CN104722150B - Pharmacy and chemical industry catalytic converter - Google Patents
Pharmacy and chemical industry catalytic converter Download PDFInfo
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- CN104722150B CN104722150B CN201510130273.2A CN201510130273A CN104722150B CN 104722150 B CN104722150 B CN 104722150B CN 201510130273 A CN201510130273 A CN 201510130273A CN 104722150 B CN104722150 B CN 104722150B
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- 239000000126 substance Substances 0.000 title claims abstract description 20
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 145
- 238000010521 absorption reaction Methods 0.000 claims abstract description 77
- 238000001914 filtration Methods 0.000 claims abstract description 74
- 238000001179 sorption measurement Methods 0.000 claims abstract description 71
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000008187 granular material Substances 0.000 claims abstract description 23
- 239000000428 dust Substances 0.000 claims abstract description 19
- 239000012530 fluid Substances 0.000 claims description 18
- 239000011229 interlayer Substances 0.000 claims description 17
- 239000010410 layer Substances 0.000 claims description 10
- 238000005406 washing Methods 0.000 abstract description 6
- 239000002912 waste gas Substances 0.000 description 20
- 239000007789 gas Substances 0.000 description 18
- 101100493712 Caenorhabditis elegans bath-42 gene Proteins 0.000 description 13
- 101100493711 Caenorhabditis elegans bath-41 gene Proteins 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 239000010865 sewage Substances 0.000 description 7
- 238000004140 cleaning Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000011941 photocatalyst Substances 0.000 description 3
- 238000005452 bending Methods 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 206010010904 Convulsion Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000036461 convulsion Effects 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
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000004531 microgranule Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 210000000664 rectum Anatomy 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Separation Of Particles Using Liquids (AREA)
- Filtering Materials (AREA)
Abstract
The invention discloses a kind of pharmacy and chemical industry catalytic converter, including band air inlet pipe and the casing of escape pipe, the reservoir being located at box bottom and the water pump connected with reservoir, coarse strainer and the adsorption net of adsorbable harmful gas molecule that may filter that granule and dust it is provided with in casing, water pump includes coarse filtration liquid pump and absorption liquid pump, the water side of coarse filtration liquid pump with absorption liquid pump water side connect with coarse strainer and adsorption net respectively, coarse strainer be respectively equipped with in adsorption net the coarse filtration liquid back pipe connected with reservoir and adsorb liquid back pipe.The pharmacy of the present invention and chemical industry catalytic converter dust capable of washing and granule also effectively reduce harmful gas molecule content, and job stability is strong, reliability is high.
Description
Technical field
The present invention relates to industrial waste gas treatment device, a kind of dust capable of washing and granule also effectively reduce harmful gas
The pharmacy of body molecule content and chemical industry catalytic converter.
Background technology
Along with stepping up of China's industrialization degree, the waste materials that factory discharges in daily production is increasing, thus
It is the most increasingly severe to the pollution of surrounding.In the emission of factory, waste gas is one of main polluter, especially
Such as the enterprises such as cement plant, Foundry Works, pharmaceutical factory, chemical plant or feed factory, its discharge waste gas in containing substantial amounts of granule,
Dust or heavy metal chip etc..For reducing the plant gas impact on environment, existing industrial premises the most all can arrange air
Purifier, its objective is to reduce the content of harmful substance in air, makes in Factory Building that the air of discharge will not be to surrounding
Producing and pollute, current industrial air purifier mainly divides fountain and adsorption-type two kinds.
Wherein, Chinese patent ZL 201420527312.3 discloses the air cleaner of a kind of Multi-layer sprinkling, this device profit
Constitute snakelike air channel with staggered division board, and spray head is set on division board, make air be subject to when by air channel
The repeatedly washing of spray head, it is achieved reduce granule, the effect of dust content in air.But, this device is only with spray
Mode makes the granule in air, dust weight increase and precipitate, it is impossible to thoroughly clean gas.Further, this device exists
The impulsive force produced during spray can slow down the flowing velocity of air in air channel, makes the air in air channel become weight with steam,
It is unfavorable for the discharge of air.
It addition, Chinese patent ZL 201320094064.3 discloses a kind of sky utilizing photocatalyst net and active carbon net to combine
Gas purifier, by adsorption and the Degradation of photocatalyst of activated carbon, reduces the content of harmful gas molecule in air.
But, there are two bigger defects in this depurator.One, owing to granule can blocking activities compared with waste gas big, that chip is more
Charcoal net and the mesh of photocatalyst net, such as occasions such as cement plant, Foundry Works or feed factories, user needs frequently to enter filter screen
Row cleaning, its use is inconvenient for；Its two, in this depurator, there are electric elements, when the humidity of waste gas is excessive time, meeting
Short circuit damages to make electric elements occur, has a strong impact on its service life.Therefore, the application industrially of this depurator has
Significant limitation.
Summary of the invention
It is an object of the invention to overcome the deficiencies in the prior art, it is provided that a kind of dust capable of washing and granule effectively minimizing have
The pharmacy of evil gas molecule content and chemical industry catalytic converter, it includes band air inlet pipe and the casing of escape pipe, is located at
The reservoir of box bottom and the water pump connected with reservoir, be provided with in casing and may filter that the coarse strainer of granule and dust and can inhale
With the adsorption net of evil gas molecule, water pump includes coarse filtration liquid pump and absorption liquid pump, the water side of coarse filtration liquid pump and absorption liquid pump
Water side connect with coarse strainer and adsorption net respectively, coarse strainer returns with being respectively equipped with the coarse filtration connected with reservoir in adsorption net
Liquid pipe and absorption liquid back pipe.The pharmacy of the present invention and chemical industry catalytic converter dust capable of washing and granule also effectively subtract
Rare harmful gas molecule content, and job stability is strong, reliability is high.
The goal of the invention of the present invention is achieved in that a kind of pharmacy and chemical industry catalytic converter, including band air inlet pipe
With the casing of escape pipe, the reservoir being located at box bottom and the water pump connected with reservoir, its construction features is: described case
Internal being provided with coarse strainer and the adsorption net of adsorbable harmful gas molecule that may filter that granule and dust, water pump includes coarse filtration liquid pump
With absorption liquid pump, the water side of coarse filtration liquid pump connects with coarse strainer and adsorption net respectively with the water side of absorption liquid pump, coarse strainer
Be respectively equipped with in adsorption net the coarse filtration liquid back pipe connected with reservoir and absorption liquid back pipe.
Further, reservoir is provided with and reservoir is divided into coarse filtration liquid bath and the interlayer of absorption liquid bath, coarse filtration liquid bath and absorption
Liquid bath connects with coarse filtration liquid back pipe and absorption liquid back pipe respectively, and absorption liquid bath constitutes airtight by the obstruct of interlayer relative to casing
Cavity.
Being optimized according to said structure, the bottom of coarse filtration liquid bath and absorption liquid bath is respectively equipped with coarse filtration liquid sewage draining exit and adsorption liquid
Sewage draining exit.
It is optimized according to said structure, in coarse filtration liquid bath, is provided with drainage screen with coarse filtration liquid pump connectivity part.
It is optimized according to said structure, interlayer is provided with sealing member with absorption liquid back pipe connectivity part.
It is optimized according to said structure, in absorption liquid bath, is loaded with expandable cleanout fluid.
Further, adsorption net and coarse strainer are arranged from top to bottom, and adsorption net pumps out end that water end (W.E.) connects and thick with adsorption liquid
The end that filter screen connects with coarse filtration liquid pump is equipped with intake chute, and adsorption net is provided with collecting tank with absorption liquid back pipe connectivity part.
It is optimized according to said structure, intake chute has equally distributed liquid outlet.
Being optimized according to said structure, adsorption net is taper dictyosome.
Being optimized according to said structure, coarse strainer is inverted cone shape dictyosome.
Further, air inlet pipe is the most down inclined at the bottom of casing, the side that air inlet pipe is relative with coarse strainer
Being provided with venthole, opposite side is provided with outage.
Further, escape pipe is located at casing top, and escape pipe inwall and casing connectivity part are provided with moisture absorption layer.
Further, it is provided with extractor fan in escape pipe.
Further, casing is up-small and down-big taper.
Preferably, adsorption net uses two-layer or above fine-meshed screen to be formed by stacking.
Further, described interlayer is bending structure, and its sidewall contact with casing, another side connects with the bottom of casing
Touching, absorption liquid bath constitutes airtight cavity by the obstruct of interlayer relative to casing.
The industrial waste gas purification device of prior art is improved by the present invention, and its advantage is as follows:
1, the pharmacy of the present invention and chemical industry are with in catalytic converter structure, arrange in casing utilize coarse filtration liquid pump, coarse strainer,
Coarse filtration liquid back pipe and absorption liquid pump, adsorption net, the Two-way Cycle filtration system of absorption liquid back pipe composition.Followed by separate
Ring filters, and makes coarse strainer and adsorption net can carry out by harmful fine particle in granule, dust and waste gas bigger to particle diameter respectively
Individually filter, substantially increase the filter efficiency of coarse strainer and adsorption net.Due to the most only between coarse filtration and two processes of absorption
Vertical, when real work, coarse filtration and absorption can be carried out in strict accordance with order, thus coarse filtration and two kinds of filter types of absorption are in work
Shi Buhui produces interference phenomenon, greatly strengthens the washer cleaning performance to waste gas.
2, the pharmacy of the present invention and chemical industry are with in catalytic converter structure, and reservoir is provided with interlayer, and absorption liquid bath leads to
The obstruct crossing interlayer constitutes airtight cavity relative to casing.Owing to interlayer makes adsorption liquid groove form the confined space relative to casing,
The granule precipitate produced in casing endogenous cause of ill coarse filtration will not enter in absorption liquid bath.Extract to suction in absorption liquid bath at cleanout fluid
Attached online time, it is to avoid the mesh of granule that particle diameter is bigger, dust blocking adsorption net, improve the stability that adsorption net uses.
It addition, coarse filtration liquid bath and coarse filtration liquid pump connectivity part arrange drainage screen, owing to coarse strainer is for filtering dust and the granule of big particle diameter,
At coarse filtration liquid pump, drainage screen is set, when can effectively prevent air purge the dust of precipitation and granule along with coarse filtration pump extraction with
Cleanout fluid flow to the back side of coarse strainer, the mesh of blocking coarse strainer together.
3, the pharmacy of the present invention and chemical industry are with in catalytic converter structure, are loaded with expandable cleanout fluid in absorption liquid bath,
The surface tension of expandable cleanout fluid is relatively big, and it may adhere on the mesh of adsorption net.When waste gas is by mesh, cleanout fluid
Forming bubble under capillary effect, the harmful gas microgranule in waste gas is adsorbed by liquid film.When bubble inner pressure power mistake
Time big, bubble i.e. ruptures, and liquid film forming drop drops down onto in adsorption net, and again adheres on mesh.By film forming-broken bubble-
The cyclic process of film forming, makes the waste gas of coarse filtration dry linting dirt and granule fully be cleaned.
4, the pharmacy of the present invention and chemical industry are with in catalytic converter structure, and adsorption net pumps out the end that water end (W.E.) connects with adsorption liquid
The end that portion and coarse strainer connect with coarse filtration liquid pump is equipped with intake chute, and adsorption net is provided with collecting tank with absorption liquid back pipe connectivity part,
And adsorption net be taper dictyosome, coarse strainer be inverted cone shape dictyosome.By intake chute and the setting of collecting tank, make coarse strainer and suction
There is relief area, effective guarantee cleanout fluid being uniformly distributed on coarse strainer and adsorption net in attached online cleanout fluid, improves and clean
Stability with absorption.
5, the pharmacy of the present invention and chemical industry are with in catalytic converter structure, and escape pipe inwall and casing connectivity part are provided with moisture absorption
Layer.Moisture absorption layer can carry out moisture absorption process to the air cleaned, effectively prevent dampness band to the extractor fan of escape pipe,
Avoid damaging the electric elements of extractor fan.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of preferred embodiment；
Accompanying drawing 2 is the structural representation of another embodiment of the present invention；
Accompanying drawing 3 is the partial enlarged drawing of coarse strainer of the present invention and intake chute；
Accompanying drawing 4 is the structural representation of intake chute on coarse strainer of the present invention；
Accompanying drawing 5 is the structural representation of intake chute in adsorption net of the present invention；
Accompanying drawing 6 is the partial enlarged drawing of coarse filtration liquid bath filtering net of the present invention.
In figure, 1 be air inlet pipe, 11 be venthole, 12 be outage, 2 be escape pipe, 21 be moisture absorption layer, 22 for convulsion
Device, 3 be casing, 41 be coarse filtration liquid bath, 42 be absorption liquid bath, 43 be interlayer, 44 be coarse filtration liquid sewage draining exit, 45 be
Adsorption liquid sewage draining exit, 46 be drainage screen, 47 for sealing member, 51 for coarse filtration liquid pump, 52 for absorption liquid pump, 6 for coarse strainer,
61 be coarse filtration liquid back pipe, 7 be adsorption net, 71 be absorption liquid back pipe, 8 be intake chute, 81 be fluid apertures, 9 for collecting tank.
Detailed description of the invention
The invention will be further described below in conjunction with the accompanying drawings.
With reference to the accompanying drawings 1, shown in Fig. 2, Fig. 3, Fig. 4, Fig. 5 and Fig. 6, pharmacy and the chemical industry waste gas of the present invention are clean
Change device and mainly include air inlet pipe 1, escape pipe 2, casing 3, reservoir and water pump.Wherein air inlet pipe 1 and escape pipe 2 are located at
On casing 3, reservoir is located at bottom casing 3, and water pump then connects with reservoir.Coarse strainer 6 it is provided with in casing 3
And adsorption net 7, wherein coarse strainer 6 may filter that granule and dust, adsorption net 7 adsorbable harmful gas molecule.On coarse strainer 6
Being provided with the coarse filtration liquid back pipe 61 connected with reservoir, adsorption net 7 is provided with the absorption liquid back pipe 71 connected with reservoir.Water pump
Including coarse filtration liquid pump 51 and absorption liquid pump 52, the water side of coarse filtration liquid pump 51 connects with coarse strainer 6, going out of absorption liquid pump 52
Water end (W.E.) connects with adsorption net 7.In the present invention, adsorption net 7 and coarse strainer 6 are separately fixed in casing 3 from top to bottom, slightly
Filter screen 6 can use the inverted cone shape dictyosome of 100-300 mesh, and coarse filtration liquid pump 51 connects with the upper end of coarse strainer 6, and coarse filtration returns liquid
Pipe 61 is then connected to the lower end of coarse strainer 6, i.e. coarse filtration liquid pump 51 and connects in the medial wall of casing 3 with coarse strainer 6, coarse filtration
Liquid back pipe 61 is arranged on the middle part of casing 3.Adsorption net 7 can use the taper dictyosome of 400-800 mesh, absorption liquid pump 52 with
The upper end connection of adsorption net 7, adsorbs liquid back pipe 71 and is then connected to the lower end of adsorption net 7, i.e. absorption liquid pump 52 and absorption
Net 7 connects at the middle part of casing 3, and absorption liquid back pipe 71 is arranged on the medial wall of casing 3.The present invention with taper dictyosome and
Reversely being equipped with of inverted cone shape dictyosome, increases the gas-contact area of unit latus rectum in casing 3, improves waste gas and cleans
Efficiency.
The end that adsorption net 7 connects with coarse filtration liquid pump 51 with the end that connects, absorption liquid pump 52 water side and coarse strainer 6 is all provided with
There is intake chute 8, intake chute 8 has equally distributed liquid outlet 81, and adsorption net 7 sets with absorption liquid back pipe 71 connectivity part
There is collecting tank 9.Cleanout fluid flowing in coarse strainer 6, adsorption net 7 can be produced by intake chute 8, liquid outlet 81 and collecting tank 9
Raw cushioning effect, the beneficially cleanout fluid Uniform Flow in coarse strainer 6, adsorption net 7, and coarse strainer 6 and adsorption net can be improved
The efficiency of 7 pairs of air purge.So far, coarse filtration liquid bath 41, coarse filtration liquid pump 51, intake chute 8, coarse strainer 6, coarse filtration liquid back pipe
61 composition coarse filtration circulating systems, absorption liquid bath 42, absorption liquid pump 52, intake chute 8, adsorption net 7, collecting tank 9, absorption
Liquid back pipe 71 forms sorption cycle system.Coarse filtration circulating system and the mutual independent operation of sorption cycle system, clean at waste gas
Do not have interference phenomenon during device work, improve stability and the reliability of the work of waste gas washer.
It addition, reservoir is provided with interlayer 43,43 reservoirs of interlayer are divided into coarse filtration liquid bath 41 and absorption liquid bath 42.Coarse filtration
Liquid bath 41 connects with coarse filtration liquid back pipe 61, and absorption liquid bath 42 connects with absorption liquid back pipe 71.Described interlayer 43 is in bending knot
Structure, its sidewall contact with casing 3, another side contacts with the bottom of casing 3, and absorption liquid bath 42 is by interlayer 43
Obstruct constitute airtight cavity relative to casing 3.Absorption liquid bath 42 constitutes close by the obstruct of interlayer 43 relative to casing 3
Close cavity.The absorption liquid bath 42 forming airtight cavity can be prevented effectively from the bigger granule of the particle diameter after coarse strainer 6 cleans, powder
Dirt drops down onto in absorption liquid bath 42.The bottom of coarse filtration liquid bath 41 is provided with coarse filtration liquid sewage draining exit 44, and the bottom of absorption liquid bath 42 is provided with
Adsorption liquid sewage draining exit 45.The effect of above-mentioned sewage draining exit is easy for user can be respectively to slightly after waste gas washer uses for a long time
Filtrate receiver 41 and absorption liquid bath 42 individually clean, and change cleanout fluid.The particle diameter filtered due to coarse strainer 6 is bigger
Granule, dust can drop down onto in coarse filtration liquid bath 41, for avoiding granule and dust to be extracted to slightly along with the effect of coarse filtration liquid pump 51
The back side of filter screen 6, the mesh of blocking coarse strainer 6, in coarse filtration liquid bath 41, it is provided with a mistake with coarse filtration liquid pump 51 connectivity part
Filter screen 46.It is provided with sealing member 47 with absorption liquid back pipe 71 connectivity part on interlayer 43, ensures the sealing of absorption liquid bath 42
Energy.And the waste gas after coarse filtration can be carried out adsorption treatment to realize adsorption net 7, be loaded with in absorption liquid bath 42 expandable clearly
Washing liquid, utilizes the principle that liquid film adsorbs, and the film forming constantly produced during with waste gas by adsorption net 7-broken bubble-film forming circulation is to useless
Gas fully cleans.In the present invention, adsorption net 7 may utilize two-layer or above fine-meshed screen is formed by stacking, between fine-meshed screen
Gap can accelerate the rupture velocity of film-forming foam in adsorption net 7, improve the adsorption efficiency of adsorption net 7.
Additionally, air inlet pipe 1 is arranged on the bottom of casing 3, due to the coarse strainer 6 being arranged above carrying liqs and the suction of air inlet pipe 1
Attached net 7, for preventing the liquid of coarse strainer 6 and adsorption net 7 from accumulating in air inlet pipe 1, air inlet pipe 1 the most down tilts
Arranging, air inlet pipe 1 side relative with coarse strainer 6 is provided with venthole 11, and opposite side is provided with outage 12, outage 12
May be disposed at the end that air inlet pipe 1 is downward-sloping, and relative in the liquid level of reservoir.Venthole 11 is relative with coarse strainer 6,
The contact velocity of waste gas and coarse strainer 6 can be accelerated, it is to avoid air-flow produces the phenomenon of sinuous flow in casing 3.Escape pipe 2 is located at
Casing 3 top, escape pipe 2 inwall and casing 3 connectivity part are provided with extractor fan 22 in being provided with moisture absorption layer 21, and escape pipe 2.
Moisture absorption layer 21 can carry out moisture absorption process to the gas after cleaning, it is to avoid damages on the steam band in gas to extractor fan 22
Electric elements.The setting of extractor fan 22 is then to accelerate the flow velocity of gas in casing 3, is beneficial to the gas after cleaning and discharges
Casing 3.
Filtering the loss of the flow velocity after cleaning to reduce waste gas, casing 3 can use in up-small and down-big cone structure, carry
High waste gas is by the flow velocity after coarse strainer 6 and adsorption net 7, the most as shown in Figure 1.Certainly casing 3 can also use
Non-cone structure, the most as shown in Figure 2.
In the present invention, waste gas sequentially passes through coarse strainer 6 and adsorption net 7 from top to bottom, and adsorb cleanout fluid in liquid bath 42 with
The cleanout fluid of coarse filtration liquid bath 41 is mutually isolated.Even if the cleanout fluid in adsorption net 7 drops on coarse strainer 6 when normal use,
And be back in coarse filtration liquid bath 41, because the cleanout fluid of absorption liquid bath 42 has the function of film forming, coarse strainer 6 can be improved equally
Filter large-scale granule, the effect of dust.Therefore washer uses the time the longest, foamable cleanout fluid in coarse filtration liquid bath 41
Content is the highest, and the filter effect of coarse strainer 6 is the best.
Above-mentioned specific embodiment is only the preferable detailed description of the invention of effect of the present invention, all and pharmacy of the present invention and chemical industry
Structure that is identical with catalytic converter or that be equal to, the most within the scope of the present invention.
Claims (3)
1. pharmacy and a chemical industry catalytic converter, including band air inlet pipe (1) and escape pipe (2) casing (3),
The reservoir being located at the bottom of casing (3) and the water pump connected with reservoir, it is characterised in that: described casing sets in (3)
Having the adsorption net (7) of coarse strainer (6) and the adsorbable harmful gas molecule that may filter that granule and dust, water pump includes coarse filtration liquid
Pump (51) and absorption liquid pump (52), the water side of coarse filtration liquid pump (51) connects with coarse strainer (6), adsorbs liquid pump (52)
Water side connect with adsorption net (7), coarse strainer (6) is respectively equipped with, in adsorption net (7), the coarse filtration connected with reservoir
Liquid back pipe (61) and absorption liquid back pipe (71), described adsorption net (7) and coarse strainer (6) arrange from top to bottom, adsorption net
(7) end connected with absorption liquid pump (52) water side is provided with intake chute (8), at coarse strainer (6) and coarse filtration liquid pump
(51) end connected also is provided with intake chute (8), and adsorption net (7) is provided with collecting tank with absorption liquid back pipe (71) connectivity part
(9), described adsorption net (7) uses the taper dictyosome of 400-800 mesh, and absorption liquid pump (52) is upper with adsorption net (7)
End connection, absorption liquid pump (52) connects at the middle part of casing (3) with adsorption net (7), and absorption liquid back pipe (71) connects
In the lower end of adsorption net (7), absorption liquid back pipe (71) is arranged on the medial wall of casing 3；Described coarse strainer (6) is adopted
With the inverted cone shape dictyosome of 100-300 mesh, coarse filtration liquid pump (51) connects with the upper end of coarse strainer (6), coarse filtration liquid back pipe (61)
Being connected to the lower end of coarse strainer (6), coarse filtration liquid pump (51) connects, slightly in the medial wall of casing (3) with coarse strainer (6)
Filter liquid back pipe (61) is arranged on the middle part of casing (3)；Described air inlet pipe (1) is the most down inclined at casing
(3) bottom, air inlet pipe (1) side relative with coarse strainer (6) is provided with venthole (11), and opposite side is provided with discharge opeing
Hole (12), described reservoir is provided with interlayer (43), described interlayer (43) reservoir be divided into coarse filtration liquid bath (41) and
Absorption liquid bath (42), coarse filtration liquid bath (41) connects with coarse filtration liquid back pipe (61), absorption liquid bath (42) and absorption liquid back pipe
(71) connection, contains expandable cleanout fluid in absorption liquid bath (42).
Pharmacy the most according to claim 1 and chemical industry catalytic converter, it is characterised in that: described intake chute (8)
On have equally distributed liquid outlet (81).
Pharmacy the most according to claim 1 and 2 and chemical industry catalytic converter, it is characterised in that: described escape pipe (2)
Being located at casing (3) top, escape pipe (2) inwall and casing (3) connectivity part are provided with moisture absorption layer (21), described escape pipe
(2) extractor fan (22) it is provided with in.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510130273.2A CN104722150B (en) | 2015-03-24 | 2015-03-24 | Pharmacy and chemical industry catalytic converter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510130273.2A CN104722150B (en) | 2015-03-24 | 2015-03-24 | Pharmacy and chemical industry catalytic converter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104722150A CN104722150A (en) | 2015-06-24 |
| CN104722150B true CN104722150B (en) | 2016-08-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510130273.2A Active CN104722150B (en) | 2015-03-24 | 2015-03-24 | Pharmacy and chemical industry catalytic converter |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN109045869B (en) * | 2018-07-10 | 2020-11-27 | 陈楠 | Environmental protection is administered and is used dust removal shallow device |
| CN109092011B (en) * | 2018-08-27 | 2021-12-07 | 江苏煌灿新材料科技有限公司 | Industrial waste gas adsorbs processing apparatus |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN2328415Y (en) * | 1998-05-23 | 1999-07-14 | 孟昭岐 | Fume processing apparatus |
| CN2394702Y (en) * | 1999-11-05 | 2000-09-06 | 孟昭岐 | Fume purifying and treating device |
| KR20050008563A (en) * | 2004-12-08 | 2005-01-21 | 양준모 | Exit of Dust-Vampire |
| CN201431840Y (en) * | 2009-07-02 | 2010-03-31 | 福建省永泰建筑工程公司 | Smoke gas dust-removing device |
| CN201871310U (en) * | 2010-12-11 | 2011-06-22 | 居琴 | Washing type dust collector |
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