CN108187465A - A kind of rubber house exhaust processing unit - Google Patents
A kind of rubber house exhaust processing unit Download PDFInfo
- Publication number
- CN108187465A CN108187465A CN201810226410.6A CN201810226410A CN108187465A CN 108187465 A CN108187465 A CN 108187465A CN 201810226410 A CN201810226410 A CN 201810226410A CN 108187465 A CN108187465 A CN 108187465A
- Authority
- CN
- China
- Prior art keywords
- reservoir
- lye
- air inlet
- connect
- absorption tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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- 238000010521 absorption reaction Methods 0.000 claims abstract description 36
- 230000001590 oxidative effect Effects 0.000 claims abstract description 13
- 229920000049 Carbon (fiber) Polymers 0.000 claims abstract description 12
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000004917 carbon fiber Substances 0.000 claims abstract description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000007789 gas Substances 0.000 claims description 44
- 239000007788 liquid Substances 0.000 claims description 33
- 230000003647 oxidation Effects 0.000 claims description 23
- 238000007254 oxidation reaction Methods 0.000 claims description 23
- 239000006096 absorbing agent Substances 0.000 claims description 12
- 239000007921 spray Substances 0.000 claims description 12
- 239000002699 waste material Substances 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000012856 packing Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 230000001413 cellular effect Effects 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 238000001179 sorption measurement Methods 0.000 claims description 2
- 239000003595 mist Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 5
- 238000005507 spraying Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- FGRBYDKOBBBPOI-UHFFFAOYSA-N 10,10-dioxo-2-[4-(N-phenylanilino)phenyl]thioxanthen-9-one Chemical compound O=C1c2ccccc2S(=O)(=O)c2ccc(cc12)-c1ccc(cc1)N(c1ccccc1)c1ccccc1 FGRBYDKOBBBPOI-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 238000010057 rubber processing Methods 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical class S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 244000286663 Ficus elastica Species 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- -1 Sulphur compound Chemical class 0.000 description 1
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical class O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000001345 alkine derivatives Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- RCJVRSBWZCNNQT-UHFFFAOYSA-N dichloridooxygen Chemical compound ClOCl RCJVRSBWZCNNQT-UHFFFAOYSA-N 0.000 description 1
- HRKQOINLCJTGBK-UHFFFAOYSA-N dihydroxidosulfur Chemical class OSO HRKQOINLCJTGBK-UHFFFAOYSA-N 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 239000002341 toxic gas 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
-
- 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
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/023—Pockets filters, i.e. multiple bag filters mounted on a common frame
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
-
- 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
- B01D53/38—Removing components of undefined structure
- B01D53/44—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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
-
- 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
- B01D53/46—Removing components of defined structure
- B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
-
- 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
- B01D53/76—Gas phase processes, e.g. by using aerosols
-
- 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
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/104—Ozone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/108—Halogens or halogen compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/30—Alkali metal compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/604—Hydroxides
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Dispersion Chemistry (AREA)
- Treating Waste Gases (AREA)
Abstract
A kind of rubber house exhaust processing unit, mainly including sequentially connected gas collecting apparatus, lye absorption tower, Ozone Absorption device, oxidative absorption tower and absorbing carbon fiber receiving apparatus;Present apparatus uniform air distribution, energy saving, process flow reasonable design, exhaust-gas treatment effect are good.
Description
Technical field
The present invention relates to rubber exhaust-gas treatment field more particularly to a kind of rubber house exhaust processing units.
Background technology
Rubber can generate a large amount of exhaust gas in process of manufacture, these exhaust gas exhaust gas constituents mainly have:1) contain
Sulphur compound:Such as H2S, SO2, thio-alcohol, thioether class;2) dust-like:Such as carbon black;3) organic species:As alkane, alkene, alkynes,
Aromatic hydrocarbon.The primordial matter that wherein most foul gas generate is organic substance, these substances to human health damage compared with
Greatly, with the raising of human living standard and the enhancing of Public Environmental Awareness, rubber plant's exhaust-gas treatment problem is just causing increasingly
More concerns.For the influence for preventing and avoiding toxic gas to live to surrounding resident, therefore its odor problem should be also resolved.
There are following defects for the processing equipment of rubber exhaust gas at present:First, the workshop of rubber processing factory has substantially
Several production lines, therefore the dust of rubber processing factory needs to realize that emphasis concentrates dust to production line, and in entire workshop
Inside it is also required to dust;Second, the exhaust gas that this outer rubber workshop generates needs comprehensive absorption and processing, the suction of ordinary rubber exhaust gas
Receipts are sprayed using lye, and the waste liquid recycling after spray uses, but this design is also defective, is exactly that waste liquid cannot
Infinite Cyclic uses, if concentration of narmful substance is higher in gas, waste liquid is no longer appropriate for recycling;Third, treatment process
Relatively simple, effect is bad.
Invention content
The technical problem to be solved by the present invention is to overcome the deficiencies in the prior art, provide a kind of uniform air distribution, energy saving,
Process flow reasonable design, a kind of good rubber house exhaust processing unit of exhaust-gas treatment effect.
Following technical scheme is provided to realize the present invention:A kind of rubber house exhaust processing unit, it is main to include connecting successively
Gas collecting apparatus, lye absorption tower, Ozone Absorption device, oxidative absorption tower and the absorbing carbon fiber receiving apparatus connect;The gas collecting apparatus
Including several suspended hoods, several dedusters, the first blast pipe, the second blast pipe, the first wind turbine, the second wind turbine and manifold is entered the wind,
The suspended hood is arranged on the production line of main shop, and suspended hood is connected with the first blast pipe, and first blast pipe is equipped with
First wind turbine;The deduster is arranged on the corner of main shop, and deduster is connected with the second blast pipe, on second blast pipe
Equipped with the second wind turbine, first blast pipe and the second blast pipe are connected with air inlet manifold;The lye absorption tower includes tower
Body, includes air inlet section, flow equalization section, several absorber portions and demisting section in tower body successively from bottom to up, the air inlet section side wall with into
Wind manifold connections, the air inlet manifold are stretched into air inlet section, are connect with the gas distribution pipe of air inlet section center, the gas distribution pipe is
Truncated cone-shaped wide at the top and narrow at the bottom, the gas distribution pipe is interior to be equipped with several shaped form air distribution plates, and cover having holes are equipped at the top of gas distribution pipe;It is described
Cellular isocon is equipped in flow equalization section, cover having holes diameter is identical with shunting pipe diameter at the top of the gas distribution pipe;The absorption
Section includes packing layer, spray equipment and inlet tube, and described inlet tube one end is connect with spray equipment, and the other end connects with lye reservoir
It connects, the spray equipment includes multi-layer annular liquid distributor and the high-pressure spraying head being connected on liquid distributor;At the top of the demisting section
Equipped with demisting plate;Gas outlet is equipped at the top of the tower body, tower body bottom is equipped with liquid outlet, triple valve is equipped at the liquid outlet
Door, described three-way valve one end are connect with waste liquid reservoir, and the other end is connect with lye reservoir;The Ozone Absorption device is horizontal
Tank body, tank body is interior to be equipped with ozone generator;The housing structure of the oxidative absorption tower and lye absorption tower are completely the same, and oxidation is inhaled
The inlet tube for receiving tower is connect with oxidation solution reservoir, and three-way valve one end at liquid outlet is connect with waste liquid reservoir, the other end and oxygen
Change the connection of liquid reservoir;Carbon fiber adsorption filler is equipped in the absorbing carbon fiber receiving apparatus.
Preferably, PH value detector, lye reservoir and oxidation solution are equipped in the lye reservoir and oxidation solution reservoir
Grug feeding jar and water inlet are equipped at the top of reservoir, agitating device is additionally provided in lye reservoir and oxidation solution reservoir.
Preferably, at least 2 sections of the absorber portion on the lye absorption tower, inlet tube is connect respectively with lye reservoir, into
Elevator pump is additionally provided between liquid pipe and lye reservoir.
Preferably, at least 2 sections of the absorber portion of the oxidative absorption tower, inlet tube is connect respectively with oxidation solution reservoir,
Elevator pump is equipped between inlet tube and oxidation solution reservoir.
Preferably, first wind turbine is frequency controlling fan;The deduster is bag filter.
Preferably, the gas distribution pipe with air inlet manifold to be threadedly coupled, enter the wind manifold in the tilted setting of air inlet section, into
Gas section side wall is additionally provided with access hole.
Usefulness of the present invention:First, using branch gas collection, recycle lye absorption, ozone oxidation and oxychloride, carbon
Fiber absorbs, and entire process flow is scientific and reasonable, and effect is good;Second, the first wind turbine of suspended hood connection is frequency controlling fan,
Can air quantity be adjusted according to the part or all of operating condition of production line in workshop, reach energy-efficient purpose;Third adds threeway
Valve discharges the waste liquid for being not suitable for recycling;4th, lye reservoir and oxidation solution reservoir are equipped with dosing and stirring dress
It puts, convenient for allocating spray liquid, while the pH value of PH value detector detection solution;4th, the setting of gas distribution pipe and flow equalization section causes
Evenly, spraying effect is more preferable for gas distribution;5th, air inlet pipe is obliquely installed, and be can effectively prevent waste liquid and is flowed back along air inlet pipe,
Air inlet section side wall is equipped with access hole, easy access simultaneously.
Description of the drawings
Fig. 1 is schematic structural view of the invention
Fig. 2 is gas distribution pipe top view.
Fig. 3 is isocon top view
In figure:1 be gas collecting apparatus, 1.1 be suspended hood, 1.2 be deduster, 1.3 be the first blast pipe, 1.4 be the second blast pipe,
1.5 it is the first wind turbine, 1.6 be the second wind turbine, 1.7 be air inlet manifold, 2 be lye absorption tower, 2.1 be air inlet section, 2.1.1 is cloth
Tracheae, 2.1.2 be air distribution plate, 2.1.3 be cover having holes, 2.2 be flow equalization section, 2.2.1 be isocon, 2.3 be absorber portion,
2.3.1 be packing layer, 2.3.2 be liquid distributor, 2.3.3 it is that high-pressure spraying head, 2.3.4 are inlet tubes, 2.4 are demisting section, 2.4.1
It is demisting plate, 3 be Ozone Absorption device, 4 be oxidative absorption tower, 5 be absorbing carbon fiber receiving apparatus, 6 be lye reservoir, 7 is outlet
Mouthful, 8 be liquid outlet, 9 be three-way valve, 10 be waste liquid reservoir, 11 be oxidation solution reservoir, 12 be PH value detector, 13 be dosing
Tank, 14 be water inlet, 15 be agitating device, 16 be elevator pump, 17 be access hole.
Specific embodiment
A kind of rubber house exhaust processing unit, mainly including sequentially connected gas collecting apparatus 1, lye absorption tower 2, ozone
Absorption plant 3, oxidative absorption tower 4 and absorbing carbon fiber receiving apparatus 5;The gas collecting apparatus 1 includes several suspended hoods 1.1, several removes
Dirt device 1.2, the first blast pipe 1.3, the second blast pipe 1.4, the first wind turbine 1.5, the second wind turbine 1.6 and air inlet manifold 1.7, it is described
Suspended hood 1.1 is arranged on the production line of main shop, and suspended hood 1.1 is connected with the first blast pipe 1.3, first blast pipe
1.3 are equipped with the first wind turbine 1.5;The deduster 1.2 is arranged on the corner of main shop, 1.2 and second blast pipe 1.4 of deduster
Be connected, second blast pipe 1.4 be equipped with the second wind turbine 1.6,1.3 and second blast pipe 1.4 of the first blast pipe with
Manifold 1.7 is entered the wind to be connected;The lye absorption tower 2 includes tower body, includes air inlet section 2.1 in tower body successively from bottom to up, flows
Section 2.2, several absorber portions 2.3 and demisting section 2.4,2.1 side wall of air inlet section are connect with air inlet manifold 1.7, and the air inlet is total
Pipe 1.7 is stretched into air inlet section 2.1, is connect with the gas distribution pipe 2.1.1 of 2.1 center of air inlet section, and the gas distribution pipe 2.1.1 is upper
Narrow truncated cone-shaped under width, the gas distribution pipe 2.1.1 is interior to be equipped with several shaped form air distribution plate 2.1.2, is equipped at the top of gas distribution pipe 2.1.1
Cover having holes 2.1.3;Cellular isocon 2.2.1, the gas distribution pipe 2.1.1 top tape port lids are equipped in the flow equalization section 2.2
Plate 2.1.3 diameters are identical with isocon 2.2.1 diameters;The absorber portion 2.3 includes packing layer 2.3.1, spray equipment and feed liquor
Pipe 2.3.4, described inlet tube 2.3.4 one end are connect with spray equipment, and the other end is connect with lye reservoir 6, the spray equipment
Including multi-layer annular liquid distributor 2.3.2 and the high-pressure spraying head 2.3.3 being connected on liquid distributor 2.3.2;The demisting section 2.4 is pushed up
Portion is equipped with demisting plate 2.4.1;Gas outlet 7 is equipped at the top of the tower body, tower body bottom is equipped with liquid outlet 8, is set at the liquid outlet 8
There is three-way valve 9, described 9 one end of three-way valve is connect with waste liquid reservoir 10, and the other end is connect with lye reservoir 6;The ozone
Absorption plant 3 is horizontal tank body, and ozone generator is equipped in tank body;The housing structure of the oxidative absorption tower 4 is absorbed with lye
Tower 2 is completely the same, and the inlet tube 2.3.4 of oxidative absorption tower 4 is connect with oxidation solution reservoir 11, the three-way valve 9 one at liquid outlet 8
End is connect with waste liquid reservoir 10, and the other end is connect with oxidation solution reservoir 11;Absorbing carbon fiber is equipped in the absorbing carbon fiber receiving apparatus 5
Attached filler is equipped with PH value detector 12, lye reservoir 6 and oxidation solution reservoir in the lye reservoir 6 and oxidation solution reservoir 11
11 tops are equipped with grug feeding jar 13 and water inlet 14, and agitating device 15 is additionally provided in lye reservoir 6 and oxidation solution reservoir 11, described
At least 2 sections of the absorber portion 2.3 on lye absorption tower 2, inlet tube 2.3.4 is connect respectively with lye reservoir 6, inlet tube 2.3.4 with
Elevator pump 16, at least 2 sections of the absorber portion 2.3 of the oxidative absorption tower 11, inlet tube 2.3.4 are additionally provided between lye reservoir 6
It is connect respectively with oxidation solution reservoir 11, elevator pump 16, first wind turbine is equipped between inlet tube 2.3.4 and oxidation solution reservoir 11
1.5 be frequency controlling fan;The deduster 1.2 is bag filter, and the gas distribution pipe 2.1.1 and air inlet manifold 1.7 is spiral shell
Line connects, and for air inlet manifold 1.7 in 2.1 tilted setting of air inlet section, 2.1 side wall of air inlet section is additionally provided with access hole 17.
A kind of rubber house exhaust processing unit involved by the invention is not limited in above-mentioned specific embodiment is familiar with
Those skilled in the art can also make a variety of variations accordingly, but any be equal or similar variation should all be covered with of the invention
Within the scope of the claims.
Claims (6)
1. a kind of rubber house exhaust processing unit, it is characterised in that:Mainly include sequentially connected gas collecting apparatus, lye absorbs
Tower, Ozone Absorption device, oxidative absorption tower and absorbing carbon fiber receiving apparatus;The gas collecting apparatus includes several suspended hoods, several removes
Dirt device, the first blast pipe, the second blast pipe, the first wind turbine, the second wind turbine and air inlet manifold, the suspended hood are arranged on main shop
Production line on, suspended hood is connected with the first blast pipe, first blast pipe be equipped with the first wind turbine;The deduster setting
In the corner of main shop, deduster is connected with the second blast pipe, second blast pipe be equipped with the second wind turbine, described first into
Air hose and the second blast pipe are connected with air inlet manifold;
The lye absorption tower includes tower body, includes air inlet section, flow equalization section, several absorber portions in tower body successively from bottom to up and removes
Mist section, the air inlet section side wall are connect with air inlet manifold, and the air inlet manifold is stretched into air inlet section, with air inlet section center
Gas distribution pipe connects, and the gas distribution pipe is truncated cone-shaped wide at the top and narrow at the bottom, and several shaped form air distribution plates, gas distribution are equipped in the gas distribution pipe
Tube top portion is equipped with cover having holes;Be equipped with cellular isocon in the flow equalization section, at the top of the gas distribution pipe cover having holes diameter with
It is identical to shunt pipe diameter;The absorber portion includes packing layer, spray equipment and inlet tube, described inlet tube one end and spray equipment
Connection, the other end are connect with lye reservoir, and the spray equipment includes multi-layer annular liquid distributor and the height being connected on liquid distributor
Press spray head;Demisting plate is equipped at the top of the demisting section;Gas outlet is equipped at the top of the tower body, tower body bottom is equipped with liquid outlet,
Three-way valve is equipped at the liquid outlet, described three-way valve one end is connect with waste liquid reservoir, and the other end is connect with lye reservoir;
The Ozone Absorption device is horizontal tank body, and ozone generator is equipped in tank body;
The housing structure of the oxidative absorption tower and lye absorption tower are completely the same, and inlet tube and the oxidation solution of oxidative absorption tower store up
Pond connects, and three-way valve one end at liquid outlet is connect with waste liquid reservoir, and the other end is connect with oxidation solution reservoir;
Carbon fiber adsorption filler is equipped in the absorbing carbon fiber receiving apparatus.
2. a kind of rubber house exhaust processing unit according to claim 1, it is characterised in that:The lye reservoir and oxygen
Change and PH value detector is equipped in liquid reservoir, grug feeding jar and water inlet, lye are equipped at the top of lye reservoir and oxidation solution reservoir
Agitating device is additionally provided in reservoir and oxidation solution reservoir.
3. a kind of rubber house exhaust processing unit according to claim 1, it is characterised in that:The lye absorption tower
At least 2 sections of absorber portion, inlet tube is connect respectively with lye reservoir, and elevator pump is additionally provided between inlet tube and lye reservoir.
4. a kind of rubber house exhaust processing unit according to claim 1, it is characterised in that:The oxidative absorption tower
At least 2 sections of absorber portion, inlet tube is connect respectively with oxidation solution reservoir, and elevator pump is equipped between inlet tube and oxidation solution reservoir.
5. a kind of rubber house exhaust processing unit according to claim 1, it is characterised in that:First wind turbine is becomes
Frequency adjustable speed fan;The deduster is bag filter.
6. a kind of rubber house exhaust processing unit according to claim 1, it is characterised in that:The gas distribution pipe and air inlet
Manifold is is threadedly coupled, and for air inlet manifold in the tilted setting of air inlet section, air inlet section side wall is additionally provided with access hole.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201810226410.6A CN108187465A (en) | 2018-03-19 | 2018-03-19 | A kind of rubber house exhaust processing unit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201810226410.6A CN108187465A (en) | 2018-03-19 | 2018-03-19 | A kind of rubber house exhaust processing unit |
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CN108187465A true CN108187465A (en) | 2018-06-22 |
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CN201810226410.6A Pending CN108187465A (en) | 2018-03-19 | 2018-03-19 | A kind of rubber house exhaust processing unit |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109078470A (en) * | 2018-08-07 | 2018-12-25 | 吴芊葭 | A kind of purifying sulphur-containing waste wet desulphurization device |
CN109499287A (en) * | 2018-11-23 | 2019-03-22 | 北京润泰环保科技有限公司 | A kind of wet scrubber tower and medical wastes incineration acid gas processing method |
CN114247243A (en) * | 2021-12-16 | 2022-03-29 | 东台宣龙防腐管道设备有限公司 | PM2.5 trap with four drawers |
CN117046288A (en) * | 2023-10-11 | 2023-11-14 | 中太(苏州)氢能源科技有限公司 | Absorption reaction device for ship tail gas treatment |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH0975659A (en) * | 1995-09-08 | 1997-03-25 | Babcock Hitachi Kk | Wet exhaust gas desulfurizer |
CN105169904A (en) * | 2015-07-27 | 2015-12-23 | 浙江省环境工程有限公司 | Purification system for rubber exhaust gas in sealing strip production field |
CN105749637A (en) * | 2016-04-07 | 2016-07-13 | 常州大学 | Comprehensive treatment system of waste gas in production of rubber tires |
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CN109078470A (en) * | 2018-08-07 | 2018-12-25 | 吴芊葭 | A kind of purifying sulphur-containing waste wet desulphurization device |
CN109499287A (en) * | 2018-11-23 | 2019-03-22 | 北京润泰环保科技有限公司 | A kind of wet scrubber tower and medical wastes incineration acid gas processing method |
CN114247243A (en) * | 2021-12-16 | 2022-03-29 | 东台宣龙防腐管道设备有限公司 | PM2.5 trap with four drawers |
CN117046288A (en) * | 2023-10-11 | 2023-11-14 | 中太(苏州)氢能源科技有限公司 | Absorption reaction device for ship tail gas treatment |
CN117046288B (en) * | 2023-10-11 | 2024-01-02 | 中太(苏州)氢能源科技有限公司 | Absorption reaction device for ship tail gas treatment |
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