CN206463738U - A kind of organic gas recovery type sterilizing deodorization device - Google Patents
A kind of organic gas recovery type sterilizing deodorization device Download PDFInfo
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- CN206463738U CN206463738U CN201720151601.1U CN201720151601U CN206463738U CN 206463738 U CN206463738 U CN 206463738U CN 201720151601 U CN201720151601 U CN 201720151601U CN 206463738 U CN206463738 U CN 206463738U
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- import
- absorbing liquid
- tower
- destilling tower
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Abstract
The utility model discloses a kind of organic gas recovery type sterilizing deodorization device, including：Absorption tower, destilling tower, condenser, distillation still；It is characterized in that：The absorbing liquid import on the absorption tower is connected by pipeline with the outlet of absorbing liquid solution feed pump, the bottom leakage fluid dram on absorption tower is connected with the import of original fluid container, the outlet of original fluid container is connected with the import of stoste solution feed pump, the outlet of stoste solution feed pump is connected with the import of destilling tower, the top vent of destilling tower is connected with the import of condenser, the bottom of destilling tower is connected by pipeline with the bottom of distillation still, the top vent of distillation still in the middle part of destilling tower with being connected, having heaters is installed in distillation still, the bottom of destilling tower is also connected by pipeline with the import of absorbing liquid temporary storage tank, import of the absorbing liquid temporary storage tank through reflux pump with absorbing flow container is connected, the outlet for absorbing flow container is connected with the import of absorbing liquid solution feed pump, the utility model has energy-conservation, environmental protection, the high advantage of organic efficiency.
Description
Technical field
The utility model belongs to sterilizing deodorization technique field, and in particular to a kind of organic gas recovery type sterilizing deodorization dress
Put.
Background technology
VOC（Volatile Organic Compounds, VOC）It is petrochemical process and each
Plant the industry using organic solvent, such as spray painting, printing, pharmacy, the most common pollutant of coal chemical industry industry discharge.Such is changed
Compound majority has penetrating odor and toxicity.Part has been listed in carcinogenic substance；Most VOC gases are inflammable and explosive, and enterprise is given birth to
Production safety threatens.
Due to VOC danger, the discharge to VOC of promulgating a decree of many countries has carried out control.American-European countries is in 20 generation
Record before and after the nineties, emission request is all defined to the place of all use organic solvents.The U.S. improves waste gas row nineteen ninety
Standard is put, 189 kinds of pollutants in industrial production toxic pollutant is classified as, wherein most is VOC.What China promulgated《Greatly
Gas prevention and cure of pollution method》It is required that carrying out purified treatment to the toxic gas produced in industrial production, profit will be reclaimed to imflammable gas
With；China《Discharge standard of air pollutants》The discharge standard of 33 kinds of volatile organic matters is defined, will be most
Other volatile organic matters press non-methane
Class hydrocarbon is handled, and defines unified discharge standard（＜ l20mg/m3）.
Disruptive method and the class of non-destructive method two can also be divided into by removing the method for VOC in industrial waste gas.It is destructive
Method such as thermal oxidation method, CO2 and H2O are changed into by VOC gases；Non-destructive method is absorption method.Conventional absorption method has work
Property carbon adsorption, condensation method and membrane separation process etc..
Mainly there are absorption and sorption, catalysis burning etc. to the processing method that VOCs treatment is used both at home and abroad at present, these
Method device therefor is more, technique is numerous, energy consumption is big；And relatively popular biological treatment faces floor space greatly, easily by
Load variations influence, microorganism strains filtration and domestication difficulty still than it is larger the problems such as.Therefore, it is economical, efficiently administer low
The recovery of organic gas in concentration, the waste gas of big flow, in addition to conventional art is improved, the new technology of exploitation of still needing.
Utility model content
The purpose of this utility model is to overcome above-mentioned the deficiencies in the prior art to sterilize there is provided a kind of organic gas recovery type
Deodorization device.
A kind of organic gas recovery type sterilizing deodorization device, including：Absorption tower, destilling tower, condenser, distillation still；It is special
Levy and be：The absorbing liquid import on the absorption tower is connected by pipeline with the outlet of absorbing liquid solution feed pump, the bottom on absorption tower
Leakage fluid dram is connected with the import of original fluid container, and the outlet of original fluid container is connected with the import of stoste solution feed pump, stoste solution feed pump
Outlet is connected with the import of destilling tower, and the top vent of destilling tower is connected with the import of condenser, the bottom of destilling tower
It is connected by pipeline with the bottom of distillation still, the top vent of distillation still in the middle part of destilling tower with being connected, in distillation still
Having heaters is installed, the bottom of destilling tower is also connected by pipeline with the import of absorbing liquid temporary storage tank, absorbing liquid temporary storage tank warp
Import of the reflux pump with absorbing flow container is connected, and the outlet for absorbing flow container is connected with the import of absorbing liquid solution feed pump.
Preferably, the top on the absorption tower is provided with demister, the side wall of absorption tower bottom and is provided with exhaust gas inlet
Pipe.
Preferably, the leakage fluid dram of the condenser is connected with the import of finished pot.
Compared with prior art, the beneficial effects of the utility model：
The utility model is realized by absorption tower to be absorbed to organic gas in waste gas, the waste gas handled by absorption tower
Go out from absorbing tower top row, realize qualified discharge, absorb the stoste after organic gas and enter distillation column distillation, organic gas volatilization
Liquid is condensed into gaseous state into condenser, the recovery of organic gas is realized, the stoste after distillation is re-fed into absorption flow container weight
Newly use, have the advantages that energy-saving and environmental protection, organic efficiency are high.
Brief description of the drawings
Fig. 1 is a kind of structural representation of organic gas recovery type sterilizing deodorization device of the utility model.
In figure, 1, absorb flow container, 2, absorbing liquid solution feed pump, 3, demister, 4, absorption tower, 5, exhaust gas inlet pipe, 6, stoste
Tank, 7, stoste solution feed pump, 8, destilling tower, 9, condenser, 10, finished pot, 11, distillation still, 12, heater, 13, reflux pump, 14,
Absorbing liquid temporary storage tank.
Embodiment
Referring to Fig. 1, a kind of organic gas recovery type sterilizing deodorization device, including：Absorption tower 4, destilling tower 8, condenser 9,
Distillation still 11；It is characterized in that：The absorbing liquid import on the absorption tower 4 is connected by pipeline with the outlet of absorbing liquid solution feed pump 2
Connect, the bottom leakage fluid dram on absorption tower 4 is connected with the import of original fluid container 6, the outlet of original fluid container 6 and the import of stoste solution feed pump 7
It is connected, the outlet of stoste solution feed pump 7 is connected with the import of destilling tower 8, top vent and the condenser 9 of destilling tower 8
Import is connected, and the bottom of destilling tower 8 is connected by pipeline with the bottom of distillation still 11, the top vent of distillation still 11 with
The middle part of destilling tower 8 is connected, and having heaters 12 is installed in distillation still 11, the bottom of destilling tower 8 also passes through pipeline and absorbing liquid
The import of temporary storage tank 14 is connected, and import of the absorbing liquid temporary storage tank 14 through reflux pump 13 with absorbing flow container 1 is connected, and absorbs flow container
1 outlet is connected with the import of absorbing liquid solution feed pump 2.
The top on the absorption tower 4 is provided with demister 3, the side wall of the bottom of absorption tower 4 and is provided with exhaust gas inlet pipe 5.
The leakage fluid dram of the condenser 9 is connected with the import of finished pot 10.
Utility model is exemplarily described above in conjunction with accompanying drawing for technical solutions of the utility model, it is clear that this practicality
New implement is not subject to the restrictions described above, as long as employing method design of the present utility model and technical scheme progress
Various unsubstantialities improve, or it is not improved the design of utility model and technical scheme are directly applied into other occasions,
Within protection domain of the present utility model.
Claims (3)
- The deodorization device 1. a kind of organic gas recovery type sterilizes, including：Absorption tower（4）, destilling tower（8）, condenser（9）, distillation Kettle（11）；It is characterized in that：The absorption tower（4）Absorbing liquid import pass through pipeline and absorbing liquid solution feed pump（2）Outlet phase Connection, absorption tower（4）Bottom leakage fluid dram and original fluid container（6）Import be connected, original fluid container（6）Outlet and stoste solution feed pump （7）Import be connected, stoste solution feed pump（7）Outlet and destilling tower（8）Import be connected, destilling tower（8）Top row Gas port and condenser（9）Import be connected, destilling tower（8）Bottom pass through pipeline and distillation still（11）Bottom be connected, Distillation still（11）Top vent and destilling tower（8）Middle part be connected, distillation still（11）Interior installation having heaters（12）, steam Evaporate tower（8）Bottom also pass through pipeline and absorbing liquid temporary storage tank（14）Import be connected, absorbing liquid temporary storage tank（14）Through backflow Pump（13）With absorbing flow container（1）Import be connected, absorb flow container（1）Outlet and absorbing liquid solution feed pump（2）Import be connected Connect.
- 2. a kind of organic gas recovery type sterilizing deodorization device as claimed in claim 1, it is characterised in that：The absorption tower （4）Top demister is installed（3）, absorption tower（4）Exhaust gas inlet pipe is installed on the side wall of bottom（5）.
- 3. a kind of organic gas recovery type sterilizing deodorization device as claimed in claim 1, it is characterised in that：The condenser （9）Leakage fluid dram and finished pot（10）Import be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720151601.1U CN206463738U (en) | 2017-02-20 | 2017-02-20 | A kind of organic gas recovery type sterilizing deodorization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720151601.1U CN206463738U (en) | 2017-02-20 | 2017-02-20 | A kind of organic gas recovery type sterilizing deodorization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206463738U true CN206463738U (en) | 2017-09-05 |
Family
ID=59707096
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720151601.1U Expired - Fee Related CN206463738U (en) | 2017-02-20 | 2017-02-20 | A kind of organic gas recovery type sterilizing deodorization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206463738U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116603367A (en) * | 2023-05-30 | 2023-08-18 | 华澄(江门)环保装备科技有限公司 | Toughened glass silk screen waste gas recycling and purifying system and method |
-
2017
- 2017-02-20 CN CN201720151601.1U patent/CN206463738U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116603367A (en) * | 2023-05-30 | 2023-08-18 | 华澄(江门)环保装备科技有限公司 | Toughened glass silk screen waste gas recycling and purifying system and method |
| CN116603367B (en) * | 2023-05-30 | 2024-04-02 | 广东华澄环保装备科技有限公司 | Toughened glass silk screen waste gas recycling and purifying system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170905 Termination date: 20210220 |
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| CF01 | Termination of patent right due to non-payment of annual fee |