CN205598912U - Separation of industry organic waste gas vary voltage multimembrane is concentrated from going back original mounting - Google Patents
Separation of industry organic waste gas vary voltage multimembrane is concentrated from going back original mounting Download PDFInfo
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- CN205598912U CN205598912U CN201620067509.2U CN201620067509U CN205598912U CN 205598912 U CN205598912 U CN 205598912U CN 201620067509 U CN201620067509 U CN 201620067509U CN 205598912 U CN205598912 U CN 205598912U
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- enrichment facility
- air inlet
- desorption
- control valve
- separation
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Abstract
The utility model provides a separation of industry organic waste gas vary voltage multimembrane is concentrated from going back original mounting, belongs to the concentrated technical field of organic waste gas separation. The enrichment facility includes main intake hole, two extra -air inlets, main exhaust gas mouth, and the enrichment facility both ends are arranged respectively in to main intake hole, main exhaust gas mouth, and enrichment facility both ends, the inside multilayer diffusion barrier that is equipped with of enrichment facility are also arranged respectively in to two enrichment facility extra -air inlets, dust removal desicator one end links to each other with the air inlet, and the other end passes through the varying -voltage control valve and links to each other with main intake hole, and enrichment facility main exhaust gas antilinear varying -voltage control valve links to each other with the main exhaust fan, haustorium one end is separated to the microwave and the desorption fan links to each other, and the other end links to each other with one of them extra -air inlet through reverse attenuator, desorption control valve respectively, and the other end of desorption fan links to each other with another extra -air inlet. The utility model discloses can be according to actual amount of wind needs control valve, and simple accurate, improve production efficiency, utilize microwave desorption gas can lengthen the life of enrichment facility simultaneously.
Description
Technical field
This utility model relates to a kind of membrane separation device, particularly to a kind of industry organic exhaust gas transformation many membrane separation concentrations autoreduction device, belongs to organic exhaust gas separation concentration technique field.
Technical background
At present, the scope of application of gas separation concentration device is quite varied, almost relates to the every aspect in commercial production, is required for using when processing and manufacture.Gas separation concentration device be mainly used in oil refining and petrochemical industry organic fine chemical industry, synthetic material, chemical drugs former medicine manufacture, equipment manufacturing application, plastic product manufacture, electronic equipment manufacturing, print, bind, in the daily life such as industry and building decoration, food and beverage sevice and garment dry cleaning such as industry cleaning link, the most frequent in equipment manufacturing paint industry especially.
In equipment manufacturing painting operation, gas separation concentration device is mainly used in the separation before organic waste-gas purification and concentrates, the volume being so possible not only to minimizing organic exhaust gas reaches the effect of unhurried current current stabilization, harmful substance in waste gas can also be focused on, and then raising purification efficiency, it is highly important part in VOCs treatment industry.
In prior art, it is possible to the universal existence of device concentrated for Wind Volume, low-concentration organic exhaust gas is filtered or absorption is abundant not, and of long duration, efficiency is low, and changes the shortcomings such as the most frequent.
Utility model content
The purpose of this utility model is to provide for a kind of easy to adjust, the suitability is strong, efficiency is high gas separation concentration device, i.e. a kind of industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device, which overcome the shortcoming that existing enrichment facility exists, achieve separation concentrate and solve adsorption desorption automatization, decrease the equipment work requirement to manpower.
The technical solution of the utility model is as follows: a kind of industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device, it is characterized in that, including air inlet, dedusting exsiccator, enrichment facility, microwave desorption device, desorption blower fan, main exhaust fan, be placed in the air vent at main exhaust fan；
Described enrichment facility includes enrichment facility primary air inlet, enrichment facility extra-air inlet, enrichment facility main vent and enrichment facility auxiliary exhaust port, enrichment facility primary air inlet, enrichment facility main vent are respectively placed in enrichment facility two ends, enrichment facility extra-air inlet and enrichment facility auxiliary exhaust port are also respectively placed in enrichment facility two ends, are provided with multilamellar separation film inside enrichment facility；
Described dedusting exsiccator one end is connected with air inlet, and the other end is connected with enrichment facility primary air inlet by voltage control valve, and described enrichment facility main vent is connected with main exhaust fan through voltage control valve；
Described microwave desorption device one end is connected with desorption blower fan, and the other end is connected with one of them enrichment facility extra-air inlet by reverse antivibrator, desorbing control valve respectively, and the other end of described desorption blower fan is connected with another enrichment facility auxiliary exhaust port.
Described separation film has different film cross section flux, by the ordered arrangement of multilamellar separation film, can only separate the gas of required filtering and concentrating by the elemental gas of special diameter size.
It is connected between described desorption blower fan and enrichment facility auxiliary exhaust port and has shunting selection machine.
Described shunting selection machine two ends are connected to control valve.
Connect between described microwave desorption device, desorption blower fan and have reverse antivibrator, control valve.
Described enrichment facility is at least one.
In this utility model, dedusting exsiccator is directly connected with air inlet, can play the effect that dedusting is dried, can reach again the effect of unhurried current current stabilization.Enrichment facility realizes concentration and the solution adsorption desorption of gas by the control valve of import and export, and microwave desorption device is connected with two extra-air inlets of enrichment facility with desorption blower fan, separates, for fast desorption desorption, the gas that film institute filtering and concentrating goes out.
Organic exhaust gas is mainly delivered to enrichment facility after dedusting exsiccator processes, and is transported to air vent by microwave desorption device and desorption blower fan by separating the gas after concentrating.This utility model integrated level is high, is conducive to improving the automatization level of product, and orderly intelligentized control method is conducive to improving treatment effeciency and the service life of whole device.
Usefulness of the present utility model:
1. this utility model can realize the dedusting of gas and is dried, separates concentration with to solve adsorption desorption close-coupled processing, reduces the overall dimensions of device, the treatment effeciency of raising gas；
2. this utility model can be not only used for pretreatment stage before large-scale organic waste-gas purification processes, and the concentration that be can be used for gas in daily life by simple repacking is used；
3. this utility model uses the technology such as voltage control, microwave desorbing can significantly improve the service life of device.
A kind of gas separation concentration device of this utility model design is relatively flexible, can need adjusting control valve according to actual air volume, and simple and easy to do, improves production efficiency, utilizes microwave desorption gas can extend the service life of enrichment facility simultaneously.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
In figure: 1 air inlet, 2 dedusting exsiccators, 3 enrichment facilities, 4 enrichment facility primary air inlets, 5 enrichment facility extra-air inlets, 6 separation films, 7 enrichment facility main vents, 8 enrichment facility auxiliary exhaust ports, 9 microwave desorption devices, 10 desorption blower fans, 11 shunting selection machine, 12 main exhaust fans, 13 air vents, 14 voltage control valves, 15 desorbing control valves, 16 reverse antivibrators, 17 reverse antivibrators.
Detailed description of the invention
In order to enable more clearly to state this utility model patent, this utility model is further described by the accompanying drawing 1 in conjunction with transformation many membrane separation concentrations autoreduction device.
A kind of industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device, is mainly made up of air inlet 1, dedusting exsiccator 2, enrichment facility 3, microwave desorption device 9, desorption blower fan 10, shunting selection machine 11, main exhaust fan 12, air vent 13, voltage control valve 14, desorbing control valve 15 and reverse antivibrator 16,17 etc..
Enrichment facility includes enrichment facility primary air inlet 4, enrichment facility extra-air inlet 5, enrichment facility main vent 7, enrichment facility auxiliary exhaust port 8, enrichment facility primary air inlet 4, enrichment facility main vent 7 are respectively placed in enrichment facility two ends, enrichment facility extra-air inlet 5, enrichment facility auxiliary exhaust port 8 are also respectively placed in enrichment facility two ends, and enrichment facility 3 is internal is provided with multilamellar separation film 6.
Dedusting exsiccator 2 is directly connected with air inlet 1, then is connected with enrichment facility primary air inlet 4 by voltage control valve 14；Enrichment facility main vent 7 is connected with main exhaust fan 12 through voltage control valve 14.
Microwave desorption device 9 is connected with desorption blower fan 10, and reverse antivibrator 16 and desorbing control valve 15 are arranged between microwave desorption device 9 and enrichment facility extra-air inlet 5, after desorption blower fan 10 is joined directly together with shunting selection machine 11, then is connected with enrichment facility auxiliary exhaust port 8.
Separate film 6 and there is different film cross section flux, by the ordered arrangement of multilamellar separation film 6, the gas of required filtering and concentrating can only be separated by the elemental gas of special diameter size.
Enrichment facility controls internal pressure by voltage control valve, successively separates harmful gas composition in combination with separating film；Microwave desorption device is connected with extra-air inlet 5, the gas after utilizing microwave principle solution adsorption desorption to filter.
Organic exhaust gas enters dedusting exsiccator 2 by air inlet 1, it is possible not only to after treatment gas carries out the effect that dedusting is dried and can reach unhurried current current stabilization, then gas is transferred in enrichment facility 3 by primary air inlet 4, by voltage control valve 14, the pressure of gas in device can be controlled between so that it is reach optimal separation enrichment stage；Gas harmful composition after separation can pass through the combination of microwave desorption device 9, desorbing control valve 15 and desorption blower fan 10 and control, and is transported to air vent 13 through main vent 7 and main exhaust fan 12 and is for further processing, thus reaches to solve the effect of adsorption desorption autoreduction.
This utility model integrated level is high, is conducive to improving the automatization level of product, and orderly intelligentized control method is conducive to improving treatment effeciency and the service life of whole device.
Claims (6)
1. industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device, it is characterized in that, including air inlet (1), dedusting exsiccator (2), enrichment facility (3), microwave desorption device (9), desorption blower fan (10), main exhaust fan (12), be placed in the air vent (13) at main exhaust fan；
Described enrichment facility includes enrichment facility primary air inlet (4), enrichment facility extra-air inlet (5), enrichment facility main vent (7), enrichment facility auxiliary exhaust port (8), enrichment facility primary air inlet (4), enrichment facility main vent (7) are respectively placed in enrichment facility two ends, enrichment facility extra-air inlet (5), enrichment facility auxiliary exhaust port (8) are also respectively placed in enrichment facility two ends, and enrichment facility (3) is internal is provided with multilamellar separation film (6)；
Described dedusting exsiccator (2) one end is connected with air inlet (1), and the other end is connected with enrichment facility primary air inlet (4) by voltage control valve (14), and described enrichment facility main vent (7) is connected with main exhaust fan (12) through voltage control valve；
Described microwave desorption device (9) one end is connected with desorption blower fan (10), the other end is connected with enrichment facility extra-air inlet (5) by reverse antivibrator (16), desorbing control valve (15) respectively, and the other end of described desorption blower fan (10) is connected with enrichment facility auxiliary exhaust port (8).
A kind of industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device the most according to claim 1, it is characterized in that, described separation film (6) has different film cross section flux, can only be by the elemental gas of special diameter size, by the ordered arrangement of multilamellar separation film (6), separate the gas of required filtering and concentrating.
A kind of industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device the most according to claim 1, is characterized in that, be connected and have shunting selection machine (11) between described desorption blower fan (10) and enrichment facility auxiliary exhaust port (8).
A kind of industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device the most according to claim 3, is characterized in that, described shunting selection machine (11) two ends are connected to control valve.
A kind of industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device the most according to claim 1, is characterized in that, connecting between described microwave desorption device (9), desorption blower fan (10) has reverse antivibrator (17), control valve.
A kind of industrial organic exhaust gas transformation many membrane separation concentrations autoreduction device the most according to claim 1, is characterized in that, described enrichment facility (3) at least.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620067509.2U CN205598912U (en) | 2016-01-25 | 2016-01-25 | Separation of industry organic waste gas vary voltage multimembrane is concentrated from going back original mounting |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620067509.2U CN205598912U (en) | 2016-01-25 | 2016-01-25 | Separation of industry organic waste gas vary voltage multimembrane is concentrated from going back original mounting |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205598912U true CN205598912U (en) | 2016-09-28 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620067509.2U Expired - Fee Related CN205598912U (en) | 2016-01-25 | 2016-01-25 | Separation of industry organic waste gas vary voltage multimembrane is concentrated from going back original mounting |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205598912U (en) |
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2016
- 2016-01-25 CN CN201620067509.2U patent/CN205598912U/en not_active Expired - Fee Related
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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 |
Granted publication date: 20160928 Termination date: 20190125 |
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| CF01 | Termination of patent right due to non-payment of annual fee |