CN203061024U - Organic waste gas adsorption and steam stripping recovery and treatment device - Google Patents
Organic waste gas adsorption and steam stripping recovery and treatment device Download PDFInfo
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- CN203061024U CN203061024U CN 201220636568 CN201220636568U CN203061024U CN 203061024 U CN203061024 U CN 203061024U CN 201220636568 CN201220636568 CN 201220636568 CN 201220636568 U CN201220636568 U CN 201220636568U CN 203061024 U CN203061024 U CN 203061024U
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- exhaust gas
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Abstract
The utility model discloses an organic waste gas adsorption and steam stripping recovery and treatment device. The device comprises a first adsorbent bed and a second adsorbent bed. One end of the first adsorbent bed and one end of the second adsorbent bed are connected with a waste gas source together through input ducts; the other end of the first adsorbent bed and the other end of the second adsorbent bed are connected with a main fan together through output ducts; the first adsorbent bed and the second adsorbent bed are connected with a steam source together through steam ducts; the device is provided with a condenser connected with the output ducts of the first adsorbent bed and the second adsorbent bed respectively, and the condenser is connected with a condensate recovery tank; and the condensate recovery tank is also connected with the input ducts, the first adsorbent bed and the second adsorbent bed respectively. The device is mainly used for treating waste gases generated in loading, major breath of a storage tank and temperature difference breath of the storage tank; and the waste gases in contact with the air are probably in an explosion range. The high-concentration waste gases are mixed with the air in shortest time and smallest space, so that the concentration of the treated waste gases is reduced to be less than 25 percent below the lower limit of the explosion limit, and then the safety is ensured.
Description
Technical field:
The utility model relates to emission-control equipment, particularly a kind of organic exhaust gas absorption and steam desorption recycling and processing device.
Background technology:
As everyone knows, the recycling of existing organic exhaust gas is owing to the reason of process aspect, its cost is generally than higher, and on the effect of recycling, also be difficult to accomplish organic exhaust gas is thoroughly reclaimed, do not reach the requirement of waste gas circulation, become a great problem of puzzlement enviromental protection enterprise.
The utility model content:
In view of above-mentioned technical problem, the utility model provides a kind of organic exhaust gas absorption and steam desorption recycling and processing device.This device adsorbs organic exhaust gas operations such as reflection, steam desorption, purging cooling by automatic control and waste gas is carried out circular treatment, the waste gas safety after guaranteeing to handle.
Concrete technical scheme of the present utility model is as follows:
Organic exhaust gas absorption and steam desorption recycling and processing device comprise first adsorbent bed and second adsorbent bed, it is characterized in that an end of described first adsorbent bed and second adsorbent bed is connected exhaust gas source jointly by input channel; The other end of described first adsorbent bed and second adsorbent bed is connected main air blower jointly by output channel; Described first adsorbent bed is connected vapour source with second adsorbent bed jointly by steam pipework; The described condenser that is connected with the output channel of first adsorbent bed and second adsorbent bed respectively that is provided with, this condenser connects the condensate liquid accumulator tank; Described condensate liquid accumulator tank also connects input channel, first adsorbent bed and second adsorbent bed respectively.
In the such scheme, described exhaust gas source is the waste gas from useless admittedly warehouse or storage tank.
In the such scheme, described condenser is set to the condenser of two series connection.
In the such scheme, the input channel of described first adsorbent bed and second adsorbent bed is connected purging motor respectively.
In the such scheme, the density of described vapour source is 6kgf/cm
2
The utility model is primarily aimed at entrucking, the big breathing of storage tank, the storage tank temperature difference and breathes the waste gas that produces, because it contacts with air, may be in the explosive range.So mix in the shortest and in the minimum space by allowing high-concentration waste gas and air, and make the concentration after handling drop to below 25% of lower explosive limit, thereby guarantee safety.
Description of drawings:
Further specify the utility model below in conjunction with the drawings and specific embodiments.
Fig. 1 is the structured flowchart of organic exhaust gas absorption described in the utility model and steam desorption recycling and processing device.
The specific embodiment:
For technological means, creation characteristic that the utility model is realized, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
As shown in Figure 1, organic exhaust gas absorption described in the utility model and steam desorption recycling and processing device, it comprises first adsorbent bed 100 and second adsorbent bed 200.
Wherein, first adsorbent bed 100 is connected exhaust gas source 300 with an end of second adsorbent bed 200 jointly by input channel, and this exhaust gas source 300 can be the waste gas from useless admittedly warehouse or storage tank.The other end of first adsorbent bed 100 and second adsorbent bed 200 is connected main air blower 400 jointly by output channel, and this main air blower connects gas discharging tower 401.It is 6kgf/cm that first adsorbent bed 100 is connected its density of vapour source 500(with second adsorbent bed 200 jointly by steam pipework
2, from the workshop).
In addition, treating apparatus also is provided with the condenser 600 of two series connection that are connected with the output channel of first adsorbent bed 100 and second adsorbent bed 200 respectively, and this condenser 600 connects condensate liquid accumulator tank 601.Condensate liquid accumulator tank 601 also connects input channel 700, first adsorbent bed 100 and second adsorbent bed 200 respectively.The input channel 700 of first adsorbent bed 100 and second adsorbent bed 200 is connected purging motor 800 respectively.
Waste gas is through exhaust gas source 300 mixing airs, drops to that to enter the first adsorbent bed 100(, second adsorbent bed 200 this moment after the safe concentration standby), send into chimney 401 high-altitude qualified discharges with main air blower 400 then; Close exhaust gas inlet and outlet after 100 absorption of first adsorbent bed are saturated, change into and enter standby second adsorbent bed, 200 processing, first adsorbent bed 100 enters the regeneration stage.
Open the steam inlet of first adsorbent bed 100, steam directly heats 100 interior activated carbon of first adsorbent bed, and the solvent of absorption is heated and is driven out of in the carbon, enters condenser 600 coolings of series connection, cooling fluid enters cooling liquid bath 601 and reclaims, and incoagulable gas returns second adsorbent bed 200 and handles the back discharging.When the regeneration of first adsorbent bed 100 finishes, the steam off import, first adsorbent bed 100 enters cooling stage.
Open purging motor 800, open cooling air import and the condensed water sewage draining exit of first adsorbent bed 100, cold wind enters first adsorbent bed 100 and purges damp and hot activated carbon, steam is taken out of enters condenser 600 coolings, condensed water enters the condensation liquid bath equally, and incoagulability wind returns first adsorbent bed 100 and further purges, and drops to room temperature up to first adsorbent bed, the cooling air import of shut-down purge blower fan 800 and first adsorbent bed 100, condensed water sewage draining exit, first adsorbent bed 100 enters stand-by state.
More than show and described basic principle of the present utility model and principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that describes in above-described embodiment and the specification just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed the utility model scope.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (5)
1. organic exhaust gas absorption and steam desorption recycling and processing device comprise first adsorbent bed and second adsorbent bed, it is characterized in that an end of described first adsorbent bed and second adsorbent bed is connected exhaust gas source jointly by input channel; The other end of described first adsorbent bed and second adsorbent bed is connected main air blower jointly by output channel; Described first adsorbent bed is connected vapour source with second adsorbent bed jointly by steam pipework; The described condenser that is connected with the output channel of first adsorbent bed and second adsorbent bed respectively that is provided with, this condenser connects the condensate liquid accumulator tank; Described condensate liquid accumulator tank also connects input channel, first adsorbent bed and second adsorbent bed respectively.
2. according to organic exhaust gas absorption and the steam desorption recycling and processing device of claim 1, it is characterized in that described exhaust gas source is the waste gas from useless admittedly warehouse or storage tank.
3. according to organic exhaust gas absorption and the steam desorption recycling and processing device of claim 1, it is characterized in that described condenser is set to the condenser of two series connection.
4. according to organic exhaust gas absorption and the steam desorption recycling and processing device of claim 1, it is characterized in that the input channel of described first adsorbent bed and second adsorbent bed is connected purging motor respectively.
5. according to organic exhaust gas absorption and the steam desorption recycling and processing device of claim 1, it is characterized in that the density of described vapour source is 6kgf/cm
2
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220636568 CN203061024U (en) | 2012-11-27 | 2012-11-27 | Organic waste gas adsorption and steam stripping recovery and treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220636568 CN203061024U (en) | 2012-11-27 | 2012-11-27 | Organic waste gas adsorption and steam stripping recovery and treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203061024U true CN203061024U (en) | 2013-07-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220636568 Expired - Fee Related CN203061024U (en) | 2012-11-27 | 2012-11-27 | Organic waste gas adsorption and steam stripping recovery and treatment device |
Country Status (1)
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| CN (1) | CN203061024U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103386246A (en) * | 2013-08-01 | 2013-11-13 | 北京洁利诺环境科技有限公司 | Method for recycling gasoline from gasoline-containing mixed gas |
| CN105032116A (en) * | 2015-07-06 | 2015-11-11 | 太仓中化环保化工有限公司 | Method for recovering tail gas in fluorocarbon alkane production apparatus |
| CN105536429A (en) * | 2015-12-11 | 2016-05-04 | 凯天环保科技股份有限公司 | Waste gas adsorption treatment device and treatment method thereof |
-
2012
- 2012-11-27 CN CN 201220636568 patent/CN203061024U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103386246A (en) * | 2013-08-01 | 2013-11-13 | 北京洁利诺环境科技有限公司 | Method for recycling gasoline from gasoline-containing mixed gas |
| CN103386246B (en) * | 2013-08-01 | 2016-03-30 | 北京洁利诺环境科技有限公司 | The method of gasoline is reclaimed containing gasoline mixture body |
| CN105032116A (en) * | 2015-07-06 | 2015-11-11 | 太仓中化环保化工有限公司 | Method for recovering tail gas in fluorocarbon alkane production apparatus |
| CN105536429A (en) * | 2015-12-11 | 2016-05-04 | 凯天环保科技股份有限公司 | Waste gas adsorption treatment device and treatment method thereof |
| CN105536429B (en) * | 2015-12-11 | 2018-05-11 | 凯天环保科技股份有限公司 | Exhaust gas absorbing treatment device and processing method |
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Legal Events
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130717 Termination date: 20131127 |