CN201171923Y - Oil material cracking evaporating waste gas treatment device - Google Patents
Oil material cracking evaporating waste gas treatment device Download PDFInfo
- Publication number
- CN201171923Y CN201171923Y CNU2008201070425U CN200820107042U CN201171923Y CN 201171923 Y CN201171923 Y CN 201171923Y CN U2008201070425 U CNU2008201070425 U CN U2008201070425U CN 200820107042 U CN200820107042 U CN 200820107042U CN 201171923 Y CN201171923 Y CN 201171923Y
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- gas
- waste
- oil
- processing device
- oiliness
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Abstract
The utility model relates to a processing device for oil waste-gas, in particular to a processing device for waste gas generated by the crack and evaporation of oil materials. The processing device for oil waste-gas comprises a heat-medium boiler, a heat-supplying pipeline, an oil-material evaporating tank, a heat exchanger, an oil-gas pipeline, a condenser, a gas-and-liquid separating tank, a waste-gas pipeline and a waste-gas burner, and a waste-gas purifier is installed on the waste-gas pipeline connected between the gas-and-liquid separating tank and the waste-gas burner. The processing device for oil waste-gas is very suitable for processing various oil waste-gases with complex components needed to be purified and can effectively prolong the cleaning and examining-and-repairing period of a waste-gas circulation system, thus improving the security and the sustainability of the oil waste-gas combustion system; filtrating cloth can be used as the filtrating medium of a filter so that when the filter is blocked, the filtrating cloth can be cleaned to be used again; cheap coke can be used as the charcoal adsorption medium in an adsorption medium tank so that when the coke is under the saturated state by adsorbing solid impurities of oil waste-gas, according to the combustible commonness of the charcoal adsorption medium and the adsorbed substances, the charcoal adsorption medium and the adsorbed substances can be used as the fuel to be combusted so that the environment protection and the energy recycle economy can be achieved.
Description
Technical field:
The utility model relates to the oiliness emission-control equipment, especially a kind of oiliness material cracking evaporation emission-control equipment.
Background technology:
When processing oiliness material, can produce a large amount of oiliness waste gas.This gas determines its component structure according to different masterbatch and different treatment process, and this component structure is very complicated, in the process of circulation, is very easy to become solid state by gaseous state.Traditional oiliness waste gas processing method has: (1) directly is discharged into atmosphere with oiliness waste gas.(2) oiliness waste gas is discharged into the boiler internal combustion simply; Above-mentioned processing defective: (1) will cause the large tracts of land atmosphere pollution if oil gas directly is discharged in the atmosphere, and so that 1 ton of mineral oil evaporation is condensed into example again, the oil gas of generation can pollute the atmosphere of several square kilometres of areas; (2) if oiliness waste gas is discharged into the boiler internal combustion simply, in oiliness waste line and burner, be easy to produce fast the abundant residues solidfied material, in the very short cycle, can cause the waste gas system for the distribution of commodities to be stopped up.
Summary of the invention:
The utility model is intended to solve the described drawback of background technology, can evaporate emission-control equipment and provide a kind of to the oiliness material cracking that waste gas purifies before waste gas burning.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of oiliness material cracking evaporation emission-control equipment, comprise thermophore boiler, heat supply pipeline, oiliness material evaporator, heat exchanger, oil-gas pipeline, condenser, knockout drum, waste line, gas flare, be connected on the waste line of knockout drum and gas flare catalytic converter is housed.
Description of drawings:
Fig. 1 is a structural representation of the present utility model.
Among the figure: thermophore boiler 1, heat supply pipeline 2, oiliness material evaporator 3, heat exchanger 4, oil-gas pipeline 5, condenser 6, knockout drum 7, waste line 8, filter 9, adsorbing medium jar 10, charcoal class adsorbing medium 11, gas flare 12.
The specific embodiment:
Below in conjunction with drawings and Examples the utility model is further specified.
The described oiliness material of present embodiment cracking evaporation emission-control equipment, its thermophore boiler 1 is connected with oiliness material evaporator 3 by heat supply pipeline 2, and thermophore is sent to the interior heat exchanger 4 of oiliness material evaporator 3; This oiliness material evaporator 3 is connected by one section oil-gas pipeline 5 with knockout drum 7, is connected with condenser 6 in the centre of this section oil-gas pipeline 5; On the waste line 8 between this knockout drum 7 and the gas flare 12 catalytic converter is housed.
The described catalytic converter of present embodiment can be a filter 9, also can be adsorbing medium jar 10, can also be filter 9 and the adsorbing medium jar 10 that is serially connected.As shown in Figure 1, such catalytic converter collection filters, is adsorbed in one, and effect is better.
In the described adsorbing medium jar 10 of present embodiment charcoal class adsorbing medium 11 is arranged, this charcoal class adsorbing medium 11 can be coke, charcoal or active carbon.
The operation principle of this device:
Compared with prior art, the utlity model has following advantage:
The utility model is simple in structure, consumables cost is low, and the filter medium of filter 9 can Adopt filter cloth, again usefulness capable of washing during obstruction, the charcoal class absorption in the adsorbing medium tank 10 is situated between Matter 11 can adopt cheap coke, when coke is satisfied the absorption of the solid impurity in the oiliness waste gas And the time, according to the flammable general character of charcoal class adsorbing medium and absorbate, can with its as Fuel burns, and realizes the recycling economy of environmental protection and reusing of energy source with it.
Claims (5)
1, a kind of oiliness material cracking evaporation emission-control equipment, comprise thermophore boiler, heat supply pipeline, oiliness material evaporator, heat exchanger, oil-gas pipeline, condenser, knockout drum, waste line, gas flare, it is characterized in that: be connected on the waste line of knockout drum and gas flare catalytic converter is housed.
2, oiliness material cracking evaporation emission-control equipment according to claim 1 is characterized in that described catalytic converter is a filter.
3, oiliness material cracking evaporation emission-control equipment according to claim 1 is characterized in that described catalytic converter is the adsorbing medium jar.
4, oiliness material cracking evaporation emission-control equipment according to claim 1 is characterized in that described catalytic converter is filter and the adsorbing medium jar that is serially connected.
5, oiliness material cracking evaporation emission-control equipment according to claim 1 is characterized in that charcoal class adsorbing medium is arranged in the described adsorbing medium jar, and this charcoal class adsorbing medium can be coke, charcoal or active carbon.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201070425U CN201171923Y (en) | 2008-04-14 | 2008-04-14 | Oil material cracking evaporating waste gas treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201070425U CN201171923Y (en) | 2008-04-14 | 2008-04-14 | Oil material cracking evaporating waste gas treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201171923Y true CN201171923Y (en) | 2008-12-31 |
Family
ID=40199031
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201070425U Expired - Fee Related CN201171923Y (en) | 2008-04-14 | 2008-04-14 | Oil material cracking evaporating waste gas treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201171923Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101829434A (en) * | 2010-06-11 | 2010-09-15 | 吴国存 | Convective heat exchange fractionation device |
| CN102634665A (en) * | 2012-04-16 | 2012-08-15 | 金川集团有限公司 | Treatment method of waste copper cuttings |
| CN108404591A (en) * | 2018-05-03 | 2018-08-17 | 天津市可帮化工产品有限公司 | The processing unit of chemical emission |
-
2008
- 2008-04-14 CN CNU2008201070425U patent/CN201171923Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101829434A (en) * | 2010-06-11 | 2010-09-15 | 吴国存 | Convective heat exchange fractionation device |
| CN102634665A (en) * | 2012-04-16 | 2012-08-15 | 金川集团有限公司 | Treatment method of waste copper cuttings |
| CN108404591A (en) * | 2018-05-03 | 2018-08-17 | 天津市可帮化工产品有限公司 | The processing unit of chemical emission |
| CN108404591B (en) * | 2018-05-03 | 2023-08-25 | 安徽昊源化工集团有限公司 | Chemical waste gas treatment device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20081231 Termination date: 20110414 |