CN109289512A - A kind of device and method of skid module formula processing VOCs exhaust gas - Google Patents
A kind of device and method of skid module formula processing VOCs exhaust gas Download PDFInfo
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- CN109289512A CN109289512A CN201811391346.3A CN201811391346A CN109289512A CN 109289512 A CN109289512 A CN 109289512A CN 201811391346 A CN201811391346 A CN 201811391346A CN 109289512 A CN109289512 A CN 109289512A
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- 238000000034 method Methods 0.000 title claims abstract description 76
- 238000012545 processing Methods 0.000 title claims abstract description 73
- 239000007921 spray Substances 0.000 claims abstract description 94
- 239000003463 adsorbent Substances 0.000 claims abstract description 76
- 230000003197 catalytic effect Effects 0.000 claims abstract description 54
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- 125000004122 cyclic group Chemical group 0.000 claims abstract description 32
- 239000000945 filler Substances 0.000 claims abstract description 12
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- 229910052799 carbon Inorganic materials 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 19
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 18
- 238000010521 absorption reaction Methods 0.000 claims description 17
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- 238000003795 desorption Methods 0.000 claims description 7
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- 238000007710 freezing Methods 0.000 claims description 5
- 230000008014 freezing Effects 0.000 claims description 5
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- 239000011941 photocatalyst Substances 0.000 claims description 5
- 238000006303 photolysis reaction Methods 0.000 claims description 5
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- 239000002808 molecular sieve Substances 0.000 claims description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 3
- 238000005516 engineering process Methods 0.000 abstract description 17
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- 239000007789 gas Substances 0.000 description 93
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 35
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- 238000001914 filtration Methods 0.000 description 8
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- 229910021529 ammonia Inorganic materials 0.000 description 5
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- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 4
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- 238000011068 loading method Methods 0.000 description 2
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- 230000003068 static effect Effects 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
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- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
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- 238000004073 vulcanization Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8678—Removing components of undefined structure
- B01D53/8687—Organic components
-
- 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
-
- 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
- B01D2255/00—Catalysts
- B01D2255/80—Type of catalytic reaction
- B01D2255/802—Photocatalytic
-
- 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
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/804—UV light
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention belongs to handle VOCs exhaust gas field, more particularly to a kind of device and method of skid module formula processing VOCs exhaust gas, the device of the skid module formula processing VOCs exhaust gas includes pretreatment spray apparatus, ultraviolet lamp catalytic unit, adsorbent equipment, condenser and cyclic water tank, the exhaust gas passes sequentially through pretreatment spray apparatus, ultraviolet lamp catalytic unit and adsorbent equipment, is filled with many-sided ball filler inside the pretreatment spray apparatus.The present invention, which provides, a kind of takes spray pretreatment+ultraviolet catalytic+adsorption technology treatment process combination, VOCs removal efficiency is up to 95% or more after spray, ultraviolet catalytic oxidation and adsorption treatment, suitable for the VOCs exhaust gas of all kinds of high-concentration and low-concentrations and occasion, has the advantages that the device and method for the skid module formula processing VOCs exhaust gas that applied widely, Operation and Maintenance is simple, safety, operating cost are low.
Description
Technical field
The invention belongs to handle VOCs exhaust gas field more particularly to a kind of skid module formula processing VOCs exhaust gas device and
Method.
Background technique
The prior art and defect:
VOCs (Volatile Organic Compounds, volatile organic matter) be a kind of strong volatility, it is irritant,
There are special odor, toxic organic gas, photochemical fog can be formed and destroy ozone layer, there is significant damage to environment；In addition,
VOCs can also inhibit human central nervous system, have certain carcinogenicity.Petroleum, chemical industry, automobile, printing and dyeing, electronics, metallurgy
Etc. industries can produce volatile organic matter.Existing VOCs processing technique include recovery technologies and the burnings such as condensation, absorption,
Technology is destroyed in photodissociation etc., still, single processing technique often exist processing not enough thoroughly, treatment effeciency is lower, higher cost,
Cause secondary pollution problems.
In addition, structure is complicated mostly for existing processing unit, involve great expense, it is fixedly mounted irremovable, for certain
The pollution sources that noncontinuity process, temporary device, emergency situations generate, are not able to satisfy its instant needs arrived.
Solve the difficulty and meaning of above-mentioned technical problem:
Therefore, these problems are based on, provides and a kind of takes spray pretreatment+ultraviolet catalytic+adsorption technology processing work
Skill combination, VOCs removal efficiency is suitable for all kinds of up to 95% or more after spray, ultraviolet catalytic oxidation and adsorption treatment
The VOCs exhaust gas of high-concentration and low-concentration and occasion has the advantages that the low sled of simple applied widely, Operation and Maintenance, safety, operating cost
The device and method of dress modular processing VOCs exhaust gas has important practical significance.
Summary of the invention
Present invention aims at for solve well-known technique present in technical problem and provide one kind take spray pretreatment+
The combination of ultraviolet catalytic+adsorption technology treatment process, VOCs is removed after spray, ultraviolet catalytic oxidation and adsorption treatment
Efficiency is up to 95% or more, suitable for the VOCs exhaust gas of all kinds of high-concentration and low-concentrations and occasion, with applied widely, Operation and Maintenance is simple
Easily, the device and method of the skid module formula processing VOCs exhaust gas of the low advantage of safety, operating cost.
Another object of the present invention is to provide a kind of using skid mould to solve technical problem present in well-known technique
Blockization design, facilitates vehicle-mounted transport, the setting of device subregion, and treating capacity is handled according to the skid module formula that on-site actual situations are adjusted
The device and method of VOCs exhaust gas.
The technical scheme adopted by the present invention to solve the technical problems existing in the known art is that
A kind of device of skid module formula processing VOCs exhaust gas, the device of the skid module formula processing VOCs exhaust gas include
Pretreatment spray equipment, ultraviolet lamp catalytic unit, adsorbent equipment, condenser and cyclic water tank, the exhaust gas pass sequentially through pre- place
Spray equipment, ultraviolet lamp catalytic unit and adsorbent equipment are managed, is filled with many-sided ball filler, institute inside the pretreatment spray equipment
It states the medicament in cyclic water tank and is sprayed at the many-sided ball filler surface, absorption in the adsorbent equipment by pre-processing circulating pump
It is regenerated after filling adsorption saturation by high-temperature steam, the high temperature exhaust steam that the regenerative process generates is carried out by the condenser
Condensation.
Present invention process takes spray pretreatment+ultraviolet catalytic+adsorption technology treatment process combination, through spray, purple
VOCs removal efficiency is up to 95% or more after outer photochemical catalytic oxidation and adsorption treatment, suitable for all kinds of high-concentration and low-concentrations and occasion
VOCs exhaust gas, applied widely, Operation and Maintenance is simple, safety, operating cost are low.
The present invention can also use following technical scheme:
In the device of above-mentioned skid module formula processing VOCs exhaust gas, further, the exhaust gas is conveyed by blower
To pretreatment spray equipment, pretreatment spray equipment upper outlet position is provided with demister, the import of the blower with
Outlet is connect by being flexible coupling the A and B that is flexible coupling with pipeline respectively.
Demister of the invention is to remove the mist carried secretly in removing exhaust gas or droplet.
The both ends of blower of the invention, which are taken, to be flexible coupling, and vibration influences the stability of static equipment when preventing blower from working.
In the device of above-mentioned skid module formula processing VOCs exhaust gas, further, the quantity of the adsorbent equipment is
Two, it is denoted as adsorbent equipment A and adsorbent equipment B, is filled with active carbon particle and molecular sieve, regenerative process in the adsorbent equipment
The high temperature exhaust steam of generation is sent directly into sewage draining exit after being condensed by the condenser, the not solidifying component of the condenser discharge returns
The pretreatment spray equipment continues with, and the condenser is to freeze unit recirculated water as refrigerant.
The adsorbent equipment is arranged using the using and the reserved, and each equipment is fixed on the base with support, adsorbent equipment A and absorption
Device B is vertical Space Facilities, is arranged using subregion, can enable halfth area or the whole district according to tolerance difference.
In the device of above-mentioned skid module formula processing VOCs exhaust gas, further, the pretreatment spray equipment bottom
Portion is communicated with cyclic water tank, and the pH value of liquid is pressurizeed by force (forcing) pump and squeezes into medicament holding from medicament storage tank in the cyclic water tank
Stablize, the cyclic water tank is provided with filter, and liquidometer B and PH meter, the medicament storage tank are equipped in the cyclic water tank
Inside it is provided with blender and liquidometer A.
Cyclic water tank is provided with filter, continues to use after the spray liquid of reflux is filtered, is provided with and stirs in medicament storage tank
Device is mixed, it is uniform to stir medicament.By monitoring high water tank height and pH value, automatically controls water inlet and added by dosing pump
Enter medicament.
In the device of above-mentioned skid module formula processing VOCs exhaust gas, further, the skid module formula processing
The device of VOCs exhaust gas is integrated on two skid pedestals, the steel construction that the pedestal makes for square steel or I-steel, and two
The pedestal is denoted as the blower that pipeline connection is provided on pedestal A and pedestal B, the pedestal A, pretreatment spray dress respectively
It sets, medicament storage tank, cyclic water tank, dosing pump, pretreatment circulating pump A, pre-process circulating pump B, ultraviolet lamp catalytic unit, pedestal B
On be disposed with condenser, freezing unit, adsorbent equipment A, adsorbent equipment B.
The device that present invention process system uses is designed using skid moduleization, facilitates vehicle-mounted transport, and processing unit uses
Subregion setting, treating capacity is according to on-site actual situations flexible modulation.Emission-control equipment is designed as skid module form, according to
Different enterprise demands draw the device for needing collection to handle to scene, connection by vehicle-mounted form, realize qualified discharge.Handle work
After work, then processing unit pulled away, be not take up place, does not increase the fixed device investment of enterprise, it can be different for different enterprises
Exhaust-gas treatment demand provides service, improves utilization rate.
In the device of above-mentioned skid module formula processing VOCs exhaust gas, further, the pretreatment spray equipment point
For left and right two chambers, it is denoted as left chamber and right chamber, exhaust gas is delivered to left chamber or right chamber by blower or conveys simultaneously
To two chambers, the adsorbent equipment is divided into the chamber of left, center, right three, is denoted as middle chamber, left chamber and right chamber, the chamber
Between using adsorbent material filling and one-way flow, through ultraviolet catalytic device, treated that exhaust gas is delivered to left chamber or right chamber
Room is delivered to two chambers simultaneously, is discharged after adsorbing through adsorbent material from middle chamber.
The pretreatment spray equipment and adsorbent equipment are vertical Space Facilities, are arranged using subregion, can be according to tolerance
Difference enables halfth area or the whole district.
A kind of method of skid module formula processing VOCs exhaust gas, the method for the skid module formula processing VOCs exhaust gas use
The device of skid module formula processing VOCs exhaust gas described in any of the above embodiments, the side of the skid module formula processing VOCs exhaust gas
Method is further comprising the steps of:
Step 1: the exhaust gas containing VOCs is pumped by blower to pretreatment spray equipment lower entrances through collection system, and with
The chemical washing liquid sprayed downwards comes into full contact with, and removes grease particle and part volatile organic matter, preprocessed spray equipment
Enter ultraviolet lamp catalytic unit after the dehydration of top demister demisting；
Step 2: the exhaust gas passes through the photodissociation of ultraviolet light and the catalytic action of photocatalyst, in a very short period of time oxygen
Change, decomposing pollutant molecule；
Step 3: the adsorption stuffing absorption of the adsorbent equipment by step 2 treated excessive ozone and place completely
The small molecule contaminants of reason；
Step 4: the adsorption stuffing after adsorption saturation uses high-temperature steam desorption and regeneration, the useless steaming generated in regenerative process
Vapour is passed through condenser and is condensed, and condensate liquid is sent directly into sewage draining exit and is handled, and not solidifying component can return to pretreatment spray dress
It sets and continues with.
For valuable organic waste materials, condensate liquid connects collecting vessel, and while environmentally friendly mode is handled, collecting can be maximum
Economic loss may be mitigated
In the method for above-mentioned skid module formula processing VOCs exhaust gas, further, the pretreatment unit spray temperature
Degree is 15~40 DEG C, and pressure is 101~500Kpa, and adsorbent equipment temperature is 15~40 DEG C, and pressure is 101~150Kpa.
In the method for above-mentioned skid module formula processing VOCs exhaust gas, further, the condenser is to freeze unit
Recirculated water is cooled to 38 DEG C as refrigerant, by 145 DEG C of high-temperature steam.
In the method for above-mentioned skid module formula processing VOCs exhaust gas, further, after step 4 desorption
Adsorbent it is dry by hot-air, humidity tester is set in the discharge outlet of the adsorbent equipment, when humidity reaches setting number
When value, drying process terminates.
In conclusion the present invention has the advantages that:
The present invention takes spray pretreatment+ultraviolet catalytic+adsorption technology treatment process combination, through spray, ultraviolet light
VOCs of the VOCs removal efficiency up to 95% or more, suitable for all kinds of high-concentration and low-concentrations and occasion after catalysis oxidation and adsorption treatment
Exhaust gas, applied widely, Operation and Maintenance is simple, safety, operating cost are low.
Detailed description of the invention
Technical solution of the present invention is described in further detail below with reference to drawings and examples, but should
Know, these attached drawings are designed for task of explanation, therefore not as the restriction of the scope of the invention.In addition, except non-specifically
It points out, these attached drawings are meant only to conceptually illustrate structure construction described herein, without to be drawn to scale.
Fig. 1 is VOCs exhaust gas spray pretreatment+ultraviolet catalytic+adsorption technology processing technological flow figure of the present invention；
Fig. 2 is skid module Formula V OCs processing unit forward sight arrangement schematic diagram of the present invention；
Fig. 3 is that skid module Formula V OCs processing unit of the present invention overlooks arrangement schematic diagram.
In figure:
1, be flexible coupling A, 2, blower, 3, be flexible coupling B, 4, pretreatment spray equipment, 5, many-sided ball filler, 6, demister, 7,
Ultraviolet catalytic device, 8, adsorbent equipment A, 9, adsorbent equipment B, 10, freezing unit, 11, condenser, 12, medicament storage tank, 13,
Blender, 14, liquidometer A, 15, dosing pump, 16, cyclic water tank, 17, filter, 18, PH meter, 19, liquidometer B, 20, pre- place
Manage circulating pump A, 21, pretreatment circulating pump B, 22, pedestal A, 23, pedestal B.
Specific embodiment
Firstly, it is necessary to which explanation, illustrates skid module formula processing of the invention for by way of example below
Specific structure, features and advantages of the device and method of VOCs exhaust gas etc., however what all descriptions were intended merely to be illustrated,
And it should not be construed as forming any restrictions to the present invention.In addition, being described by each embodiment mentioned by this paper or hidden
Any single technical characteristic contained, or shown or implicit any single technical characteristic in the drawings, still can be at this
Continue any combination between a little technical characteristics (or its equivalent) or delete, so that obtain not to mention directly herein
And more other embodiments of the invention.In addition, same or like technical characteristic is same for the sake of simplifying drawing
It may only be indicated at one in attached drawing.
It will be understood that when component ' attach ' to another component when it is said that, it can be directly connected to another component or
There may be intermediate members.On the contrary, when component " being directly connected to " being arrived another component when it is said that, then it represents that middle part is not present
Part.
Fig. 1 gives VOCs exhaust gas spray pretreatment+ultraviolet catalytic+adsorption technology processing technological flow figure of the present invention,
And it by the way that Fig. 2 shows skid module Formula V OCs processing unit forward sight arrangement schematic diagrams of the present invention, and is shown by Fig. 3
Skid module Formula V OCs processing unit of the present invention overlooks arrangement schematic diagram, below just Fig. 1 to Fig. 3 is combined to illustrate the present invention.
In order to further understand the content, features and effects of the present invention, the following examples are hereby given, and cooperate attached drawing
Detailed description are as follows:
A kind of device of skid module formula processing VOCs exhaust gas, the device of the skid module formula processing VOCs exhaust gas include
Pretreatment spray equipment 4, ultraviolet lamp catalytic unit 7, adsorbent equipment, condenser and cyclic water tank, the exhaust gas pass sequentially through pre-
Spray equipment 4, ultraviolet lamp catalytic unit 7 and adsorbent equipment are handled, 4 inside of pretreatment spray equipment is filled out filled with many-sided ball
Expect 5, the medicament in the cyclic water tank 16 is sprayed at 5 surface of many-sided ball filler, the absorption by pre-processing circulating pump
Device is regenerated by high-temperature steam, and the high-temperature steam is condensed by the condenser.
Present invention process takes spray pretreatment+ultraviolet catalytic+adsorption technology treatment process combination, through spray, purple
VOCs removal efficiency is up to 95% or more after outer photochemical catalytic oxidation and adsorption treatment, suitable for all kinds of high-concentration and low-concentrations and occasion
VOCs exhaust gas, applied widely, Operation and Maintenance is simple, safety, operating cost are low.
For further, it can also consider in the present invention, the exhaust gas is delivered to pretreatment spray dress by blower 2
4 are set, the 4 upper outlet position of pretreatment spray equipment is provided with demister 6.
Demister 6 is to remove the mist droplet carried secretly in removing exhaust gas.
For further, it can also consider in the present invention, the inlet and outlet of the blower 2 passes through respectively to be flexible coupling
A1 and the B3 that is flexible coupling are connect with pipeline.
The both ends of blower of the invention, which are taken, to be flexible coupling, and vibration influences the stability of static equipment when preventing blower 2 from working.
It should be pointed out that the quantity of the adsorbent equipment is two, it is denoted as adsorbent equipment A8 and adsorbent equipment B9, it is described
It is filled with active carbon particle and molecular sieve in adsorbent equipment, sewage draining exit is sent directly by the condensed condensate liquid of the condenser,
The not solidifying component of condenser discharge returns to the pretreatment spray equipment 4 and continues with, and the condenser 11 is with refrigerator
10 recirculated waters of group are as refrigerant.
The adsorbent equipment 8,9 is arranged using the using and the reserved, and each equipment is fixed on the base with support, adsorbent equipment A8 and
Adsorbent equipment B9 is vertical Space Facilities, is arranged using subregion, can enable halfth area or the whole district according to tolerance difference.
It should be pointed out that 4 bottom of pretreatment spray equipment is communicated with cyclic water tank 16, in the cyclic water tank 16
The pH value of liquid is pressurizeed by force (forcing) pump 15 and squeezes into medicament holding stabilization from medicament storage tank 12, and the cyclic water tank 16 was provided with
Filter 17 is equipped with liquidometer B19 and PH meter 18 in the cyclic water tank 16, is provided with blender 13 in the medicament storage tank 12
With liquidometer A14.
Cyclic water tank 16 is provided with filter 17, continues to use after the spray liquid of reflux is filtered, sets in medicament storage tank 12
It is equipped with blender 13, it is uniform to stir medicament.By monitoring high water tank height and pH value, automatically controls water inlet and pass through
Medicament is added in dosing pump.
For further, it can also consider in the present invention, the device collection of the skid module formula processing VOCs exhaust gas
At on two skid pedestals, the pedestal is the steel construction that square steel or I-steel make, and two pedestals are denoted as respectively
Blower 2, the pretreatment spray equipment 4, medicament storage tank that pipeline connects are provided on pedestal A and pedestal B, the pedestal A22
12, cyclic water tank 16, dosing pump 15, pretreatment circulating pump A20, pretreatment circulating pump B21, ultraviolet lamp catalytic unit 7, pedestal
Condenser 11, freezing unit 12, adsorbent equipment A8, adsorbent equipment B9 are disposed on B23.
The device that present invention process system uses is designed using skid moduleization, facilitates vehicle-mounted transport, and device uses subregion
Setting, treating capacity is according to on-site actual situations flexible modulation.Emission-control equipment is designed as skid module form, according to difference
Enterprise demand draws the device for needing collection to handle to scene, connection by vehicle-mounted form, realizes qualified discharge.Handle work knot
Shu Hou, then processing unit is pulled away, it is not take up place, does not increase the fixed device investment of enterprise, can be different enterprise's difference exhaust gas
Process demand provides service, improves utilization rate.
It should be pointed out that the pretreatment spray equipment 4 divides for left and right two chambers, it is denoted as left chamber and right chamber,
Exhaust gas is delivered to left chamber or right chamber or is delivered to two chambers simultaneously by blower 2, and the adsorbent equipment is divided into left, center, right
Three chambers are denoted as middle chamber, left chamber and right chamber, adsorbent material filling and one-way flow, warp are used between the chamber
Treated that exhaust gas is delivered to left chamber or right chamber or is delivered to two chambers simultaneously for ultraviolet catalytic device 7, through adsorption material
It is discharged after material absorption from middle chamber.
The pretreatment spray equipment 4 and adsorbent equipment are vertical Space Facilities, are arranged using subregion, can be according to tolerance
Difference enables halfth area or the whole district.
A kind of method of skid module formula processing VOCs exhaust gas, the method for the skid module formula processing VOCs exhaust gas use
The device of skid module formula processing VOCs exhaust gas described in any of the above embodiments, the side of the skid module formula processing VOCs exhaust gas
Method is further comprising the steps of:
Step 1: the exhaust gas containing VOCs is pumped by blower 2 to pretreatment 4 lower entrances of spray equipment through collection system, and
It is come into full contact with the chemical washing liquid sprayed downwards, removes grease particle and part volatile organic matter, preprocessed spray dress
Enter ultraviolet lamp catalytic unit 7 after setting the dehydration of 4 top demister, 6 demisting；
Step 2: the exhaust gas passes through the photodissociation of ultraviolet light and the catalytic action of photocatalyst, in a very short period of time oxygen
Change, decompose the contaminant molecules such as methyl mercaptan, ammonia, hydrogen sulfide；
Step 3: the adsorption stuffing absorption of the adsorbent equipment by step 2 treated excessive ozone and place completely
The small molecule contaminants of reason；
Step 4: the adsorption stuffing after adsorption saturation uses high-temperature steam desorption and regeneration, the useless steaming generated in regenerative process
Vapour is passed through condenser 11 and is condensed, and condensate liquid is sent directly into sewage draining exit and is handled, and not solidifying component can return to pretreatment spray
Device 4 continues with.
For valuable organic waste materials, condensate liquid connects collecting vessel, and while environmentally friendly mode is handled, collecting can be maximum
Economic loss may be mitigated.
It should be pointed out that it is 15~40 DEG C that the pretreatment spray equipment 4, which sprays temperature, pressure is 101~500Kpa,
Adsorbent equipment temperature is 15~40 DEG C, and pressure is 101~150Kpa.
It should be pointed out that the condenser 11 is to freeze 10 recirculated water of unit as refrigerant, by 145 DEG C of high-temperature steam
It is cooled to 38 DEG C.
It should be pointed out that the adsorbent after step 4 desorption is dry by hot-air, filled in the absorption
The discharge outlet setting humidity tester set, when humidity reaches setting numerical value, drying process terminates.
Present invention process takes spray pretreatment+ultraviolet catalytic+adsorption technology treatment process combination, pre- by spraying
Handle (removal rate (30%-50%), ultraviolet catalytic oxidation (removal rate 40%-60%), adsorption treatment (removal rate 90%-
95%)), overall removal rate breaches the limitation of single treatment technology up to 95% or more, before adsorbent equipment pretreatment and
Ultraviolet lamp catalysis oxidation reduces the adsorptive pressure of activated carbon adsorption device, reduces the operating cost of single adsorption device.Together
When, the group technology is compared to single treatment technology, suitable for the VOCs exhaust gas of all kinds of high-concentration and low-concentrations and occasion, the scope of application
Extensively, Operation and Maintenance is simple, safety, operating cost are low.
It as an example, in the present invention, further include supplement circulating water pipeline and overflow blow-off line, the supplement recirculated water
Pipeline carries out moisturizing to medicament storage tank 12 and cyclic water tank 16 respectively, pacifies on the supplement circulating water pipeline communicated with cyclic water tank 16
Equipped with the solenoid valve controlled by liquidometer B19.Overflow blow-off line includes cyclic water tank overflow water pipeline, cyclic water tank sewage pipe
Road and medicament storage tank blow-off line, the cyclic water tank blow-off line and medicament storage tank blow-off line are mounted on 12 He of medicament storage tank
Check-valves is installed on 16 bottom of cyclic water tank, the cyclic water tank blow-off line and medicament storage tank blow-off line.
As an example, in the present invention, exhaust gas containing VOCs is pumped by blower to pretreatment spray equipment through collection system, with
The chemical washing liquid of spray comes into full contact with, and generation is a series of chemically and physically to react, and removes grease particle and part volatility
Organic matter；Then enter ultraviolet lamp catalytic unit, photodissociation and photocatalyst by ultraviolet light after demisting dehydration at the top of device
Catalytic action, aoxidize in a very short period of time, decompose methyl mercaptan, ammonia, the contaminant molecules such as hydrogen sulfide；Ultraviolet photocatalyst catalysis
After oxidation, may there are excessive ozone and incompletely processed small molecule contaminants escape, under the action of adsorbent equipment, filtering reaches
Mark discharge.Pretreatment unit, ultraviolet light catalyzing device and adsorbent equipment all use subregion to be arranged, and can be opened according to tolerance difference
With halfth area or the whole district；Adsorbent equipment is designed using the using and the reserved, and the adsorbent material of adsorption saturation uses high-temperature steam desorption and regeneration.
The exhaust steam generated in regenerative process is passed through condenser and is condensed, and condensate liquid is sent directly into sewage draining exit and is handled, and does not coagulate group
Point can return to preprocessing module continues with.Applicability of the present invention is extensive, can handle various concentration, different tolerance, different fields
VOCs tail gas can facilitate shifting according to the different needs in pollution scene in addition by each module collection at two skid-mounted type structures
It is dynamic, improve the utilization rate of device.
As an example, in the present invention, the loading of pretreatment unit 4 is general to select depending on polyhedron empty ball specification
With 32/ φ 50 (mm) of φ, surface area is respectively 300/236 (m/m), and accumulation number is respectively 28500/11500 (n/m)；It is more
Face hollow sphere filler has high cycle speed, blade is more, and resistance is small, large specific surface area, high temperature resistant (< 120 compared to common fillers
DEG C), corrosion-resistant, the features such as surface hydrophilic performance is good, polyhedron empty ball filler is the prior art, is chiefly used in cooling tower, in recent years
It gradually uses in VOCs processing unit.
The pH value of liquid is according to acid in different occasion exhaust gas, alkaline matter concentration is default in cyclic water tank 16, as
Hydrogen containing partial vulcanization etc. in exhaust gas, presetting pH value is 8-10.
The chemical washing liquid sprayed downwards in pretreatment spray equipment 4 can configure special chemical drugs according to different occasions
The stronger medicament of agent, generally oxidisability, spray aproll amount are determined by filter area and spray volume density.
Active carbon filtration velocity≤0.3m/s in adsorbent equipment A8 and adsorbent equipment B9, gas is when active carbon effectively stops
Between >=1s, active carbon iodine number >=850m/g, carbon tetrachloride adsorption rate >=50%, mechanical strength >=90%, moisture content≤3%, water
Appearance >=66%, benzene adsorptive value >=450mg/g, adsorbance >=900mg/g, ash≤10%, specific surface area >=800m2/ g, Kong Mi
Spend the hole 50-300/m2, true specific gravity 2-2.2g/cm3, bulk density 0.35-0.55g/cm3。
Filler loading is according to adsorbent equipment internal filtration layer specification and filtering wind in adsorbent equipment A8 and adsorbent equipment B9
It is general calculation method depending on speed calculates.
Embodiment one: the middle and high concentration tail of a certain benzene,toluene,xylene containing pollutant, hydrogen sulfide, ammonia, methyl mercaptan is handled
Gas, gas flow 2500Nm3/h；Spray process is done with the diluted lye containing 5%NaOH, spray room temperature is room temperature (25
DEG C), atmospheric operation, the tail gas after spray is passed through bio-trickling processing unit (biological inoculum is existing matured product), through biochemistry
Enter adsorbent equipment after processing, adsorbent equipment temperature is 25 DEG C, adsorptive pressure 110KPa, loads normal activated carbon (active carbon mistake
Wind speed 0.35m/s is filtered, gas is in active carbon effective stay time 0.6s, active carbon iodine number 800m/g, moisture content 2%, specific surface
Product 750m2/ g, 100 holes of hole density/m2, true specific gravity 1.8g/cm3, bulk density 0.6g/cm3), obtained process results such as the following table 1:
1 process result of table
The embodiment is comparative example, using the prior art of VOCs processing technique: spray pretreatment+bio-trickling+
Activated carbon adsorption, some of the contaminants such as benzene is not up to discharge standard requirement after processing, and overall contamination removal rate is 81.24%,
The secondary pollutions such as solid waste are generated after the technique biochemical treatment, and biochemical device volume is larger, it is mobile inconvenient, it is disposable to put into
Larger, strain requires height to ambient humidity, and maintenance cost is higher.
Embodiment two: a certain tail gas for being 1% or so containing pollutant concentration of processing, gas flow 2500Nm3/h；With containing
The diluted lye of 5%NaOH does preposition spray process, and spray room temperature is room temperature (25 DEG C), atmospheric operation, the tail gas after spray
It is passed through bio-trickling processing unit (biological inoculum is existing matured product), this patent is entered after biochemical treatment and improves absorption dress
Left and right two chambers are set, adsorbent equipment temperature is 25 DEG C, adsorptive pressure 110KPa, and filling high-performance improves active carbon (active carbon
Filtration velocity 0.26m/s, gas is in active carbon effective stay time 1.15s, active carbon iodine number 1000m/g, moisture content 1%, than
Surface area 1000m2/ g, 200 holes of hole density/m2, true specific gravity 2g/cm3, bulk density 0.4g/cm3), obtained process results are as follows
Table 2:
2 process result of table
The embodiment is comparative example, using the prior art of VOCs processing technique: spray pretreatment+bio-trickling+
Activated carbon adsorption, but adsorbent equipment, using described in this patent, exhaust gas is conveyed from left and right two chambers increases exhaust gas and filler
Contact area, reduces filtration resistance, and adsorption stuffing improves active carbon particle, top charging, bottom discharge, place using high-performance
Each pollutant reaches discharge standard requirement after reason, and overall contamination removal rate is 89.74%.
Embodiment three: a certain tail gas for being 1% or so containing pollutant concentration of processing, gas flow 5000Nm3/h；With containing
The diluted lye of 5%NaOH does preposition spray process, and spray room temperature is 15 DEG C, pressure 101Kpa, and the tail gas after spray is passed through
Ultraviolet lamp catalytic oxidizing equipment (30 UV light tubes of filling, 150W/ branch), is passed through an adsorbent equipment left side after ultraviolet catalytic acts on
Right two chambers, adsorbent equipment temperature are 15 DEG C, adsorptive pressure 101KPa, filling high-performance improvement active carbon (active carbon filtering
Wind speed 0.26m/s, gas is in active carbon effective stay time 1.15s, active carbon iodine number 1000m/g, moisture content 1%, specific surface
Product 1000m2/ g, 200 holes of hole density/m2, true specific gravity 2g/cm3, bulk density 0.4g/cm3), obtained process results such as the following table 3:
3 process result of table
After spraying pretreatment+ultraviolet catalytic+absorption process, each pollutant concentration is all satisfied discharge standard
It is required that pollutants removal rate reaches 96.42%.The process operation is easy to maintain, and high degree of automation is stable, apparatus body
Product is moderate, can meet into sled movement.
Example IV: a certain tail gas for being 0.6% or so containing pollutant concentration of processing, gas flow 2500Nm3/h；With
The diluted lye containing 5%NaOH does preposition spray process, and spray room temperature is 40 DEG C, absolute pressure 500Kpa, and the tail gas after spray is logical
Enter ultraviolet lamp catalytic oxidizing equipment (20 UV light tubes of filling, 150W/ branch), is passed through adsorbent equipment after ultraviolet catalytic acts on
Left and right two chambers, adsorbent equipment temperature are 40 DEG C, adsorptive pressure 150KPa, and (active carbon filters wind to filling high performance active carbon
Fast 0.2m/s, gas is in active carbon effective stay time 1s, active carbon iodine number 1200m/g, moisture content 1%, specific surface area
1200m2/ g, 220 holes of hole density/m2, true specific gravity 2g/cm3, bulk density 0.4g/cm3), obtained process results such as the following table 4:
4 process result of table
After spraying pretreatment+ultraviolet catalytic+absorption process, each pollutant concentration is all satisfied discharge standard
It is required that pollutants removal rate reaches 96.81%.
Embodiment five: a certain tail gas for being 1% or so containing pollutant concentration of processing, gas flow 5000Nm3/h；With containing
The diluted lye of 5%NaOH does preposition spray process, and spray room temperature is room temperature (25 DEG C), atmospheric operation, the tail gas after spray
It is passed through ultraviolet lamp catalytic oxidizing equipment (30 UV light tubes of filling, 150W/ branch), obtained process results such as the following table 5:
5 process result of table
After spraying pretreatment+ultraviolet catalytic process, each pollutant concentration is all satisfied discharge standard requirement,
Pollutants removal rate only has 91.79%.
Embodiment six: a certain tail gas for being 1% or so containing pollutant concentration of processing, gas flow 5000Nm3/h；With containing
The diluted lye of 5%NaOH does preposition spray process, and spray room temperature is room temperature (25 DEG C), atmospheric operation, the tail gas after spray
It is passed through ultraviolet lamp catalytic oxidizing equipment (30 UV light tubes of filling, 150W/ branch), absorption dress is entered after ultraviolet catalytic acts on
It sets, adsorbent equipment temperature is 25 DEG C, adsorptive pressure 110KPa, filling high performance active carbon (active carbon filtration velocity 0.26m/s,
Gas is in active carbon effective stay time 1.15s, active carbon iodine number 1000m/g, moisture content 1%, specific surface area 1000m2/ g, hole
200 holes of density/m2, true specific gravity 2g/cm3, bulk density 0.4g/cm3), obtained process results such as the following table 6:
6 process result of table
After spraying pretreatment+ultraviolet catalytic+absorption process, each pollutant concentration is all satisfied discharge standard
It is required that pollutants removal rate reaches 96.66%.The process operation is easy to maintain, and high degree of automation is stable, apparatus body
Product is moderate, can meet into sled movement.
Embodiment seven: a certain tail gas for being 0.6% or so containing pollutant concentration of processing, gas flow 2500Nm3/h；With
The diluted lye containing 5%NaOH does preposition spray process, and spray room temperature is 30 DEG C, absolute pressure 200Kpa, and the tail gas after spray is logical
Enter ultraviolet lamp catalytic oxidizing equipment (20 UV light tubes of filling, 150W/ branch), absorption dress is entered after ultraviolet catalytic acts on
It sets, adsorbent equipment temperature is 30 DEG C, adsorptive pressure 110KPa, loads high performance active carbon (active carbon filtration velocity 0.2m/s, gas
Body is in active carbon effective stay time 1s, active carbon iodine number 1200m/g, moisture content 1%, specific surface area 1200m2/ g, hole density
220 holes/m2, true specific gravity 2g/cm3, bulk density 0.4g/cm3), obtained process results such as the following table 7:
7 process result of table
After spraying pretreatment+ultraviolet catalytic+absorption process, each pollutant concentration is all satisfied discharge standard
It is required that pollutants removal rate reaches 96.89%.
As an example, in the present invention, spray pretreatment is only to the bulky grains pollutant such as sulfide, ammonia, grease particle point
Son is effective, relatively difficult to mercaptan or other VOCs removal, and treatment effeciency is generally less than 50% when independent role；Ultraviolet lamp is urged
Change is only effective to the pollution molecule such as alcohols, benzene class, formaldehyde, resin, hydrogen sulfide, ammonia, is chiefly used in low concentration gas processing, individually
Treatment effeciency is generally less than 60% when use；Adsorption technology has a suction-operated to most of molecule, when exclusive use at early period
Reason efficiency can achieve 90%-95%, but adsorption stuffing is easily saturated, and be chiefly used in low concentration gas processing, and with adsorption stuffing
Saturation regeneration, adsorption efficiency gradually fails.Three of the above technology is neither able to satisfy qualified discharge requirement when being used alone.Combination
After, Each performs its own functions for each segment process section, is applicable to the VOCs exhaust gas of all kinds of high-concentration and low-concentrations and occasion, breaches single treatment skill
The limitation of art, pretreatment and ultraviolet lamp catalysis oxidation, reduce the adsorptive pressure of activated carbon adsorption device before adsorbent equipment,
Reduce the operating cost of single adsorption device, overall removal rate is up to 95% or more.
In conclusion taking spray pretreatment+ultraviolet catalytic+adsorption technology treatment process the present invention can provide a kind of
Combination, VOCs removal efficiency is suitable for all kinds of height up to 95% or more after spray, ultraviolet catalytic oxidation and adsorption treatment
The VOCs exhaust gas of low concentration and occasion has the advantages that the low skid of simple applied widely, Operation and Maintenance, safety, operating cost
The device and method of modular processing VOCs exhaust gas.
Above embodiments describe the invention in detail, but content is only the preferred embodiment of the present invention, no
It can be believed to be used to limit the scope of the invention.Any changes and modifications in accordance with the scope of the present application,
It should still fall within the scope of the patent of the present invention.
Claims (10)
1. a kind of device of skid module formula processing VOCs exhaust gas, it is characterised in that: the skid module formula handles VOCs exhaust gas
Device include pretreatment spray equipment (4), ultraviolet lamp catalytic unit (7), adsorbent equipment, condenser (11) and cyclic water tank
(16), the exhaust gas passes sequentially through pretreatment spray equipment (4), ultraviolet lamp catalytic unit (7) and adsorbent equipment, the pretreatment
Many-sided ball filler (5) are filled with inside spray equipment (4), the medicament in the cyclic water tank (16) passes through pretreatment circulating pump spray
It is sprinkled upon many-sided ball filler (5) surface, is regenerated after absorption filling adsorption saturation by high-temperature steam in the adsorbent equipment, institute
The high temperature exhaust steam for stating regenerative process generation is condensed by the condenser.
2. the device of skid module formula processing VOCs exhaust gas according to claim 1, it is characterised in that: the exhaust gas passes through
Blower (2) is delivered to pretreatment spray equipment (4), and pretreatment spray equipment (4) the upper outlet position is provided with demister
(6), the inlet and outlet of the blower (2) is connect by the A that is flexible coupling (1) and the B that is flexible coupling (3) with pipeline respectively.
3. the device of skid module formula processing VOCs exhaust gas according to claim 2, it is characterised in that: the adsorbent equipment
Quantity be two, be denoted as adsorbent equipment A (8) and adsorbent equipment B (9), in the adsorbent equipment filled with active carbon particle with
Molecular sieve, the high temperature exhaust steam that regenerative process generates are sent directly into sewage draining exit, the condenser row after condenser condensation
Not solidifying component out returns to the pretreatment spray equipment (4) and continues with, and the condenser (11) is followed with freezing unit (10)
Ring water is as refrigerant.
4. the device of skid module formula processing VOCs exhaust gas according to claim 3, it is characterised in that: the pretreatment spray
Shower device (4) bottom is communicated with cyclic water tank (16), and the pH value of the interior liquid of the cyclic water tank (16) is added by force (forcing) pump (15)
Pressure squeezes into medicament from medicament storage tank (12) and keeps stablizing, and the cyclic water tank (16) is provided with filter (17), the recirculated water
Liquidometer B (19) and PH meter (18) is installed in case (16), is provided with blender (13) and liquid level in the medicament storage tank (12)
It counts A (14).
5. the device of skid module formula processing VOCs exhaust gas according to claim 4, it is characterised in that: the skid module
The device of formula processing VOCs exhaust gas is integrated on two skid pedestals, and the pedestal is the steel knot that square steel or I-steel make
Structure, two pedestals are denoted as pedestal A and pedestal B respectively, and the blower of pipeline connection is provided on the pedestal A (22)
(2), pre-process spray equipment (4), medicament storage tank (12), cyclic water tank (16), dosing pump (15), pretreatment circulating pump A (20),
Circulating pump B (21), ultraviolet lamp catalytic unit (7) are pre-processed, condenser (11), freezing unit are disposed on pedestal B (23)
(12), adsorbent equipment A (8), adsorbent equipment B (9).
6. the device of skid module formula processing VOCs exhaust gas according to claim 5, it is characterised in that: the pretreatment spray
Shower device (4) is divided into left and right two chambers, is denoted as left chamber and right chamber, and exhaust gas is delivered to left chamber or the right side by blower (2)
Chamber is delivered to two chambers simultaneously, and the adsorbent equipment is divided into the chamber of left, center, right three, is denoted as middle chamber, left chamber and the right side
Chamber, using adsorbent material filling and one-way flow between the chamber, through ultraviolet catalytic device (7), treated, and exhaust gas is defeated
It send to left chamber or right chamber or is delivered to two chambers simultaneously, be discharged after being adsorbed through adsorbent material from middle chamber.
7. a kind of method of skid module formula processing VOCs exhaust gas, it is characterised in that: the skid module formula handles VOCs exhaust gas
Method used the device of skid module formula described in any one of claims 1-6 processing VOCs exhaust gas, the skid module
The method that formula handles VOCs exhaust gas is further comprising the steps of:
Step 1: the exhaust gas containing VOCs is pumped by blower (2) to pretreatment spray equipment (4) lower entrances through collection system, and
It is come into full contact with the chemical washing liquid sprayed downwards, removes grease particle and part volatile organic matter, preprocessed spray dress
It sets and enters ultraviolet lamp catalytic unit (7) after the dehydration of demister (6) demisting at the top of (4)；
Step 2: the exhaust gas is aoxidized in a very short period of time, is divided by the photodissociation of ultraviolet light and the catalytic action of photocatalyst
Solve contaminant molecule；
Step 3: the adsorption stuffing absorption of the adsorbent equipment is by step 2 treated excessive ozone and incompletely processed
Small molecule contaminants；
Step 4: the adsorption stuffing after adsorption saturation uses high-temperature steam desorption and regeneration, and the exhaust steam generated in regenerative process leads to
Enter condenser (11) to be condensed, condensate liquid is sent directly into sewage draining exit and is handled, and not solidifying component can return to pretreatment unit (4)
It continues with.
8. the method for skid module formula processing VOCs exhaust gas according to claim 7, it is characterised in that: the pretreatment dress
Set (4) spray temperature be 15~40 DEG C, pressure be 101~500Kpa, adsorbent equipment temperature be 15~40 DEG C, pressure be 101~
150Kpa。
9. the method for skid module formula processing VOCs exhaust gas according to claim 7, it is characterised in that: the condenser
(11) to freeze unit (10) recirculated water as refrigerant, 145 DEG C of high-temperature steam is cooled to 38 DEG C.
10. the method for skid module formula processing VOCs exhaust gas according to claim 7, it is characterised in that: pass through the step
Adsorption stuffing after rapid four desorption is dry by hot-air, humidity tester is arranged in the discharge outlet of the adsorbent equipment, when wet
When degree reaches setting numerical value, drying process terminates.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110548389A (en) * | 2019-03-19 | 2019-12-10 | 邹源 | Skid-mounted VOCs malodorous gas treatment device |
| CN111068513A (en) * | 2019-12-27 | 2020-04-28 | 东华大学 | Method for treating coating waste gas by manganese-loaded expanded graphite adsorption coupling catalysis ozone oxidation |
| CN114733309A (en) * | 2022-04-14 | 2022-07-12 | 常州大学 | High-efficient purifier of VOCs organic waste gas |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463937A (en) * | 2013-07-25 | 2013-12-25 | 天津大学 | Resourcable volatile organic tail gas treating method and skid-mounted moving device |
| CN104689712A (en) * | 2015-02-12 | 2015-06-10 | 杨阳 | Tubular modularized waste gas purification treatment device |
| CN105219464A (en) * | 2015-10-23 | 2016-01-06 | 中国石油大学(华东) | Natural qi exhaustion liquid slagging-off acid gas removal skid-mounted device and technique |
| CN105498446A (en) * | 2016-01-08 | 2016-04-20 | 浙江大学 | Method for recycling organic matter through organic waste gas adsorption, steam desorption and fractional condensation |
| CN207913507U (en) * | 2017-11-30 | 2018-09-28 | 临川环境技术（天津）有限公司 | Box emission-control equipment |
| CN209317446U (en) * | 2018-11-21 | 2019-08-30 | 中海油能源发展股份有限公司安全环保分公司 | A kind of device of skid module formula processing VOCs exhaust gas |
-
2018
- 2018-11-21 CN CN201811391346.3A patent/CN109289512A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463937A (en) * | 2013-07-25 | 2013-12-25 | 天津大学 | Resourcable volatile organic tail gas treating method and skid-mounted moving device |
| CN104689712A (en) * | 2015-02-12 | 2015-06-10 | 杨阳 | Tubular modularized waste gas purification treatment device |
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