CN205340496U - Organic waste gas integrated treating equipment - Google Patents
Organic waste gas integrated treating equipment Download PDFInfo
- Publication number
- CN205340496U CN205340496U CN201620003001.6U CN201620003001U CN205340496U CN 205340496 U CN205340496 U CN 205340496U CN 201620003001 U CN201620003001 U CN 201620003001U CN 205340496 U CN205340496 U CN 205340496U
- Authority
- CN
- China
- Prior art keywords
- spray
- exhaust gas
- organic exhaust
- equipment according
- dry filter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007789 gas Substances 0.000 title abstract description 15
- 239000010815 organic waste Substances 0.000 title abstract description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 65
- 239000007921 spray Substances 0.000 claims abstract description 43
- 238000001179 sorption measurement Methods 0.000 claims abstract description 30
- 239000007788 liquid Substances 0.000 claims abstract description 21
- 238000000034 method Methods 0.000 claims abstract description 15
- 230000008569 process Effects 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 230000010354 integration Effects 0.000 claims description 15
- 239000000443 aerosol Substances 0.000 claims description 14
- 229920000742 Cotton Polymers 0.000 claims description 13
- 239000002250 absorbent Substances 0.000 claims description 10
- 230000002745 absorbent Effects 0.000 claims description 10
- 239000003610 charcoal Substances 0.000 claims description 10
- 239000003595 mist Substances 0.000 claims description 9
- 230000008676 import Effects 0.000 claims description 5
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 14
- 239000002912 waste gas Substances 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 9
- 230000008859 change Effects 0.000 abstract description 4
- 238000005507 spraying Methods 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 3
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 239000003814 drug Substances 0.000 abstract 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses an organic waste gas integrated treating equipment, including liquid medicine spraying system, aerial fog piece -rate system, dry -type filtration system and active carbon adsorption system, liquid medicine spraying system one side is equipped with the air inlet, and the opposite side communicates with each other with aerial fog piece -rate system, dry -type filtration system, active carbon adsorption system in proper order, the top of active carbon adsorption system is equipped with the gas outlet. Waste gas process liquid medicine sprays in this equipment, the aerial fog separates, the dry -type is filtered, a series of processing of active carbon adsorption, and purifying effect is good, and safe energy -conservation, and the adsorption effect of adsorption bed is good in here equipment, active carbon be liable to change, and active carbon long service life.
Description
Technical field
This utility model relates to exhaust-gas treatment field, and particularly a kind of organic exhaust gas integration processes equipment.
Background technology
In VOCs treatment industry, the improvement for waste gas is usually employing active carbon adsorption or Production by Catalytic Combustion Process to administer organic exhaust gas.When adopting active carbon adsorption to process waste gas, traditional process equipment active carbon layer easily blocks and activated carbon is changed cumbersome, equipment resistance is relatively larger, cause that time the later stage uses, its efficiency is very low: although and traditional Treatment of Organic Waste Gas Containing Cyclohexanone treatment effect is relatively good, but its electrical power required when processing is relatively big, and operating cost is higher.
Summary of the invention
For solving the problems referred to above of analysis system test strips Sorting Technique aspect, the purpose of this utility model is in that the organic exhaust gas integration providing a kind of energy-saving safe, exhaust-gas treatment effective processes equipment.
For achieving the above object, this utility model provides a kind of organic exhaust gas integration to process equipment, including medicinal liquid spray system, aerosol piece-rate system, dry filter system and activated carbon adsorption system, medicinal liquid spray system side is provided with air inlet, opposite side communicates with aerosol piece-rate system, dry filter system, activated carbon adsorption system successively, and the top of described activated carbon adsorption system is provided with air vent.
Further, described medicinal liquid spray system bottom is provided with water tank, and tank top is connected with spray district by spray liquid flow export, and spray top, district is provided with spray and imports and exports water pipe, is provided with spray pipe, spray pipe is provided with shower nozzle in jet band.
Further, described spray pipe is stainless steel helix tube.
Further, both sides, described spray district are provided with observation panel, have two, for observing the spraying effect in spray district.
Further, the top of described aerosol piece-rate system is provided with feeding mouth, and bottom is provided with discharge port, also includes mesh sheet and staggers the labyrinth type being welded except mist plate.
Further, described dry filter system includes dry filter device, and vertical in described dry filter device have baffle plate, baffle plate to be provided with filter cotton placement framework, is used for placing dry filter cotton.
Further, described filter cotton is placed framework and is adopted flanging setting.
Further, the quantity of described dry filter device is multiple, and described dry filter device takes drawer type to arrange.
Further, described activated carbon adsorption system includes absorbent charcoal adsorber, is placed with mesh sheet in described absorbent charcoal adsorber, and mesh sheet is placed with activated carbon.
Further, the quantity of described absorbent charcoal adsorber is multiple, and described absorbent charcoal adsorber takes drawer type to arrange.
This utility model has the advantages that in (1) this equipment, waste gas sprays through medicinal liquid, aerosol separates, dry filter, a series of process of activated carbon adsorption, good purification, and energy-saving safe, first pass through medicinal liquid spray, absorb most organic gas, if waste gas is directly entered activated carbon adsorption bed after process, adsorbent bed adsorbs waste gas and moisture simultaneously, hardening of activated carbon adsorption bed will be caused, therefore first pass through aerosol to separate, after being processed by medicinal liquid spray by blower fan, waste gas imports in aerosol piece-rate system except mist, rear entrance dry filter system, waste gas after filtration enters back into activated carbon adsorption system, the now advantages of good adsorption effect of waste gas, extend the service life of activated carbon adsorption bed simultaneously；(2) adopt vertically-arranged drawer type active carbon adsorbent bed, compared with traditional active carbon adsorption equipment, can better change activated carbon therein, be conducive to the permanent Effec-tive Function of equipment；(3) being provided with multilamellar vertically-arranged activated carbon adsorption bed in the activated carbon adsorption system that the design adopts, waste gas is with less flow velocity by after active-carbon bed, and organic pollution therein is adsorbed under the strong adsorptivity effect of activated carbon to be retained, thus being purified；(4), when aerosol separates, organic exhaust gas particulate matter and cotton-shaped sicker, under the flanging labyrinth type crown_interception except mist plate, play dedusting sedimentation crown_interception, then through dry filter device, it is ensured that subsequent technique activated carbon efficient absorption；(5) in order to prevent active carbon layer from blocking, this equipment adopts drawer type dry filter device, the inside is placed with dry filter cotton, filter cotton is placed framework and is adopted flanging to arrange, it is simple to the replacing of filter cotton, does not worry on the one hand that equipment resistance is excessive and causes that its treatment effeciency is on the low side, its filter area can be increased on the other hand, when this equipment runs simultaneously, power demand is only small, and can guarantee that waste gas energy qualified discharge, complies fully with the requirement of energy-conserving and environment-protective；(6) this device energy conservation effect is obvious, owing to fan pressure head only has traditional 60%, thus has saved the energy consumption of 40%.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be done simple introduction below, apparently, accompanying drawing in the following describes is embodiments more of the present utility model, for those of ordinary skill in the art, under the premise not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Accompanying drawing 1 is the front view of this utility model embodiment.
Accompanying drawing 2 is the top view of this utility model embodiment.
Accompanying drawing 3 is the right view of this utility model embodiment.
Accompanying drawing 4 is the A-A profile of this utility model embodiment.
Accompanying drawing 5 is the dry filter components of system as directed structure chart of this utility model embodiment.
Accompanying drawing 6 is the E-E profile of this utility model embodiment.
In accompanying drawing, 101 is medicinal liquid spray system, and 102 is aerosol piece-rate system, 103 is dry filter system, and 104 is activated carbon adsorption bed system, and 1 is air inlet, 2 is exhaust outlet, 3 is water tank, and 4 is running water inlet water pipe, and 5 is unit fixed on water pump suction water pipe, 6 is overfall, 7 is evacuation port, and 8 is plant bottom case support, and 9 is feeding mouth, 10 is discharge port, 11 is spray import water pipe, and 12 is that labyrinth type removes mist plate, and 13 is baffle plate, 14 is that filter cotton places framework, 15 is observation panel, and 16 is spray liquid flow export, and 17 is drawer sliding rail.
Detailed description of the invention
Below by specific embodiment, this utility model is further described.
Accompanying drawing 1 to accompanying drawing 6 discloses a kind of organic exhaust gas integration and processes equipment, including medicinal liquid spray system 101, aerosol piece-rate system 102, dry filter system 103, activated carbon adsorption bed system 104, air inlet 1 is airintake direction, and air inlet 1 is connected with medicinal liquid spray system, and the top of activated carbon adsorption bed system is provided with air vent 2.Having water tank 3 under medicinal liquid spray system, water tank 3 has running water inlet water pipe 4, unit fixed on water pump suction water pipe 5, overfall 6, evacuation port 7, overfall 6 receives water channel, and evacuation port 7 is ball valve, is set to silk mouth and connects.Being spray district above water tank, spray district is connected by spray liquid flow export 16 with water tank, and spray top, district is additionally provided with spray import water pipe 11.Spray district is set to cylindric.Spray both sides, district are additionally provided with observation panel 15, for observing the spray situation inside spray district, hold spraying effect better.After medicinal liquid spray, gas inlet mist piece-rate system, aerosol piece-rate system includes feeding mouth 9, discharge port 10, and the inside also includes labyrinth type except mist plate 12, and labyrinth type is that two mesh sheet stagger and are welded except mist plate, has dedusting, except fog effect.Aerosol piece-rate system is cylindrical setting, and discharge port is multiaspect sky ball discharge port.After mist, enter dry filter system.Drawer sliding rail 17 it is provided with in dry filter system, can arranging the dry filter device of 6 drawer types, vertical in dry filter device have baffle plate 13, baffle plate has filter cotton place framework 14, filter cotton is placed framework 14 and is arranged for flanging, so can facilitate the extracting replacing of filter cotton.After dry filter, enter activated carbon adsorption bed system, in activated carbon adsorption bed system, be provided with drawer sliding rail 17, the absorbent charcoal adsorber of 6 drawer types can be set, it is placed with mesh sheet in absorbent charcoal adsorber, mesh sheet has stainless (steel) wire, stainless (steel) wire can be placed column-shaped active carbon.
Principle of the present utility model and embodiment are set forth by specific embodiment used herein, and the explanation of above example is only intended to help to understand method of the present utility model and core concept thereof.The above is only preferred implementation of the present utility model, should be understood that, finiteness due to literal expression, and objectively there is unlimited concrete structure, for those skilled in the art, under the premise without departing from this utility model principle, it is also possible to make some improvement, retouching or change, it is also possible to above-mentioned technical characteristic is combined by rights；These improve retouching, change or combination, or the not improved design by utility model and technical scheme directly apply to other occasion, are regarded as protection domain of the present utility model.
Claims (10)
1. organic exhaust gas integration processes equipment, it is characterized in that, including medicinal liquid spray system, aerosol piece-rate system, dry filter system and activated carbon adsorption system, medicinal liquid spray system side is provided with air inlet, opposite side communicates with aerosol piece-rate system, dry filter system, activated carbon adsorption system successively, and the top of described activated carbon adsorption system is provided with air vent.
2. organic exhaust gas integration equipment according to claim 1, it is characterized in that, described medicinal liquid spray system bottom is provided with water tank, tank top is connected with spray district by spray liquid flow export, spray top, district is provided with spray and imports and exports water pipe, it is provided with spray pipe in jet band, spray pipe is provided with shower nozzle.
3. organic exhaust gas integration equipment according to claim 2, it is characterised in that described spray pipe is stainless steel helix tube.
4. organic exhaust gas integration equipment according to claim 2, it is characterised in that both sides, described spray district are provided with observation panel.
5. organic exhaust gas integration equipment according to claim 1, it is characterised in that the top of described aerosol piece-rate system is provided with feeding mouth, and bottom is provided with discharge port, also includes mesh sheet and staggers the labyrinth type being welded except mist plate.
6. organic exhaust gas integration equipment according to claim 1, it is characterised in that described dry filter system includes dry filter device, vertical in described dry filter device have baffle plate, baffle plate to be provided with filter cotton placement framework, is used for placing dry filter cotton.
7. organic exhaust gas integration equipment according to claim 6, it is characterised in that described filter cotton is placed framework and adopted flanging to arrange.
8. organic exhaust gas integration equipment according to claim 6, it is characterised in that the quantity of described dry filter device is multiple, and described dry filter device takes drawer type to arrange.
9. the organic exhaust gas integration equipment according to any one of claim 1, it is characterised in that described activated carbon adsorption system includes absorbent charcoal adsorber, is placed with mesh sheet in described absorbent charcoal adsorber, and mesh sheet is placed with activated carbon.
10. organic exhaust gas integration equipment according to claim 9, it is characterised in that the quantity of described absorbent charcoal adsorber is multiple, and described absorbent charcoal adsorber takes drawer type to arrange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620003001.6U CN205340496U (en) | 2016-01-05 | 2016-01-05 | Organic waste gas integrated treating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620003001.6U CN205340496U (en) | 2016-01-05 | 2016-01-05 | Organic waste gas integrated treating equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205340496U true CN205340496U (en) | 2016-06-29 |
Family
ID=56172887
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620003001.6U Expired - Fee Related CN205340496U (en) | 2016-01-05 | 2016-01-05 | Organic waste gas integrated treating equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205340496U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106492586A (en) * | 2016-10-24 | 2017-03-15 | 佛山科学技术学院 | Spray and the case integrated processing equipment of activated carbon |
| CN107854931A (en) * | 2017-12-12 | 2018-03-30 | 曹诗晴 | A kind of computer plastic fittings production emission-control equipment |
| CN111715026A (en) * | 2020-06-20 | 2020-09-29 | 安徽宝图实验室设备有限公司 | Filter box with time delay mechanism |
-
2016
- 2016-01-05 CN CN201620003001.6U patent/CN205340496U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106492586A (en) * | 2016-10-24 | 2017-03-15 | 佛山科学技术学院 | Spray and the case integrated processing equipment of activated carbon |
| CN107854931A (en) * | 2017-12-12 | 2018-03-30 | 曹诗晴 | A kind of computer plastic fittings production emission-control equipment |
| CN111715026A (en) * | 2020-06-20 | 2020-09-29 | 安徽宝图实验室设备有限公司 | Filter box with time delay mechanism |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160629 Termination date: 20180105 |