CN104190232A - Vulcanization accelerator M tail gas treatment device - Google Patents
Vulcanization accelerator M tail gas treatment device Download PDFInfo
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- CN104190232A CN104190232A CN201410454166.0A CN201410454166A CN104190232A CN 104190232 A CN104190232 A CN 104190232A CN 201410454166 A CN201410454166 A CN 201410454166A CN 104190232 A CN104190232 A CN 104190232A
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Abstract
The invention relates to a vulcanization accelerator M tail gas treatment device which comprises a high-pressure reaction kettle, wherein the high-pressure reaction kettle, a first extraction tank and a second extraction tank are connected in sequence by virtue of pipelines; the second extraction tank is respectively connected with a distillation kettle and an air-blowing oxide kettle by virtue of pipelines; the upper part of the high-pressure reaction kettle is connected with a first alkali absorption tank by virtue of a hydrogen sulfide pipeline; the first alkali absorption tank is connected with a second alkali absorption tank by virtue of a pipeline; the second alkali absorption tank is connected with a third alkali absorption tank by virtue of a pipeline; the third alkali absorption tank is connected with a water storage tank by virtue of a first pipeline; a first water storage tank is connected with a second water storage tank by virtue of a pipeline; the second water storage tank is connected with a combustion stove by virtue of a pipeline; the combustion stove is connected with a desulfurization and dust collection device which is connected with a chimney; a pump is arranged on the first pipeline and is connected with the second water storage tank. According to the vulcanization accelerator M tail gas treatment device, the emission of hydrogen sulfide gas is reduced; air pollution is avoided; the standard exhaust emission is realized, the energy conservation and consumption reduction of fuels are also realized and the fuel cost is reduced.
Description
Technical field
The present invention relates to a kind of accelerator M exhaust gas processing device.
Background technology
In chemical rubber auxiliary agent-accelerator M production process, produce a large amount of tail gas, the composition of tail gas is mainly hydrogen sulfide.In prior art, normally claus oven burning, or after adopting waste gas directly to react by reburner, form liquid gas separated, and liquid is Molten sulphur, gas is directly discharge.In accelerator M production process, the hydrogen sulfide gas producing in autoclave, does not absorb completely yet, is thrown in air, causes air pollution.In residual gas discharged air, cause severe contamination, and easily form acid rain, plant, animal are caused and had a strong impact on.Because the hydrogen sulfide tail gas rate of recovery is lower, cause serious environmental pollution, and a part of enterprise is because exhaust emissions is not up to standard and halted, to producer, has brought economic loss.
Summary of the invention
The object of this invention is to provide a kind of accelerator M exhaust gas processing device.Reduce hydrogen sulfide gas discharge, avoid air pollution, not only meet environmental protection waste gas qualified discharge but also realize the energy-saving and cost-reducing of fuel, reduce fuel cost.
Accelerator M exhaust gas processing device of the present invention, comprises autoclave, and autoclave, the first extractor, the second extractor connect successively by pipeline, and the second extractor is connected with air blast stills for air blowing with distillation still respectively by pipeline; Autoclave top is connected with the first alkali tourie by hydrogen sulfide pipeline, the first alkali tourie is connected with the second alkali tourie by pipeline, the second alkali tourie is connected with the 3rd alkali tourie by pipeline, the 3rd alkali tourie is connected with water tank by the first pipeline, the first water tank is connected with the second water tank by pipeline, the second water tank is connected with combustion furnace by pipeline, combustion furnace is connected with desulfation dust-extraction device, desulfation dust-extraction device is connected with chimney, this pump on the first pipeline, pump is connected with the second water tank by pipeline.
On the pipeline between pump and the first water tank, the second Pressure gauge and check-valves are set.
On the pipeline between pump and the 3rd alkali tourie, the first Pressure gauge and air control valve are set.
On combustion furnace, configure blower fan.
Adopt pump to suck ability of swimming air cleaner, the cigarette ash of burning is precipitated to meet the requirement of environmental protection through water filtration.
The first ability of swimming air cleaner and the second ability of swimming air cleaner adopt circulating water pipe, and water circulation use, reaches hot body cooling effect, prevents from firing.
It is gap discharge that autoclave produces hydrogen sulfide, and discharge temperature is 200 ℃, and drain time is 1 hour, and pressure is 1 ?1.5MP.
The hydrogen sulfide gas that autoclave produces enters the first alkali tourie, the second alkali tourie, the 3rd alkali tourie successively, by vavuum pump, input the first ability of swimming air cleaner again and the second ability of swimming air cleaner carries out filtering-depositing, at 30 ℃ of temperature, vacuum pressure 0.7 ?0.8MPa send into combustion furnace, mate and burn with blower fan, in combustion furnace temperature 600 ?800 ℃, after burning, through desulfation dust-extraction device, carry out desulfurization and dedusting again, finally by chimney, get rid of.
Combustion furnace is that stalk heat-conducting oil furnace burns in company, because production technology needs conduction-oil warming, by burning, reduces stalk consumption, reduces environmental pollution.
Compared with prior art, the present invention has following beneficial effect:
Accelerator M exhaust gas processing device of the present invention, has reduced hydrogen sulfide gas discharge, has avoided air pollution, not only meets environmental protection waste gas qualified discharge but also realize the energy-saving and cost-reducing of fuel, has reduced fuel cost.
Accompanying drawing explanation
Fig. 1 structural representation of the present invention;
In figure, 1 ?1, hydrogen sulfide pipeline, 1 ?the 2, first pipeline, the 2, second alkali tourie, 3, the first Pressure gauge, 4, air control valve, the 5, second Pressure gauge, 6, check-valves, 7, the first ability of swimming air cleaner, the 8, second ability of swimming air cleaner, 9, combustion furnace, 10, pump, 11, the 3rd alkali tourie, the 12, first alkali tourie, 13, desulfation dust-extraction device, 14, chimney, 15, distillation still, 16, air blast stills for air blowing, 17, the second extractor, the 18, first extractor, 19, autoclave.
The specific embodiment
Below in conjunction with embodiment, the present invention will be further described.
Embodiment
As Fig. 1, accelerator M exhaust gas processing device described in the present embodiment, comprise autoclave 19, autoclave 19, the first extractor 18, the second extractor 17 connect successively by pipeline, and the second extractor 17 is connected with air blast stills for air blowing 16 with distillation still 15 respectively by pipeline, autoclave 19 tops are connected with the first alkali tourie 12 by hydrogen sulfide pipeline 1, the first alkali tourie 12 is connected with the second alkali tourie 2 by pipeline, the second alkali tourie 2 is connected with the 3rd alkali tourie 11 by pipeline, the 3rd alkali tourie 11 by the first pipeline 1 ?2 be connected with water tank 7, the first water tank 7 is connected with the second water tank 8 by pipeline, the second water tank 8 is connected with combustion furnace 9 by pipeline, combustion furnace 9 is connected with desulfation dust-extraction device 13, desulfation dust-extraction device 13 is connected with chimney 14, this pump 10 on the first pipeline, pump 10 is connected with the second water tank 8 by pipeline.
On the pipeline between pump 10 and the first water tank 7, the second Pressure gauge 5 and check-valves 6 are set.
On the pipeline between pump 10 and the 3rd alkali tourie 11, the first Pressure gauge 3 and air control valve 4 are set.
Claims (3)
1. an accelerator M exhaust gas processing device, comprise autoclave (19), it is characterized in that, autoclave (19), the first extractor (18), the second extractor (17) connect successively by pipeline, and the second extractor (17) is connected with air blast stills for air blowing (16) with distillation still (15) respectively by pipeline, autoclave (19) top is connected with the first alkali tourie (12) by hydrogen sulfide pipeline (1), the first alkali tourie (12) is connected with the second alkali tourie (2) by pipeline, the second alkali tourie (2) is connected with the 3rd alkali tourie (11) by pipeline, the 3rd alkali tourie (11) is connected with ability of swimming air cleaner (7) by the first pipeline (1-2), the first ability of swimming air cleaner (7) is connected with the second ability of swimming air cleaner (8) by pipeline, the second ability of swimming air cleaner (8) is connected with gas-distributing fan (9) by pipeline, gas-distributing fan (9) is connected with desulfation dust-extraction device (13), desulfation dust-extraction device (13) is connected with chimney (14), this pump (10) on the first pipeline, pump (10) is connected with the second ability of swimming air cleaner (8) by pipeline.
2. accelerator M exhaust gas processing device according to claim 1, is characterized in that, on the pipeline between pump (10) and the first ability of swimming air cleaner (7), the second Pressure gauge (5) and check-valves (6) is set.
3. accelerator M exhaust gas processing device according to claim 1, is characterized in that, on the pipeline between pump (10) and the 3rd alkali tourie (11), the first Pressure gauge (3) and air control valve (4) is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410454166.0A CN104190232A (en) | 2014-09-05 | 2014-09-05 | Vulcanization accelerator M tail gas treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410454166.0A CN104190232A (en) | 2014-09-05 | 2014-09-05 | Vulcanization accelerator M tail gas treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104190232A true CN104190232A (en) | 2014-12-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410454166.0A Pending CN104190232A (en) | 2014-09-05 | 2014-09-05 | Vulcanization accelerator M tail gas treatment device |
Country Status (1)
| Country | Link |
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| CN (1) | CN104190232A (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3974170A (en) * | 1974-08-26 | 1976-08-10 | Monsanto Company | Preparation of 2-mercaptoazoles |
| CN1123277A (en) * | 1995-10-17 | 1996-05-29 | 杨秉德 | New method for refinement of crude 2-mercapto benzothiazole |
| US20050214925A1 (en) * | 2004-03-03 | 2005-09-29 | Chen Jen K | Process for the high recovery efficiency of sulfur from an acid gas stream |
| CN101402615A (en) * | 2008-11-12 | 2009-04-08 | 山东阳谷华泰化工有限公司 | Fine purification method for rubber vulcanization accelerant 2-mercaptobenzothiazole (M) |
| CN102116482A (en) * | 2011-01-30 | 2011-07-06 | 浙江省环境保护科学设计研究院 | System and process for heat power incineration and purification of volatile organic waste gas boiler |
| CN102850292A (en) * | 2011-06-30 | 2013-01-02 | 鹤壁市恒瑞橡塑材料有限公司 | Totally enclosed clean production system for rubber vulcanization accelerator 2-mercaptobenzothiazole |
| CN203628681U (en) * | 2013-12-09 | 2014-06-04 | 浙江环科环境研究院有限公司 | Incineration disposing system of organic exhaust boiler via heating power |
| CN204017658U (en) * | 2014-09-05 | 2014-12-17 | 淄博高汇化工有限公司 | Accelerator M exhaust gas processing device |
-
2014
- 2014-09-05 CN CN201410454166.0A patent/CN104190232A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3974170A (en) * | 1974-08-26 | 1976-08-10 | Monsanto Company | Preparation of 2-mercaptoazoles |
| CN1123277A (en) * | 1995-10-17 | 1996-05-29 | 杨秉德 | New method for refinement of crude 2-mercapto benzothiazole |
| US20050214925A1 (en) * | 2004-03-03 | 2005-09-29 | Chen Jen K | Process for the high recovery efficiency of sulfur from an acid gas stream |
| CN101402615A (en) * | 2008-11-12 | 2009-04-08 | 山东阳谷华泰化工有限公司 | Fine purification method for rubber vulcanization accelerant 2-mercaptobenzothiazole (M) |
| CN102116482A (en) * | 2011-01-30 | 2011-07-06 | 浙江省环境保护科学设计研究院 | System and process for heat power incineration and purification of volatile organic waste gas boiler |
| CN102850292A (en) * | 2011-06-30 | 2013-01-02 | 鹤壁市恒瑞橡塑材料有限公司 | Totally enclosed clean production system for rubber vulcanization accelerator 2-mercaptobenzothiazole |
| CN203628681U (en) * | 2013-12-09 | 2014-06-04 | 浙江环科环境研究院有限公司 | Incineration disposing system of organic exhaust boiler via heating power |
| CN204017658U (en) * | 2014-09-05 | 2014-12-17 | 淄博高汇化工有限公司 | Accelerator M exhaust gas processing device |
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Application publication date: 20141210 |