CN204051377U - Effective integrated soda acid and organic exhaust gas adsorption device - Google Patents
Effective integrated soda acid and organic exhaust gas adsorption device Download PDFInfo
- Publication number
- CN204051377U CN204051377U CN201420469670.3U CN201420469670U CN204051377U CN 204051377 U CN204051377 U CN 204051377U CN 201420469670 U CN201420469670 U CN 201420469670U CN 204051377 U CN204051377 U CN 204051377U
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- CN
- China
- Prior art keywords
- tower body
- absorption tower
- active carbon
- pall ring
- soda acid
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- Expired - Fee Related
Links
- 239000002253 acid Substances 0.000 title claims abstract description 28
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 title claims abstract description 22
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 11
- 238000010521 absorption reaction Methods 0.000 claims abstract description 71
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 43
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 229920000742 Cotton Polymers 0.000 claims abstract description 10
- 239000000945 filler Substances 0.000 claims abstract description 9
- 239000012530 fluid Substances 0.000 claims abstract description 9
- 238000003860 storage Methods 0.000 claims abstract description 9
- 239000007789 gas Substances 0.000 description 23
- 239000002912 waste gas Substances 0.000 description 16
- 239000007788 liquid Substances 0.000 description 7
- 239000003513 alkali Substances 0.000 description 6
- 238000000746 purification Methods 0.000 description 5
- 238000007599 discharging Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of effective integrated soda acid and organic exhaust gas adsorption device, comprise: absorption tower body and active carbon absorption plant, the side, lower end of described absorption tower body is provided with centrifugal blower, the upper end of described soda acid fluid storage tank is provided with water pump, described shower is provided with some nozzles, Pall ring filler layer is provided with in absorption tower body below described shower, rotational flow plate defroster is provided with in absorption tower body above described shower, the upper end of described absorption tower body is connected with active carbon absorption plant by delivery conduit, at described Pall ring except the upper end of water layer is provided with feeding port, at described Pall ring except the side, lower end of water layer is provided with discharge outlet, filter cotton is provided with except in the active carbon absorption plant below water layer at described Pall ring, activated carbon filter layer is provided with in active carbon absorption plant below described filter cotton, the side, lower end of described active carbon absorption plant is provided with exhaust outlet.
Description
Technical field
The utility model relates to a kind of gas cleaning plant, particularly relates to a kind of effective integrated soda acid and organic exhaust gas adsorption device.
Background technology
In the production process of chemical industry, metallurgy, papermaking, fuel, printed circuit board (PCB) and semicon industry, acid, alkali waste gas and the various organic exhaust gas such as H2S, SOX, NOX, HCl, HF, NH3, Cl2 can be produced.At present, this type of soda acid waste gas and organic waste-gas purification method adopt two covering devices to purify respectively usually, need two Fans to add work.Along with the development of national economy, the improving constantly of the progress of technology and people's quality of life, require strictly to control the discharge of this type of waste gas and using energy source.In actual applications, most purifier simplicity of design, gas-liquid skewness, absorption efficiency is low, absorbing liquid consumption large, exit gas fog is large, the discharge standard of increasingly stringent can not be met, two covering device two Fans separately work simultaneously, troublesome poeration, purification efficiency is low, cost is high, wastes energy, and can not respond the call that national energy-saving reduces discharging.
Utility model content
Technical problem to be solved in the utility model is: provide a kind of purification efficiency is high, cost is low effective integrated soda acid and organic exhaust gas adsorption device.
In order to solve the problems of the technologies described above, the technical solution adopted in the utility model is: soda acid and organic exhaust gas absorption tower, comprise: absorption tower body and active carbon absorption plant, the side, lower end of described absorption tower body is provided with centrifugal blower, one end of pipeline is connected with centrifugal blower, the inside, lower end that the other end of described pipeline stretches into absorption tower body is interconnected with it, one end that described pipeline is connected with absorption tower body is provided with oblique air inlet, the lower end opposite side of described absorption tower body is provided with soda acid fluid storage tank, the upper end of described soda acid fluid storage tank is provided with water pump, one end of tube connector is connected with water pump, the other end of described tube connector be arranged on the intrinsic shower in absorption tower and be connected, described shower is provided with some nozzles, Pall ring filler layer is provided with in absorption tower body below described shower, rotational flow plate defroster is provided with in absorption tower body above described shower, the upper end of described absorption tower body is connected with active carbon absorption plant by delivery conduit, the inner upper end of described active carbon absorption plant is provided with the Pall ring be connected with delivery conduit and removes water layer, at described Pall ring except the upper end of water layer is provided with feeding port, at described Pall ring except the side, lower end of water layer is provided with discharge outlet, filter cotton is provided with except in the active carbon absorption plant below water layer at described Pall ring, activated carbon filter layer is provided with in active carbon absorption plant below described filter cotton, the side, lower end of described active carbon absorption plant is provided with exhaust outlet.
The utility model has the advantages that: above-mentioned effective integrated soda acid and organic exhaust gas adsorption device, all Pall ring filler is filled with in absorption tower body and active carbon absorption plant, can moisture content effectively in divided gas flow, reduce the moisture content of gas, the harmful substance in gas is absorbed by active carbon, absorption efficiency is high, the absorption cycle is long, ensure that gas can reach discharge standard, adopt set of device to process acid, alkali waste gas and various organic exhaust gas simultaneously, purification efficiency is high, cost is low, economize energy, has responded the call that national energy-saving reduces discharging.
Accompanying drawing explanation
Fig. 1 is the structural representation of the effective integrated soda acid of the utility model and organic exhaust gas adsorption device.
In figure: 1, absorption tower body, 2, active carbon absorption plant, 3, centrifugal blower, 4, pipeline, 5, oblique air inlet, 6, soda acid fluid storage tank, 7, water pump, 8, tube connector, 9, shower, 10, nozzle, 11, Pall ring filler layer, 12, rotational flow plate defroster, 13, delivery conduit, 14, Pall ring is except water layer, and 15, feeding port, 16, discharge outlet, 17, filter cotton, 18, activated carbon filter layer, 19, exhaust outlet.
Detailed description of the invention
Particular content of the present utility model is described in detail below in conjunction with the drawings and specific embodiments.
As shown in Figure 1, effective integrated soda acid and organic exhaust gas adsorption device, comprise: absorption tower body 1 and active carbon absorption plant 2, the side, lower end of described absorption tower body 1 is provided with centrifugal blower 3, one end of pipeline 4 is connected with centrifugal blower 3, the inside, lower end that the other end of described pipeline 4 stretches into absorption tower body 1 is interconnected with it, one end that described pipeline 4 is connected with absorption tower body 1 is provided with oblique air inlet 5, the lower end opposite side of described absorption tower body 1 is provided with soda acid fluid storage tank 6, the upper end of described soda acid fluid storage tank 6 is provided with water pump 7, one end of tube connector 8 is connected with water pump 7, the other end of described tube connector 8 is connected with the shower 9 be arranged in absorption tower body 1, described shower 9 is provided with some nozzles 10, Pall ring filler layer 11 is provided with in absorption tower body 1 below described shower 9, rotational flow plate defroster 12 is provided with in absorption tower body 1 above described shower 9, the upper end of described absorption tower body 1 is connected with active carbon absorption plant 2 by delivery conduit 13, the inner upper end of described active carbon absorption plant 2 is provided with the Pall ring be connected with delivery conduit 13 and removes water layer 14, at described Pall ring except the upper end of water layer 14 is provided with feeding port 15, at described Pall ring except the side, lower end of water layer 14 is provided with discharge outlet 16, filter cotton 17 is provided with except in the active carbon absorption plant 2 below water layer 14 at described Pall ring, activated carbon filter layer 18 is provided with in active carbon absorption plant 2 below described filter cotton 17, the side, lower end of described active carbon absorption plant 2 is provided with exhaust outlet 19.
When above-mentioned effective integrated soda acid and organic exhaust gas adsorption device use, start centrifugal blower 3 and water pump 7, waste gas is by centrifugal blower 3 intake line 4, enter in absorption tower body 1 through oblique air inlet 5, acid & alkali liquid in soda acid fluid storage tank 6 is by water pump 7 suction connection 8, thus enter in shower 9, acid & alkali liquid is sprayed by nozzle 10 pairs of waste gas, be used for regulating pH value, when acid & alkali liquid is through Pall ring filler layer 11, Pall ring filler layer 11 effectively can be separated the gas liquid mixture of mixing, waste gas after PH has regulated through the rotational flow plate defroster 12 of absorption tower body 1 inner upper end, demist is carried out to waste gas, waste gas after demist enters by delivery conduit 13 Pall ring being arranged on inside, active carbon absorption plant 2 upper end and removes in water layer 14, Pall ring removes water layer 14 pairs of waste gas and carries out secondary gas-liquid separation, water after separation is discharged outside active carbon absorption plant 2 by discharge outlet 16, waste gas after separation is filtered by filter cotton 17, waste gas after filtration passes in activated carbon filter layer 18, active carbon effectively absorbs there being the organic matter in waste gas, waste gas after having processed is discharged by exhaust outlet 19.
Above-mentioned effective integrated soda acid and organic exhaust gas adsorption device, all Pall ring filler is filled with in absorption tower body and active carbon absorption plant, can moisture content effectively in divided gas flow, reduce the moisture content of gas, the harmful substance in gas is absorbed by active carbon, absorption efficiency is high, the absorption cycle is long, ensure that gas can reach discharge standard, adopt set of device to process acid, alkali waste gas and various organic exhaust gas, purification efficiency is high, and cost is low simultaneously, economize energy, has responded the call that national energy-saving reduces discharging.
Claims (1)
1. effective integrated soda acid and organic exhaust gas adsorption device, it is characterized in that: comprising: absorption tower body (1) and active carbon absorption plant (2), the side, lower end on described absorption tower body (1) is provided with centrifugal blower (3), one end of pipeline (4) is connected with centrifugal blower (3), the inside, lower end that the other end of described pipeline (4) stretches into absorption tower body (1) is interconnected with it, one end that described pipeline (4) is connected with absorption tower body (1) is provided with oblique air inlet (5), the lower end opposite side on described absorption tower body (1) is provided with soda acid fluid storage tank (6), the upper end of described soda acid fluid storage tank (6) is provided with water pump (7), one end of tube connector (8) is connected with water pump (7), the other end of described tube connector (8) is connected with the shower (9) be arranged in absorption tower body (1), described shower (9) is provided with some nozzles (10), Pall ring filler layer (11) is provided with in the absorption tower body (1) of described shower (9) below, rotational flow plate defroster (12) is provided with in the absorption tower body (1) of described shower (9) top, the upper end on described absorption tower body (1) is connected with active carbon absorption plant (2) by delivery conduit (13), the inner upper end of described active carbon absorption plant (2) is provided with the Pall ring be connected with delivery conduit (13) and removes water layer (14), at described Pall ring except the upper end of water layer (14) is provided with feeding port (15), at described Pall ring except the side, lower end of water layer (14) is provided with discharge outlet (16), filter cotton (17) is provided with except in the active carbon absorption plant (2) below water layer (14) at described Pall ring, activated carbon filter layer (18) is provided with in the active carbon absorption plant (2) of described filter cotton (17) below, the side, lower end of described active carbon absorption plant (2) is provided with exhaust outlet (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420469670.3U CN204051377U (en) | 2014-08-19 | 2014-08-19 | Effective integrated soda acid and organic exhaust gas adsorption device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420469670.3U CN204051377U (en) | 2014-08-19 | 2014-08-19 | Effective integrated soda acid and organic exhaust gas adsorption device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204051377U true CN204051377U (en) | 2014-12-31 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420469670.3U Expired - Fee Related CN204051377U (en) | 2014-08-19 | 2014-08-19 | Effective integrated soda acid and organic exhaust gas adsorption device |
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| CN (1) | CN204051377U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104190229A (en) * | 2014-08-19 | 2014-12-10 | 江苏自强环保科技有限公司 | High-efficiency integrated acid base and organic waste gas adsorption device |
| CN104941427A (en) * | 2015-06-25 | 2015-09-30 | 莫成杰 | Novel acid-base organic waste gas purifier |
| CN105381677A (en) * | 2015-12-11 | 2016-03-09 | 天紫工程管理（天津）有限公司 | Waste plastic granulation exhaust gas treatment system |
| CN105854498A (en) * | 2016-06-17 | 2016-08-17 | 安庆市虹泰新材料有限责任公司 | Chemical plant waste gas treatment device |
| CN105944482A (en) * | 2016-06-17 | 2016-09-21 | 安庆市虹泰新材料有限责任公司 | Waste gas treatment mechanism |
| CN106390674A (en) * | 2016-06-17 | 2017-02-15 | 安庆市虹泰新材料有限责任公司 | Recovering and purifying device for industrial exhaust gas |
-
2014
- 2014-08-19 CN CN201420469670.3U patent/CN204051377U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104190229A (en) * | 2014-08-19 | 2014-12-10 | 江苏自强环保科技有限公司 | High-efficiency integrated acid base and organic waste gas adsorption device |
| CN104941427A (en) * | 2015-06-25 | 2015-09-30 | 莫成杰 | Novel acid-base organic waste gas purifier |
| CN105381677A (en) * | 2015-12-11 | 2016-03-09 | 天紫工程管理（天津）有限公司 | Waste plastic granulation exhaust gas treatment system |
| CN105854498A (en) * | 2016-06-17 | 2016-08-17 | 安庆市虹泰新材料有限责任公司 | Chemical plant waste gas treatment device |
| CN105944482A (en) * | 2016-06-17 | 2016-09-21 | 安庆市虹泰新材料有限责任公司 | Waste gas treatment mechanism |
| CN106390674A (en) * | 2016-06-17 | 2017-02-15 | 安庆市虹泰新材料有限责任公司 | Recovering and purifying device for industrial exhaust gas |
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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: 20141231 Termination date: 20170819 |