CN204962792U - Chemical industry reaction system - Google Patents
Chemical industry reaction system Download PDFInfo
- Publication number
- CN204962792U CN204962792U CN201520714713.4U CN201520714713U CN204962792U CN 204962792 U CN204962792 U CN 204962792U CN 201520714713 U CN201520714713 U CN 201520714713U CN 204962792 U CN204962792 U CN 204962792U
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- China
- Prior art keywords
- heat exchanger
- rear side
- conduction oil
- air
- import
- Prior art date
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- Expired - Fee Related
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Chimneys And Flues (AREA)
Abstract
The utility model discloses a chemical industry reaction system, including burning burning furnace, the conduction oil heat exchanger, air heat exchanger, water chiller, draught fan and chimney, it includes the waste water import to burn burning furnace, the import of high concentration waste gas, natural gas import and conduction oil import, the burning furnace rear side is being burnt in the conduction oil setting, it is provided with a conduction oil export and conduction oil import, air heat exchanger sets up the rear side at the conduction oil heat exchanger, it is provided with a waste heat exhaust outlet and low concentration waste gas entry, water chiller sets up at the air heat exchanger rear side, it is provided with a hot water import and a cooling water inlet, the draught fan sets up water chiller at the rear side, the chimney sets up at the draught fan rear side. High temperature burnt in mill's combustion gas, waste liquid were burnt burning furnace by the introduction for the organic matter is the after -flame completely, reaches effect nontoxic, dustless, smokeless, harmless, odorless complete combustion, conduction oil and hot -blast recovery, energy saving, pollution -free, the environmental protection of accomplishing to exhaust, safe principle.
Description
Technical field
The utility model relates to a kind of chemical reaction system, belongs to field of chemical equipment.
Background technology
Organic exhaust gas waste liquid is as the major pollutants of chemical industry; just can to environment if these pollutant process are bad; be contrary to the aim of modern environment protection, so thorough burning, environmental protection treatment for him are very important, the burning reaction system of an environmental protection organic exhaust gas waste liquid is also very important.
Summary of the invention
For solving the problem, the utility model proposes a kind of chemical reaction system.
A kind of chemical reaction system, comprise incinerator, heat-condutive oil heat exchanger, air heat exchanger, water cooler, air-introduced machine and chimney, described incinerator comprises waste water inlet, high-concentration waste gas import, Imported gas and heat conductive oil inlet, described conduction oil is arranged on rear side of incinerator, it is provided with a conduction oil outlet and heat conductive oil inlet, described air heat exchanger is arranged on the rear side of heat-condutive oil heat exchanger, it is provided with a waste heat waste gas outlet and low concentration gas entrance, described water cooler is arranged on rear side of air heat exchanger, it is provided with a hot water inlet and a cooling water inlet, described air-introduced machine is arranged on water cooler at rear side, described chimney is arranged on rear side of air-introduced machine.
Further, described incinerator, heat-condutive oil heat exchanger, air heat exchanger, water cooler, be interconnected by pipeline between air-introduced machine and chimney neighbouring device.
Further, the conduction oil of described heat-condutive oil heat exchanger and the waste heat waste gas of air heat exchanger all partly pass into incinerator.
Compared with prior art, it has following beneficial effect to the utility model: chemical reaction system of the present utility model, when coming into operation, in-furnace temperature slowly raises, the waste gas that factory discharges, waste liquid are introduced into high-temp combustion in incinerator, make organic matter be able to complete after-flame, reach
To the effect that nontoxic, dustless, smokeless, harmless, odorless burn completely, waste liquid, waste gas are by heat-condutive oil heat exchanger and air heat exchanger cooling, reclaim hot blast and conduction oil, economize energy, gas up to standard after process is introduced chimney by air-introduced machine and enters air, be vented pollution-free, accomplish the principle of environmental protection, safety.
Accompanying drawing explanation
Fig. 1 is system flow chart of the present utility model.
Detailed description of the invention
Consult the chemical reaction system shown in Fig. 1, comprise incinerator, heat-condutive oil heat exchanger, air heat exchanger, water cooler, air-introduced machine and chimney, described incinerator comprises waste water inlet, high-concentration waste gas import, Imported gas and heat conductive oil inlet, described conduction oil is arranged on rear side of incinerator, it is provided with a conduction oil outlet and heat conductive oil inlet, described air heat exchanger is arranged on the rear side of heat-condutive oil heat exchanger, it is provided with a waste heat waste gas outlet and low concentration gas entrance, described water cooler is arranged on rear side of air heat exchanger, it is provided with a hot water inlet and a cooling water inlet, described air-introduced machine is arranged on water cooler at rear side, described chimney is arranged on rear side of air-introduced machine.
Described incinerator, heat-condutive oil heat exchanger, air heat exchanger, water cooler, to be interconnected by pipeline between air-introduced machine and chimney neighbouring device.
The conduction oil of described heat-condutive oil heat exchanger and the waste heat waste gas of air heat exchanger all part pass into incinerator.
The utility model compared with prior art, it has following beneficial effect: chemical reaction system of the present utility model, when coming into operation, in-furnace temperature slowly raises, the waste gas that factory discharges, waste liquid is introduced into high-temp combustion in incinerator, organic matter is made to be able to complete after-flame, reach nontoxic, dustless, smokelessly, harmless, the effect that odorless burns completely, waste liquid, waste gas is by heat-condutive oil heat exchanger and air heat exchanger cooling, reclaim hot blast and conduction oil, economize energy, gas up to standard after process is introduced chimney by air-introduced machine and enters air, be vented pollution-free, accomplish environmental protection, the principle of safety.
Embodiment recited above is only be described preferred embodiment of the present utility model, not limits design of the present utility model and scope.Under the prerequisite not departing from the utility model design concept; the various modification that this area ordinary person makes the technical solution of the utility model and improvement; protection domain of the present utility model all should be dropped into; the technology contents of the utility model request protection, all records in detail in the claims.
Claims (3)
1. a chemical reaction system, it is characterized in that: comprise incinerator, heat-condutive oil heat exchanger, air heat exchanger, water cooler, air-introduced machine and chimney, described incinerator comprises waste water inlet, high-concentration waste gas import, Imported gas and heat conductive oil inlet, described conduction oil is arranged on rear side of incinerator, it is provided with a conduction oil outlet and heat conductive oil inlet, described air heat exchanger is arranged on the rear side of heat-condutive oil heat exchanger, it is provided with a waste heat waste gas outlet and low concentration gas entrance, described water cooler is arranged on rear side of air heat exchanger, it is provided with a hot water inlet and a cooling water inlet, described air-introduced machine is arranging water cooler at rear side, described chimney is arranged on rear side of air-introduced machine.
2. chemical reaction system according to claim 1, is characterized in that: described incinerator, heat-condutive oil heat exchanger, air heat exchanger, water cooler, be interconnected by pipeline between air-introduced machine and chimney neighbouring device.
3. chemical reaction system according to claim 1, is characterized in that: the conduction oil of described heat-condutive oil heat exchanger and the waste heat waste gas of air heat exchanger all part pass into incinerator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520714713.4U CN204962792U (en) | 2015-09-15 | 2015-09-15 | Chemical industry reaction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520714713.4U CN204962792U (en) | 2015-09-15 | 2015-09-15 | Chemical industry reaction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204962792U true CN204962792U (en) | 2016-01-13 |
Family
ID=55057856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520714713.4U Expired - Fee Related CN204962792U (en) | 2015-09-15 | 2015-09-15 | Chemical industry reaction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204962792U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106016305A (en) * | 2016-05-16 | 2016-10-12 | 南京大学盐城环保技术与工程研究院 | Method for removing organic waste gas containing waste gas low in spontaneous ignition point |
| CN107062272A (en) * | 2017-05-06 | 2017-08-18 | 江西德运实业有限责任公司 | Solid state fermentation, recuperation of heat and the internal heat cleaning system of glue production |
| CN108800169A (en) * | 2018-07-06 | 2018-11-13 | 苏州克兰茨环境科技有限公司 | Liquid waste incineration processing unit |
-
2015
- 2015-09-15 CN CN201520714713.4U patent/CN204962792U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106016305A (en) * | 2016-05-16 | 2016-10-12 | 南京大学盐城环保技术与工程研究院 | Method for removing organic waste gas containing waste gas low in spontaneous ignition point |
| CN106016305B (en) * | 2016-05-16 | 2018-12-25 | 南京大学盐城环保技术与工程研究院 | A method of removal contains low self-ignition point organic exhaust gas |
| CN107062272A (en) * | 2017-05-06 | 2017-08-18 | 江西德运实业有限责任公司 | Solid state fermentation, recuperation of heat and the internal heat cleaning system of glue production |
| CN108800169A (en) * | 2018-07-06 | 2018-11-13 | 苏州克兰茨环境科技有限公司 | Liquid waste incineration processing unit |
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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: 20160113 Termination date: 20170915 |