cloths of recycling.Using non-woven fabrics or glass fibre as filter medium, filter partial size is medium effeciency filter
1~5 μm, filter efficiency is 60~95% (passing through colorimetric method for determining), and using increasing density structure, fibre structure intensity is high, bullet
Property is good, and resistance is small, and dust containing capacity is big.High efficiency filter is used as filter medium using porous ultra-fine fibre glass paper, filters partial size
It is 0.1~0.5 μm, the solid captured in gas, liquid particle (fine particles of 0.1~0.5um of trapping) can be separated.
As shown in figure 3, the first adsorption tanks 3 and the second adsorption tanks 4 are identical equipment, including tank body 3-1, stabilizer blade 3-2, spray
Head 3-3 and Multi-layer absorption component 3-4.The bottom of two stabilizer blade 3-2 and tank body 3-1 is fixed.Dimension is offered at the top of tank body 3-1
Repair personnel's import.The both ends of tank body 3-1 are respectively provided with there are two sensor pocket pipeline 3-5.Four sensor pocket pipeline 3-5's
Inner end is connected to the inner cavity tank body 3-1, and outer end is closed by end cap.Temperature is provided in four sensor pocket pipeline 3-5
Spend sensor.
Tank body 3-1 is provided with spray head 3-3 at the top of inner cavity.Spray head 3-3 is connect with water tank by water pump.Multiple field is inhaled
The middle part of the inner cavity tank body 3-1 is arranged in attached component 3-4, and the inner cavity tank body 3-1 is divided into Multi-layer absorption component 3-4 or more
Filter ante-chamber and Multi-layer absorption component 3-4 filter back cavity below.Multi-layer absorption component 3-4 include be sequentially stacked from the bottom to top and
The first equal grid of thickness, the first separation strainer, the first macroreticular resin layer, the second grid, the second macropore resin layer, second point
From strainer, bright rock layers.First macroreticular resin layer and the second macropore resin layer be all made of polydivinylbenezene (PDVB), polyethylene,
Any one in polystyrene, poly- phenolic aldehyde or two kinds.The preferred polydivinylbenezene of macroreticular resin layer (PDVB) in the present embodiment.
Bigger serface, distinctive cellular structure and the superpower hydrophobicity having due to polydivinylbenezene (PDVB), can be right
VOCs gas plays good adsorption effect.First separation strainer and the second separation strainer are using multistage strainer.Tank body 3-1 into
Port 3-6 is connected to the filter ante-chamber in tank body 3-1, and gas vent 3-7 is connected to the filter back cavity in tank body 3-1.Tank body 3-1 into
The both ends of tank body 3-1 are not arranged in by port 3-6, gas vent 3-7.The liquid outlet 3-8 of tank body 3-1 is arranged in tank body 3-1's
Bottom, and be connected to filter back cavity.The metal of more perforation Multi-layer absorption component 3-4 is provided on Multi-layer absorption component 3-4
Stick.All metal bars are grounded.Spot style conduction mode is formd, possible accumulation of static electricity is effectively prevented.
It is sequentially stacked using grid, separation strainer, macroreticular resin layer, grid, macroreticular resin layer, separation strainer, bright rock layers
Multi-layer absorption component 3-4, can reduce 10~15% or so the pressure losses while improving absorption property.Spray head
3-3 is used to be sprayed after running certain period (two hours adsorption desorption periods), to keep the adsorption activity of macroreticular resin.
The spray termination condition of spray head 3-3 is not muddy to be diluted with water in the liquid tube of outflow in tank body 3-1.Spray head 3-3 spray
During leaching, the temperature in tank body 3-1 is controlled between 180~220 DEG C.
Condenser 6 is designed using HTRI software, using the stainless steel with a thickness of 0.5~1.0mm as chief series pipe, is mentioned
High heat exchange efficiency.The shell of condenser 6 is made up of by two the half-shell that expansion joint connects.Expansion joint can compensate for shell because
Additional stress caused by the temperature difference improves service life so that condenser 6 is more safe and reliable.Condenser 6 uses shell-and-tube
Heat exchanger, the baffle plate in condenser 6 twist, and offer multiple through-holes.Area is utilized to improve baffle plate,
Liquid heat exchange dead angle phenomenon is eliminated, the cooling effect of condenser 6 is increased.The condensate liquid that condenser 6 uses is entering condenser 6
Preceding temperature is 0 DEG C~25 DEG C, and 90% or more recyclable VOCs (organic exhaust gas) can be covered while reducing energy consumption, makes it
Liquefaction is recycled.
The condensation recycling method of the volatile organic matter condensate recycling device based on macroreticular resin is specific as follows:
Step 1: the first electromagnetism on-off valve 5-1, the second electromagnetism on-off valve 5-2, the 12nd electromagnetism on-off valve 5-12, the tenth
Four electromagnetism on-off valve 5-14, the 8th electromagnetism on-off valve 5-8, the 9th electromagnetism on-off valve 5-9, the tenth electromagnetism on-off valve 5-10 and the tenth
One electromagnetism on-off valve 5-11 opens (connection).The air inlet of capture tower 1 is continually fed into processed useless containing volatile organic matter
Gas.It captures tower 1 and absorbs the component for being dissolved in water in exhaust gas processed.
Step 2: capturing the exhaust gas processed that tower 1 exports is passed through dry filter 2, dry filter 2 filters out processed useless
Solid particle in gas.
Step 3: the exhaust gas processed that dry filter 2 exports enters the first adsorption tanks 3, the multilayer in the first adsorption tanks 3
Formula absorbent module 3-4 absorbs the volatile organic matter in exhaust gas processed.Later, gas of the exhaust gas processed from the first adsorption tanks 3
Body outlet discharge.
Step 4: two as a child after, the second electromagnetism on-off valve 5-2 and the 14th electromagnetism on-off valve 5-14 are closed, third electricity
Magnetic on-off valve 5-3, the 15th electromagnetism on-off valve 5-15 are opened, and the exhaust gas processed that dry filter 2 exports enters the second absorption
Tank 4, the Multi-layer absorption component 3-4 in the second adsorption tanks 4 absorb the volatile organic matter in exhaust gas processed.Later, located
Exhaust gas is managed to be discharged from the gas vent of the second adsorption tanks 4.
7th electromagnetism on-off valve 5-7 and the 13rd electromagnetism on-off valve 5-13 is closed, the 6th electromagnetism on-off valve 5-6 and the 12nd
Electromagnetism on-off valve 5-12 is opened, and the spray head 3-3 in the first adsorption tanks 3 is opened, and the spray head 3-3 in the second adsorption tanks 4 is closed.
Air pressure in the first adsorption tanks 3 is adjusted to 15-80kPa.Spray head 3-3 in first adsorption tanks 3 multilayer into the first adsorption tanks
Formula absorbent module 3-4 water spray, vapor provide Multi-layer absorption component 3-4 of the device 13 into the first adsorption tanks and blow out 150 DEG C
Hot steam.The volatile organic matter of Multi-layer absorption component 3-4 absorption in first adsorption tanks is inhaled after eluting with multiple field
Attached component 3-4 separation, enters the condenser 6 in liquid separation loop module from the 6th electromagnetism on-off valve 5-6.Liquid separation loop module is to waving
The mixture of hair property organic matter and water is handled and is recycled.
Step 5: two as a child after, third electromagnetism on-off valve 5-3, the 15th electromagnetism on-off valve 5-15 close, the second electromagnetism
On-off valve 5-2 and the 14th electromagnetism on-off valve 5-14 is opened, and the exhaust gas processed that dry filter 2 exports enters the first adsorption tanks
3, the Multi-layer absorption component 3-4 in the first adsorption tanks 3 absorbs volatile organic matter in exhaust gas processed.Later, processed useless
Gas is discharged from the gas outlet of the first adsorption tanks 3.
6th electromagnetism on-off valve 5-6 and the 12nd electromagnetism on-off valve 5-12 is closed, the 7th electromagnetism on-off valve 5-7 and the 13rd
Electromagnetism on-off valve 5-13 is opened, and the spray head 3-3 in the first adsorption tanks 3 is closed, and the spray head 3-3 in the second adsorption tanks 4 is opened.
Air pressure in the second adsorption tanks 4 is adjusted to 15-80kPa.Spray head 3-3 in second adsorption tanks 4 multilayer into the second adsorption tanks
Formula absorbent module water spray, vapor provide the heat steaming that Multi-layer absorption component of the device 13 into the second adsorption tanks blows out 150 DEG C
Vapour.In second adsorption tanks 4 Multi-layer absorption component 3-4 absorption volatile organic matter after eluting with Multi-layer absorption component
3-4 separation, enters the condenser 6 in liquid separation loop module from the 7th electromagnetism on-off valve 5-7.Liquid separation loop module has volatility
The mixture of machine object and water is handled and is recycled.
Step 6: circulation executes step 4 and five.
The method that liquid separation loop module is handled and recycled to the mixture of volatile organic matter and water is specific as follows:
Step 1: condenser 6 starts, the condensation flow quantity of condenser 6 and the volatile organic matter and water for inputting condenser 6
The volume ratio of mixture flow rate is a:1,15≤a≤35, so that the volatile organic matter in mixture liquefies.
Step 2: Gas and liquid flow diverter 7 is by the gas contained in mixture that condenser 6 exports through the 9th electromagnetism on-off valve 5-
9 are transferred to the first adsorption tanks 3 or the second adsorption tanks 4.
Step 3: Liquid liquid Separation device 8 separates the water in mixture that Gas and liquid flow diverter 7 exports with volatile organic matter,
And drip tray 10 is delivered water into, the property of will volatilize organic matter is transported to fluid reservoir 11 through measuring tank 9.
Claims (10)
1. the volatile organic matter condensate recycling device based on macroreticular resin, including gas adsorption modules, liquid separation loop module and
Vapor provides device；It is characterized by: the gas adsorption modules include capturing tower, dry filter and parallel macropore
Resin adsorption tank；The parallel macroporous resin adsorption tank includes the first adsorption tanks and the second adsorption tanks；The capture tower
The connection of the air inlet of air outlet and dry filter；The air inlet of the air outlet of the dry filter and the first air-introduced machine connects
It connects；The air outlet of first air-introduced machine is connected to the air inlet of the first electromagnetism on-off valve；The gas outlet of first electromagnetism on-off valve and the
The connection of the air inlet of two electromagnetism on-off valves and third electromagnetism on-off valve；The outlet of second electromagnetism on-off valve, third electromagnetism on-off valve
The air inlet of mouth and the first adsorption tanks, the second adsorption tanks is separately connected；
The liquid separation loop module includes condenser, Gas and liquid flow diverter, Liquid liquid Separation device and fluid reservoir；The input port of condenser
It is connect with the liquid outlet of the first adsorption tanks by the 6th electromagnetism on-off valve, passes through the 7th electricity with the liquid outlet of the second adsorption tanks
The connection of magnetic on-off valve；The delivery outlet of condenser and the input port of Gas and liquid flow diverter connect；The liquid outlet of Gas and liquid flow diverter with
The inlet of Liquid liquid Separation device connects, and gas delivery port is connect with the air inlet of the 8th electromagnetism on-off valve；8th electromagnetism on-off valve
Gas outlet connect with the air inlet of the 9th electromagnetism on-off valve；The gas outlet of 9th electromagnetism on-off valve and the second electromagnetism on-off valve and
The air inlet of third electromagnetism on-off valve connects；Second liquid outlet of Liquid liquid Separation device is connect with fluid reservoir；The of Liquid liquid Separation device
One liquid outlet is connect with fluid reservoir；The air inlet of gas vent and the 9th electromagnetism on-off valve on Liquid liquid Separation device passes through the tenth electricity
The connection of magnetic on-off valve；
The steam outlet that the vapor provides device is connect with the first adsorption tanks by the 12nd electromagnetism on-off valve, with the
Two adsorption tanks are connected by the 13rd electromagnetism on-off valve；
First adsorption tanks and the second adsorption tanks are identical equipment, including tank body, spray head and Multi-layer absorption component；Institute
It states and is provided with spray head at the top of tank inner chamber；The Multi-layer absorption component is arranged in the middle part of tank inner chamber, and by tank
Intracoelomic cavity is divided into filter ante-chamber and filter back cavity；Multi-layer absorption component includes the first grid being sequentially stacked from the bottom to top, first
Separate strainer, the first macroreticular resin layer, the second grid, the second macropore resin layer, the second separation strainer, bright rock layers；Tank body into
Port is connected to the intracorporal filter ante-chamber of tank, and gas vent is connected to the intracorporal filter back cavity of tank；The liquid outlet of tank body is arranged in tank
The bottom of body, and be connected to filter back cavity.
2. the volatile organic matter condensate recycling device according to claim 1 based on macroreticular resin, it is characterised in that: institute
The capture tower stated includes reservoir bed from bottom to up, gas enters layer, level-one removes wet layer, level-one spraying layer, second level are except wet layer, two
Grade spraying layer, demisting layer；Gas enters layer equipped with gas feed；Level-one is stainless steel, gathers except the filler that wet layer, second level remove wet layer
One of propylene, polytetrafluoroethylene (PTFE) are a variety of；Level-one spraying layer, second level spraying layer roof spray system be added with inorganic acid
Aqueous solution；Air outlet is provided at the top of demisting layer.
3. the volatile organic matter condensate recycling device according to claim 1 based on macroreticular resin, it is characterised in that: institute
The dry filter stated includes low efficient filter, medium effeciency filter and high efficiency particulate air filter；The low efficient filter, medium air filtration
Device, high efficiency particulate air filter are arranged successively setting to the direction of air outlet along the air inlet of dry filter；Low efficient filter uses 304
Stainless steel cloth；For medium effeciency filter using non-woven fabrics or glass fibre as filter medium, filtering partial size is 1~5 μm；Efficient mistake
Using the filter medium that is used as of porous ultra-fine fibre glass paper, filtering partial size is 0.1~0.5 μm for filter；The condenser is adopted
Use stainless steel with a thickness of 0.5~1.0mm as chief series pipe；The shell of condenser is by two half-shell groups being connected by expansion joint
At；Condenser uses shell-and-tube exchanger, and the baffle plate in condenser twist, and offers multiple through-holes.
4. the volatile organic matter condensate recycling device according to claim 1 based on macroreticular resin, it is characterised in that: institute
The first adsorption tanks and the second adsorption tanks stated further include stabilizer blade；The bottom of two stabilizer blades and tank body is fixed；The top of the tank body
Portion offers maintenance personal's import；The both ends of the tank body are respectively provided with there are two sensor pocket pipeline；Four sensor pockets
The inner end of pipeline is connected to tank inner chamber, and outer end is closed by end cap；Temperature is provided in four sensor pocket pipelines
Spend sensor.
5. the volatile organic matter condensate recycling device according to claim 1 based on macroreticular resin, it is characterised in that: institute
The liquid separation loop module stated further includes drip tray and measuring tank；Second liquid outlet of the drip tray and Liquid liquid Separation device connects
It connects；Measuring tank is arranged between Liquid liquid Separation device and fluid reservoir；Gas vent and the 9th electromagnetism on-off valve on measuring tank into
Port is connected by the 11st electromagnetism on-off valve.
6. the volatile organic matter condensate recycling device according to claim 1 based on macroreticular resin, it is characterised in that: institute
The metal bar of more perforation Multi-layer absorption components is provided on the Multi-layer absorption component stated；All metal bars are grounded；Institute
The the first macroreticular resin layer and the second macropore resin layer stated be all made of polydivinylbenezene, polyethylene, polystyrene, in poly- phenolic aldehyde
Any one or two kinds；The first separation strainer and the second separation strainer is using multistage strainer.
7. the volatile organic matter condensate recycling device according to claim 1 based on macroreticular resin, it is characterised in that: institute
The gas vent for stating the first adsorption tanks is connected to by the 4th electromagnetism on-off valve, exhaust outlet pipeline with external environment；Described second inhales
The gas vent of attached tank is connected to by the 5th electromagnetism on-off valve, exhaust outlet pipeline with external environment；12nd electromagnetism is logical
Disconnected valve and the 13rd electromagnetism on-off valve and vapor, which provide, is provided with air filter between device.
8. the volatile organic matter condensate recycling device according to claim 1 based on macroreticular resin, it is characterised in that: this
Volatile organic matter condensate recycling device of the invention based on macroreticular resin further includes fresh air system；The air outlet of the fresh air system
It is connect with the first adsorption tanks by the 14th electromagnetism on-off valve, is connect with the second adsorption tanks by the 15th electromagnetism on-off valve.
9. the condensation recycling method of the volatile organic matter condensate recycling device based on macroreticular resin as described in claim 1,
It is characterized by: Step 1: the first electromagnetism on-off valve, the second electromagnetism on-off valve, the 12nd electromagnetism on-off valve, the 8th electromagnetism on-off
Valve and the tenth electromagnetism on-off valve are opened；The air inlet for capturing tower is continually fed into the exhaust gas processed containing volatile organic matter；It catches
It catches tower and absorbs the component for being dissolved in water in exhaust gas processed；
Step 2: the exhaust gas processed for capturing tower output is passed through dry filter, dry filter is filtered out in exhaust gas processed
Solid particle；
Step 3: the exhaust gas processed of dry filter output enters the first adsorption tanks, the Multi-layer absorption in the first adsorption tanks
Component absorbs the volatile organic matter in exhaust gas processed；Later, exhaust gas processed is discharged from the gas vent of the first adsorption tanks；
Step 4: 2~4 as a child after, the second electromagnetism on-off valve close, third electromagnetism on-off valve open, dry filter output
Exhaust gas processed enter the second adsorption tanks, the Multi-layer absorption component in the second adsorption tanks absorbs the volatilization in exhaust gas processed
Property organic matter；
7th electromagnetism on-off valve and the 13rd electromagnetism on-off valve are closed, and the 6th electromagnetism on-off valve and the 12nd electromagnetism on-off valve are opened
It opens, the spray head in the first adsorption tanks is opened, and the spray head in the second adsorption tanks is closed；Spray head in first adsorption tanks is to
Multi-layer absorption component is sprayed water in one adsorption tanks, and vapor provides Multi-layer absorption component blowout of the device into the first adsorption tanks
Steam；The volatile organic matter of Multi-layer absorption component absorption in first adsorption tanks divides after eluting with Multi-layer absorption component
From condenser into liquid separation loop module；Liquid separation loop module handles the mixture of volatile organic matter and water
And recycling；
Step 5: 2~4 as a child after, third electromagnetism on-off valve close, the second electromagnetism on-off valve open, dry filter output
Exhaust gas processed enter the first adsorption tanks, the Multi-layer absorption component in the first adsorption tanks absorbs volatility in exhaust gas processed
Organic matter；6th electromagnetism on-off valve and the 12nd electromagnetism on-off valve are closed, the 7th electromagnetism on-off valve and the 13rd electromagnetism on-off valve
It opens, the spray head in the first adsorption tanks is closed, and the spray head in the second adsorption tanks is opened；Spray head in second adsorption tanks to
Multi-layer absorption component is sprayed water in second adsorption tanks, and vapor provides Multi-layer absorption component of the device into the second adsorption tanks and blows
Steam out；In second adsorption tanks Multi-layer absorption component absorption volatile organic matter after eluting with Multi-layer absorption component
Separation, the condenser into liquid separation loop module；Liquid separation loop module to the mixture of volatile organic matter and water at
Reason and recycling；
Step 6: circulation executes step 4 and five.
10. the volatile organic matter condensate recycling device according to claim 9 based on macroreticular resin is condensed back to debit
Method, it is characterised in that: the method that liquid separation loop module is handled and recycled to the mixture of volatile organic matter and water is specific
It is as follows:
Step 1: condenser starts, the condensation flow quantity of condenser and the volatile organic matter and aqueous mixtures for inputting condenser
The volume ratio of flow is a:1,15≤a≤35, so that the volatile organic matter in mixture liquefies；
Step 2: the gas contained in mixture that condenser exports is transferred to through the 9th electromagnetism on-off valve by Gas and liquid flow diverter
One adsorption tanks or the second adsorption tanks；
Step 3: Liquid liquid Separation device separates the water in mixture that Gas and liquid flow diverter exports with volatile organic matter, and by water
It is transported to drip tray, the property of will volatilize organic matter is transported to fluid reservoir through measuring tank.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110384995A (en) * | 2019-07-24 | 2019-10-29 | 中国电子工程设计院有限公司 | A kind of high boiling point organic compound waste gas treatment equipment and its processing method |
| CN111992014A (en) * | 2020-07-07 | 2020-11-27 | 江苏中科睿赛环境工程有限公司 | Macroporous resin adsorption, desorption, condensation and recovery system |
| CN114053827A (en) * | 2021-12-07 | 2022-02-18 | 绍兴金泰容器制造有限公司 | Organic waste gas adsorption and purification device |
| CN117379940A (en) * | 2023-12-12 | 2024-01-12 | 山东博旭节能设备有限公司 | Separation device is administered to physical treatment vocs tail gas |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101274150A (en) * | 2007-12-17 | 2008-10-01 | 蔡志煌 | Method for cleaning, recovering and treating painted lacquer exhaust organic gas and device |
| CN106693582A (en) * | 2017-01-05 | 2017-05-24 | 南京大学 | Method for separating and recycling organic solvent from dregs evaporation tail gas |
| CN108554172A (en) * | 2018-06-14 | 2018-09-21 | 杭州电子科技大学 | Dimethylamine exhaust gas controlling device and its technique in a kind of synthetic leather industry |
| CN209076354U (en) * | 2018-10-16 | 2019-07-09 | 杭州电子科技大学 | Volatile organic matter condensate recycling device based on macroreticular resin |
-
2018
- 2018-10-16 CN CN201811203081.XA patent/CN109224754A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101274150A (en) * | 2007-12-17 | 2008-10-01 | 蔡志煌 | Method for cleaning, recovering and treating painted lacquer exhaust organic gas and device |
| CN106693582A (en) * | 2017-01-05 | 2017-05-24 | 南京大学 | Method for separating and recycling organic solvent from dregs evaporation tail gas |
| CN108554172A (en) * | 2018-06-14 | 2018-09-21 | 杭州电子科技大学 | Dimethylamine exhaust gas controlling device and its technique in a kind of synthetic leather industry |
| CN209076354U (en) * | 2018-10-16 | 2019-07-09 | 杭州电子科技大学 | Volatile organic matter condensate recycling device based on macroreticular resin |
Non-Patent Citations (1)
| Title |
|---|
| 王志良 等著: "普通高等院校精品课程规划教材 暖通空调技术", 中国环境科学出版社, pages: 179 * |
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| CN110384995A (en) * | 2019-07-24 | 2019-10-29 | 中国电子工程设计院有限公司 | A kind of high boiling point organic compound waste gas treatment equipment and its processing method |
| CN111992014A (en) * | 2020-07-07 | 2020-11-27 | 江苏中科睿赛环境工程有限公司 | Macroporous resin adsorption, desorption, condensation and recovery system |
| CN114053827A (en) * | 2021-12-07 | 2022-02-18 | 绍兴金泰容器制造有限公司 | Organic waste gas adsorption and purification device |
| CN117379940A (en) * | 2023-12-12 | 2024-01-12 | 山东博旭节能设备有限公司 | Separation device is administered to physical treatment vocs tail gas |
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Application publication date: 20190118 |