CN205287960U - Processing system to organic waste gas - Google Patents
Processing system to organic waste gas Download PDFInfo
- Publication number
- CN205287960U CN205287960U CN201520984840.6U CN201520984840U CN205287960U CN 205287960 U CN205287960 U CN 205287960U CN 201520984840 U CN201520984840 U CN 201520984840U CN 205287960 U CN205287960 U CN 205287960U
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- waste gas
- spiral board
- spray equipment
- steam
- organic waste
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Abstract
The utility model discloses a processing system to organic waste gas, including whirl washing device, catch water and low temperature plasma organic waste gas processing apparatus, inside supreme alternate baffle, air distributor, first whirl board, a spray set, second whirl board, the 2nd spray set, third whirl board and the 3rd spray set of being provided with in proper order down that follow of whirl washing device, whirl washing device and catch water are connected, and catch water and low temperature plasma organic waste gas processing apparatus are connected. The utility model discloses at first get rid of through whirl washing device and dissolve the water material in the waste gas, then through the organic macromolecule in the low temperature plasma organic waste gas processing apparatus pyrolysis oxidization waste gas to the waste gas that the efficient handling waste plastic granulation produced.
Description
Technical field
This utility model belongs to technical field of waste gas treatment, is specifically related to a kind of process system for organic exhaust gas.
Background technology
The modern life is increasing to the demand of plastics, and the regeneration of waste or used plastics also becomes trend, technics of reclaim of plastic waste is washed pelletize be a kind of turn waste into wealth, way that resource re-uses. But in regeneration and granulation process, when temperature is more than 200 DEG C, the low boiling impurity of plasticizer and inside, oxidation Decomposition can be there is, produce a large amount of harmful gas containing dust granules, wherein contain more organic substance, such as benzene, toluene, styrene, chlorinated organics etc., these harmful gass have contaminative, are directly discharged in air and not only staff can be caused actual bodily harm, also pollute the environment simultaneously.
This type of is contained the waste gas of organic substance, generally adopts the methods such as acid-alkali washing, activated carbon adsorption, catalysis burning to carry out harmless treatment. But acid-alkali washing treatment effeciency is not high, activated carbon absorption has activated carbon frequently to change or regenerates problem costly, and the equipment cost of catalysis burning is higher, it is therefore necessary to the process system of the applicable old plastic granulating exhaust-gas treatment that design research and development are new.
Utility model content
The purpose of this utility model is in that to overcome the deficiencies in the prior art, it is provided that a kind of process system for organic exhaust gas.
This utility model is achieved through the following technical solutions:
A kind of process system for organic exhaust gas, including eddy flow wash mill, steam-water separator and low-temperature plasma organic waste gas treatment device,
Described eddy flow wash mill includes a tank body, the top of tank body is provided with gas outlet, alternate successively from bottom to up in the inside of tank body is provided with dividing plate, gas distributor, the first spiral board, the first spray equipment, the second spiral board, the second spray equipment, the 3rd spiral board and the 3rd spray equipment; Described dividing plate leaves a scupper, the tank skin below dividing plate is provided with one and is recycled into the mouth of a river, be recycled into the mouth of a river and be connected with the first spray equipment, the second spray equipment and the 3rd spray equipment respectively by pipeline;Described first spiral board, the second spiral board and the 3rd spiral board are coaxially fixed on axle, and one end of axle is connected with the motor on tank body top; Tank skin between dividing plate and gas distributor is provided with air inlet;
The gas outlet of eddy flow wash mill is connected with the air inlet of steam-water separator by pipeline, the gas outlet of steam-water separator is connected by the air inlet of pipeline with low-temperature plasma organic waste gas treatment device, and is provided with centrifugal blower on the pipeline that is connected of the air inlet in the gas outlet of steam-water separator with low-temperature plasma organic waste gas treatment device.
In technique scheme, steam-water separator is provided with drain valve.
Advantage of the present utility model and having the beneficial effect that
During use, waste gas is first into inside eddy flow wash mill, waste gas uniformly upwards disperses through gas distributor, gas passes sequentially through the first spiral board, the second spiral board and the 3rd spiral board afterwards, particulate matter in gas is when by the first spiral board, the second spiral board and three spiral boards, merge with atomizing spray liquid, it is attached on spiral board, and through the centrifugal action of spiral board, particulate matter is made to be thrown to tank skin, and it flow to tank bottoms with tank skin, tentatively to remove the water solublity dust granules thing contained in waste gas; Steam-water separator is entered into after gas after eddy flow wash mill processes, the steam in steam-water separator trapping air-flow, and the water in air-flow is discharged from drain valve; Gas enters back in low-temperature plasma organic waste gas treatment device afterwards, low-temperature plasma organic waste gas treatment device adopts double-dielectric barrier discharge, produce highdensity high energy electron, ion, free radical etc., organic macromolecule in pyrolysis oxidization waste gas, it is degraded to stable, free of contamination compound, such as CO2��H2O��N2And other small-molecule substances.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Wherein: a is eddy flow wash mill, a-1 is air inlet, a-2 is dividing plate, a-3 is scupper, a-4 is for being recycled into the mouth of a river, a-5 is water circulating pump, a-6 is gas distributor, a-7 is the first spiral board, a-8 is the second spiral board, a-9 is the 3rd spiral board, a-10 is the first spray equipment, a-11 is the second spray equipment, a-12 is the 3rd spray equipment, a-13 is motor, a-14 is axle, a-15 is gas outlet, b is steam-water separator, b-1 is the air inlet of steam-water separator, b-2 is the gas outlet of steam-water separator, b-3 is drain valve, c is low-temperature plasma organic waste gas treatment device, c-1 is the air inlet of low-temperature plasma organic waste gas treatment device, d is centrifugal blower.
Detailed description of the invention
The technical solution of the utility model is further illustrated below in conjunction with specific embodiment.
A kind of process system for organic exhaust gas involved by this utility model, including eddy flow wash mill a, steam-water separator b and low-temperature plasma organic waste gas treatment device c,
Described eddy flow wash mill a includes a tank body, tank body is vertically arranged, the top of tank body is provided with gas outlet a-15, alternate successively from bottom to up in the inside of tank body is provided with dividing plate a-2, gas distributor a-6, the first spiral board a-7, the first spray equipment a-10, the second spiral board a-8, the second spray equipment a-11, the 3rd spiral board a-9 and the three spray equipment a-12, described dividing plate a-2 level is fixed in inner tank wall, dividing plate a-2 leaves a scupper a-3, tank skin below dividing plate is provided with one and is recycled into mouth of a river a-4, be recycled into mouth of a river a-4 by pipeline respectively with the first spray equipment a-10, second spray equipment a-11 and the three spray equipment a-12 is connected, and it is being recycled into mouth of a river a-4 and the first spray equipment a-10, the pipeline that second spray equipment a-11 and the three spray equipment a-12 is connected is provided with water circulating pump a-5, the water of tank base is made to feed the first spray equipment by water circulating pump a-5, (tank base is pre-loaded with water for second spray equipment and the 3rd spray equipment, the height of water is less than dividing plate), the liquid of three spray equipment ejections is back to tank base through scupper a-3 simultaneously, circulated sprinkling is formed with this,Described first spiral board, the second spiral board and the 3rd spiral board are coaxially fixed on axle a-14, and one end of axle a-14 is connected with the motor a-13 on tank body top, and motor can drive the first spiral board a-7, the second spiral board a-8 and the three spiral board a-9 to rotate by axle; Tank skin between dividing plate a-2 and gas distributor a-6 is provided with at least one air inlet a-1;
The gas outlet a-15 of eddy flow wash mill is connected with the air inlet b-1 of steam-water separator by pipeline, steam-water separator is provided with drain valve b-3, the gas outlet b-2 of steam-water separator is connected with the air inlet c-1 of low-temperature plasma organic waste gas treatment device by pipeline, and is provided with centrifugal blower d on the gas outlet b-2 of steam-water separator and the air inlet c-1 of the low-temperature plasma organic waste gas treatment device pipeline being connected.
During use, waste gas is first into inside eddy flow wash mill, waste gas uniformly upwards disperses through gas distributor a-6, gas passes sequentially through the first spiral board a-7, the second spiral board a-8 and the three spiral board a-9 afterwards, particulate matter in gas is when by the first spiral board a-7, the second spiral board a-8 and the three spiral board a-9, merge with atomizing spray liquid, it is attached on spiral board, and through the centrifugal action of spiral board, particulate matter is made to be thrown to tank skin, and it flow to tank bottoms with tank skin, tentatively to remove the water solublity dust granules thing contained in waste gas; Steam-water separator b is entered into after gas after eddy flow wash mill processes, the steam in steam-water separator trapping air-flow, and the water in air-flow is discharged from drain valve; Gas enters back in low-temperature plasma organic waste gas treatment device c afterwards, low-temperature plasma organic waste gas treatment device adopts double-dielectric barrier discharge, produce highdensity high energy electron, ion, free radical etc., organic macromolecule in pyrolysis oxidization waste gas, it is degraded to stable, free of contamination compound, such as CO2��H2O��N2And other small-molecule substances.
Above this utility model has been done exemplary description; should be noted that; when without departing from core of the present utility model, any simple deformation, amendment or other those skilled in the art can not spend the equivalent replacement of creative work to each fall within protection domain of the present utility model.
Claims (2)
1. the process system for organic exhaust gas, it is characterised in that: include eddy flow wash mill, steam-water separator and low-temperature plasma organic waste gas treatment device,
Described eddy flow wash mill includes a tank body, the top of tank body is provided with gas outlet, alternate successively from bottom to up in the inside of tank body is provided with dividing plate, gas distributor, the first spiral board, the first spray equipment, the second spiral board, the second spray equipment, the 3rd spiral board and the 3rd spray equipment; Described dividing plate leaves a scupper, the tank skin below dividing plate is provided with one and is recycled into the mouth of a river, be recycled into the mouth of a river and be connected with the first spray equipment, the second spray equipment and the 3rd spray equipment respectively by pipeline; Described first spiral board, the second spiral board and the 3rd spiral board are coaxially fixed on axle, and one end of axle is connected with the motor on tank body top; Tank skin between dividing plate and gas distributor is provided with air inlet;
The gas outlet of eddy flow wash mill is connected with the air inlet of steam-water separator by pipeline, the gas outlet of steam-water separator is connected by the air inlet of pipeline with low-temperature plasma organic waste gas treatment device, and is provided with centrifugal blower on the pipeline that is connected of the air inlet in the gas outlet of steam-water separator with low-temperature plasma organic waste gas treatment device.
2. a kind of process system for organic exhaust gas according to claim 1, it is characterised in that: steam-water separator is provided with drain valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520984840.6U CN205287960U (en) | 2015-12-01 | 2015-12-01 | Processing system to organic waste gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520984840.6U CN205287960U (en) | 2015-12-01 | 2015-12-01 | Processing system to organic waste gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205287960U true CN205287960U (en) | 2016-06-08 |
Family
ID=56436402
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520984840.6U Expired - Fee Related CN205287960U (en) | 2015-12-01 | 2015-12-01 | Processing system to organic waste gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205287960U (en) |
-
2015
- 2015-12-01 CN CN201520984840.6U patent/CN205287960U/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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160608 Termination date: 20161201 |