CN203687085U - Air pre-heater for heat storage type waste gas treatment equipment - Google Patents
Air pre-heater for heat storage type waste gas treatment equipment Download PDFInfo
- Publication number
- CN203687085U CN203687085U CN201420037790.6U CN201420037790U CN203687085U CN 203687085 U CN203687085 U CN 203687085U CN 201420037790 U CN201420037790 U CN 201420037790U CN 203687085 U CN203687085 U CN 203687085U
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- China
- Prior art keywords
- combustion
- air preheater
- gas treatment
- heater
- treatment equipment
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- 239000002912 waste gas Substances 0.000 title abstract description 5
- 238000005338 heat storage Methods 0.000 title abstract 3
- 239000007789 gas Substances 0.000 claims abstract description 35
- 238000002485 combustion reaction Methods 0.000 claims abstract description 29
- 239000002918 waste heat Substances 0.000 claims abstract description 11
- 238000009825 accumulation Methods 0.000 claims description 12
- 238000004146 energy storage Methods 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 4
- 238000010276 construction Methods 0.000 abstract description 2
- 239000010815 organic waste Substances 0.000 abstract 1
- 238000000354 decomposition reaction Methods 0.000 description 3
- 239000003925 fat Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
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Classifications
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Abstract
The utility model relates to the technical field of waste gas treatment, in particular to an air pre-heater for heat storage type waste gas treatment equipment. The air pre-heater comprises a furnace, wherein a periodical circulation heat absorbing and releasing device formed by multiple heat storage beds is arranged inside the furnace. The air pre-heater is characterized in that an open end of the furnace is connected with the inlet end of a waste heat furnace, the outlet end of the waste heat furnace is connected with the first inlet end of a combustion air pre-heater, the first outlet end of the combustion air pre-heater is connected to an inlet of a chimney through a first pipeline to form a first air path, the second inlet end of the combustion air pre-heater is connected with a combustion fan, and the second outlet end of the combustion air pre-heater is connected to the other open end of the furnace to form a second air path. The air pre-heater has the advantages of being novel and simple in structure, convenient to use, capable of improving the energy-saving performance of an RTO system greatly, small in occupied area, and capable of reducing the capital construction cost of organic waste gas treatment greatly, improving the working efficiency of the system and reducing energy loss.
Description
[technical field]
The utility model relates to technical field of waste gas treatment, specifically a kind of air preheater for heat accumulation type exhaust-gas treatment equipment.
[background technology]
RTO(Regenerative Thermal Oxidizer), it is heat accumulating type oxidation furnace, to utilize the principle of organic exhaust gas pyrolytic Cheng Shui and carbon dioxide to process the usual means of organic exhaust gas, compared with traditional catalytic combustion, direct-fired thermal oxidation furnace (TO), because of its have the thermal efficiency high (>=95%), operating cost low, can process large-wind-volume low-concentration waste gas, concentration and also can carry out secondary waste heat recovery when slightly high, greatly reduce the advantages such as production and operation cost, the exhaust-gas treatment that is widely used field.
RTO is generally made up of a burner hearth and two or more energy storage bed, here we only design two energy storage beds, two energy storage beds can carry out periodic heat absorption and release, organic exhaust gas enters burner hearth and carries out combustion decomposition after energy storage bed, because organic exhaust gas completing combustion decomposition need to reach 800 ℃, therefore will reach organic exhaust gas decomposition temperature, burner hearth must be preheated to 800 ℃.If the air of directly using normal temperature to burner hearth preheating, can be wasted a large amount of gas energies as combustion air all the time.
[summary of the invention]
The purpose of this utility model is exactly will solve above-mentioned deficiency and a kind of heat accumulation type exhaust-gas treatment equipment is provided, and obtains further energy-conservation.
Design for achieving the above object a kind of air preheater for heat accumulation type exhaust-gas treatment equipment, described heat accumulation type exhaust-gas treatment equipment comprises burner hearth, described burner hearth inside is provided with the loop cycle being made up of some energy storage beds and inhales heat-releasing device, the perforate one end that it is characterized in that described burner hearth connects waste-heat oven arrival end, the described waste-heat oven port of export connects combustion-supporting air preheater the first arrival end, and described combustion-supporting air preheater first port of export is connected to chimney import by the first pipeline and forms the first gas circuit; Described combustion-supporting air preheater the second arrival end connects combustion fan, and described combustion-supporting air preheater second port of export is connected to another perforate end of burner hearth by second pipe and forms the second gas circuit.
Between described combustion fan and combustion-supporting air preheater the second arrival end, be provided with damper A; Described combustion fan is interconnected by an arm and second pipe, and described arm is provided with damper B, and the temperature that the aperture of damper needs according to system is determined.
Described the first pipeline is provided with and mixes wind damper, and described second pipe is provided with deep fat and adds hot air disperser.
The first gas circuit and the second gas circuit are cruciform shape in combustion-supporting air preheater place, and intersection forms convection current.
Combustion air in described combustion fan adopts hot-air or normal temperature air.
The beneficial effects of the utility model, novel structure, simple, easy to use, energy-efficient performance and the floor space of greatly having improved RTO system are little, in addition, greatly reduce VOCs treatment capital construction cost, improve system works efficiency, further reduced energy loss.
[accompanying drawing explanation]
Fig. 1 is structural principle schematic diagram of the present utility model;
In figure: 1 for system fan, 2 is for lift valve A, 3 is for lift valve B, 4 is for energy storage bed A, 5 is for energy storage bed B, 6 is for burner hearth, 7 waste-heat ovens, 8 combustion fans, 9 damper A, 10 damper B, 11 are for combustion air air preheater, 12 mixes wind damper, 13 deep fats add hot air disperser.
[specific embodiment]
Below in conjunction with drawings and Examples, the technical solution of the utility model is described further, the structure of this device is very clearly concerning this professional people.
Air preheater as shown in Figure 1, original heat accumulation type exhaust-gas treatment equipment comprises burner hearth, described burner hearth inside is provided with the loop cycle being made up of some energy storage beds and inhales heat-releasing device, the outside corresponding every suit energy storage bed of described burner hearth, respectively by air intake branch and go out first port of export and the second entrance point that gas branch pipe connects some lift valves, the first entrance point of described some lift valves connects respectively the inlet manifold at production line blower fan place by some air intake branches, second port of export of described some lift valves is interconnected to chimney import by going out gas branch pipe.
In the Equipment Foundations of said structure, further improve;
First, by burner hearth 6 left side perforates, this one end, hole is connected to waste-heat oven 7 arrival ends, and waste-heat oven 7 ports of export connect first arrival end in combustion-supporting air preheater 11 left sides, and first port of export on described combustion-supporting air preheater 11 right sides is connected to chimney import by the first pipeline and forms the first gas circuit;
Secondly, the second arrival end of combustion-supporting air preheater 11 front sides is connected to combustion fan 8, another perforate end that second port of export of described combustion-supporting air preheater 11 rear sides is connected to burner hearth 6 rear sides by second pipe forms the second gas circuit.Make the first gas circuit and the second gas circuit be cruciform shape in combustion-supporting air preheater 11 places.
Finally, process adjusting device.Specifically, between combustion fan 8 and combustion-supporting air preheater 11 second arrival ends, be provided with damper A9; Combustion fan 8 is interconnected by an arm and second pipe, and described arm is provided with damper B10, and the temperature that the aperture of damper needs according to system is determined.The first pipeline is provided with and mixes wind damper 12, and second pipe is provided with deep fat and adds hot air disperser 13.Combustion air in described combustion fan 8 adopts hot-air or normal temperature air.
The order that the utility model switches is: the unnecessary high-temperature gas after decomposing in burner hearth passes into combustion-supporting air preheater through waste-heat oven, discharges atmosphere through chimney; Meanwhile, by combustion fan, normal temperature air is blown into combustion-supporting air preheater, by convection current, normal temperature air is heated.Combustion fan has the airduct of connection and a damper 9 to combustion-supporting air preheater porch; The combustion fan port of export has the airduct of connection and a damper 10 with the combustion-supporting air preheater port of export, the temperature that the aperture of two dampers can need according to system is determined, utilize hot-air to substitute normal temperature air as combustion air, greatly save the consumption of natural gas, thereby played energy-conservation effect.
Claims (5)
1. the air preheater for heat accumulation type exhaust-gas treatment equipment, described heat accumulation type exhaust-gas treatment equipment comprises burner hearth, described burner hearth inside is provided with the loop cycle being made up of some energy storage beds and inhales heat-releasing device, the perforate one end that it is characterized in that described burner hearth connects waste-heat oven arrival end, the described waste-heat oven port of export connects combustion-supporting air preheater the first arrival end, and described combustion-supporting air preheater first port of export is connected to chimney import by the first pipeline and forms the first gas circuit; Described combustion-supporting air preheater the second arrival end connects combustion fan, and described combustion-supporting air preheater second port of export is connected to another perforate end of burner hearth by second pipe and forms the second gas circuit.
2. a kind of air preheater for heat accumulation type exhaust-gas treatment equipment as claimed in claim 1, is characterized in that being provided with damper A between described combustion fan and combustion-supporting air preheater the second arrival end; Described combustion fan is interconnected by an arm and second pipe, and described arm is provided with damper B, and the temperature that the aperture of damper needs according to system is determined.
3. a kind of air preheater for heat accumulation type exhaust-gas treatment equipment as claimed in claim 1, is characterized in that described the first pipeline is provided with mixing wind damper, and described second pipe is provided with deep fat and adds hot air disperser.
4. a kind of air preheater for heat accumulation type exhaust-gas treatment equipment as claimed in claim 1 or 2, is characterized in that described the first gas circuit and the second gas circuit are cruciform shape in combustion-supporting air preheater place, and intersection forms convection current.
5. a kind of air preheater for heat accumulation type exhaust-gas treatment equipment as claimed in claim 3, is characterized in that the combustion air in described combustion fan adopts hot-air or normal temperature air.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420037790.6U CN203687085U (en) | 2014-01-21 | 2014-01-21 | Air pre-heater for heat storage type waste gas treatment equipment |
Applications Claiming Priority (1)
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CN201420037790.6U CN203687085U (en) | 2014-01-21 | 2014-01-21 | Air pre-heater for heat storage type waste gas treatment equipment |
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CN203687085U true CN203687085U (en) | 2014-07-02 |
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CN201420037790.6U Expired - Fee Related CN203687085U (en) | 2014-01-21 | 2014-01-21 | Air pre-heater for heat storage type waste gas treatment equipment |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107726338A (en) * | 2017-10-20 | 2018-02-23 | 江苏百纳环保设备有限公司 | One kind rotation RTO |
-
2014
- 2014-01-21 CN CN201420037790.6U patent/CN203687085U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107726338A (en) * | 2017-10-20 | 2018-02-23 | 江苏百纳环保设备有限公司 | One kind rotation RTO |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20220307 Address after: 201802 room 1515, floor 15, building 1, No. 655, Yinxiang Road, Jiading District, Shanghai Patentee after: Shanghai Yongjiang Environmental Engineering Co.,Ltd. Address before: Room 1207, 1128 Wenhui Road, Songjiang District, Shanghai, 201620 Patentee before: SHANGHAI YONGJIANG ENVIRONMENT PROTECTION RESOURCE TECHNOLOGY Co.,Ltd. |
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TR01 | Transfer of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140702 |
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CF01 | Termination of patent right due to non-payment of annual fee |