CN204901784U - Drying chamber waste gas burns burning furnace - Google Patents
Drying chamber waste gas burns burning furnace Download PDFInfo
- Publication number
- CN204901784U CN204901784U CN201520469715.1U CN201520469715U CN204901784U CN 204901784 U CN204901784 U CN 204901784U CN 201520469715 U CN201520469715 U CN 201520469715U CN 204901784 U CN204901784 U CN 204901784U
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- Prior art keywords
- heat exchanger
- preheater
- exchanger tube
- burning room
- heat
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Abstract
The utility model discloses a drying chamber waste gas burns burning furnace, pre -heater install in incineration chamber's outside, and the heat exchanger is installed inside the basin, and the pre -heater is inside to be provided with the voltage -sharing room and to set up at the indoor heat exchange tube of voltage -sharing, and the import and the incineration chamber of heat exchange tube are connected, and the export of heat exchange tube is passed through the valve and is connected with incineration chamber and heat exchanger, the export conduct of voltage -sharing room the export of pre -heater is connected with incineration chamber's import, incineration chamber passes through the high temperature valve and is connected with the heat exchanger, is provided with the heat exchange tube that turns back in the heat exchanger, and the gaseous emission pipe is installed to the end of the heat exchange tube that turns back. The utility model discloses the utilization is fired the heat that burning furnace produced and is heated waste gas, has reduced the energy consumption under the circumstances of guaranteeing preheating effect, can can also be added the water in the hot water tank by abundant decomposition through the waste gas that preheats, and heat utilization rate is high.
Description
Technical field
The utility model belongs to waste gas treatment equipment field, particularly relates to a kind of drying room waste gases incinerator.
Background technology
Considerable industrial production all can produce waste gas, waste gas produces huge harm to human body, pollute air, therefore discharge is just allowed after needing that exhaust-gas treatment is become innocuous gas, considerable waste gas is the organic compound of gaseous state, adopt burning process be the most general, effect is better, the waste gas treatment process that cost is minimum.Burning process can produce a large amount of heats while process waste gas, burned waste gas equipment all can arrange the device of some heat energy recycle, burned waste gas equipment heat energy recycle device common be at present by burn after high-temperature gas by a tank, utilize heating water to reclaim heat energy, the maximum shortcoming of this recovery method is that heat energy recycle rate is not high.The waste gas of part burned waste gas treating apparatus directly enters Burning Room without preheating, the waste gas that large amount temperature is lower enters Burning Room and Burning Room temperature can be caused too low, burned waste gas process is insufficient, and most of burned waste gas treating apparatus separately adds preheating device, energy consumption is high, investment is large, complex structure.
Utility model content
The purpose of this utility model is to provide a kind of drying room waste gases incinerator, is intended to solve the problem that existing burned waste gas treating apparatus heat energy recycle rate is low, burned waste gas process is insufficient, energy consumption is high.
The utility model is achieved in that a kind of drying room waste gases incinerator comprises preheater, Burning Room, heat exchanger, tank;
Described preheater is arranged on the outside of described Burning Room, the end of described preheater is provided with exhaust gas inlet, preheater is connected with described Burning Room by this exhaust gas inlet, be provided with combustion air compensator in the air inlet position of described Burning Room, it is inner that described heat exchanger is arranged on described tank;
Described preheater inside is provided with equal pressure chamber and is arranged on the heat exchanger tube in equal pressure chamber, air blast and oxygen conten analyser that promising described equal pressure chamber provides wind regime are installed in the air inlet position of described preheater, this oxygen conten analyser is connected with described combustion air compensator, the import of described heat exchanger tube is connected with described Burning Room, the outlet of heat exchanger tube is connected with Burning Room and heat exchanger by valve, the outlet of described equal pressure chamber as described preheater outlet and be connected with the import of described Burning Room;
Described Burning Room is connected with described heat exchanger by high temperature valve, is provided with the heat exchanger tube that turns back in described heat exchanger, and the end of this heat exchanger tube that turns back is provided with gas discharge pipe.
Further, the connector of described heat exchanger tube and heat exchanger is heat exchanger low-temperature inlet, be provided with the low-temperature outlet be connected with described low-temperature inlet on heat exchangers, described Burning Room and the connector of heat exchanger are heat exchanger high temperature inlet, be provided with the hot outlet be connected with described high temperature inlet on heat exchangers, described hot outlet is connected with described gas discharge pipe with described low-temperature outlet.
Further, described heat exchanger tube and described Burning Room closed communication, described heat exchanger tube is inner to be sealed mutually with outside.
Further, between the heat exchanger tube of described preheater inside, choke net is installed.
Further, described heat exchange pipe external surface is provided with ceramic heat layer.
The heat that the utility model utilizes combustion furnace to produce heats waste gas, and decrease energy consumption when ensureing pre-heat effect, the waste gas through preheating can be decomposed fully, and the water in all right heating water tank, heat utilization rate is high.
Accompanying drawing explanation
Fig. 1 is the structural representation of the drying room waste gases incinerator that the utility model embodiment provides;
In figure: 1, preheater; 1-1, all pressure chamber; 1-2, heat exchanger tube; 2, Burning Room; 3, heat exchanger; 4, tank.
Detailed description of the invention
For utility model content of the present utility model, Characteristic can be understood further, hereby exemplify following examples, and coordinate accompanying drawing to be described in detail as follows.
As shown in Figure 1, the utility model is achieved in that a kind of drying room waste gases incinerator comprises preheater 1, Burning Room 2, heat exchanger 3, tank 4;
Described preheater 1 is arranged on the outside of described Burning Room 2, the end of described preheater 1 is provided with exhaust gas inlet, preheater 1 is connected with described Burning Room 2 by this exhaust gas inlet, be provided with combustion air compensator in the air inlet position of described Burning Room 2, it is inner that described heat exchanger 3 is arranged on described tank 4;
Described preheater 1 inside is provided with equal pressure chamber 1-1 and is arranged on the heat exchanger tube 1-2 in equal pressure chamber 1-1, air blast and oxygen conten analyser that promising described equal pressure chamber 1-1 provides wind regime are installed in the air inlet position of described preheater 1, this oxygen conten analyser is connected with described combustion air compensator, the import of described heat exchanger tube 1-2 is connected with described Burning Room 2, the outlet of heat exchanger tube 1-2 is connected with Burning Room 2 and heat exchanger 3 by valve, the outlet of described equal pressure chamber 1-1 as described preheater 1 outlet and be connected with the import of described Burning Room 2;
Described Burning Room 2 is connected with described heat exchanger 3 by high temperature valve, and be provided with the heat exchanger tube that turns back in described heat exchanger 3, the end of this heat exchanger tube that turns back is provided with gas discharge pipe.
Further, the connector of described heat exchanger tube 1-2 and heat exchanger 3 is heat exchanger low-temperature inlet, heat exchanger 3 is provided with the low-temperature outlet be connected with described low-temperature inlet, described Burning Room 2 is heat exchanger high temperature inlet with the connector of heat exchanger 3, heat exchanger 3 is provided with the hot outlet be connected with described high temperature inlet, and described hot outlet is connected with described gas discharge pipe with described low-temperature outlet.
Further, described heat exchanger tube 1-2 and described Burning Room 2 closed communication, described heat exchanger tube 1-2 is inner to be sealed mutually with outside.
Further, between the heat exchanger tube 1-2 of described preheater 1 inside, choke net is installed.
Further, described heat exchanger tube 1-2 outer surface is provided with ceramic heat layer.
Waste gas enters preheater 1 by the exhaust gas inlet at preheater 1 place, the import of heat exchanger tube 1-2 is connected with described Burning Room 2, in Burning Room 2, gas combustion produces heat energy, and by heat exchanger tube 1-2, preheating is carried out to the waste gas entering preheater 1, waste gas after preheating enters Burning Room burning for follow-up heating by the exhaust gases, the outlet of heat exchanger tube 1-2 is connected with heat exchanger 3 by valve, Burning Room 2 is connected with described heat exchanger 3 by high temperature valve, low-temperature heat can be carried out to the water in tank 4 when only opening the valve connecting heat exchanger tube 1-2, when opening the valve connecting Burning Room 2, high-temperature heating can be carried out to the water in tank 4.
The heat that the utility model utilizes combustion furnace to produce heats waste gas, and decrease energy consumption when ensureing pre-heat effect, the waste gas through preheating can be decomposed fully, and the water in all right heating water tank, heat utilization rate is high.
The above is only to preferred embodiment of the present utility model, not any pro forma restriction is done to the utility model, every according to technical spirit of the present utility model to any simple modification made for any of the above embodiments, equivalent variations and modification, all belong in the scope of technical solutions of the utility model.
Claims (5)
1. a drying room waste gases incinerator, is characterized in that, described drying room waste gases incinerator comprises preheater, Burning Room, heat exchanger, tank;
Described preheater is arranged on the outside of described Burning Room, the end of described preheater is provided with exhaust gas inlet, preheater is connected with described Burning Room by this exhaust gas inlet, be provided with combustion air compensator in the air inlet position of described Burning Room, it is inner that described heat exchanger is arranged on described tank;
Described preheater inside is provided with equal pressure chamber and is arranged on the heat exchanger tube in equal pressure chamber, air blast and oxygen conten analyser that promising described equal pressure chamber provides wind regime are installed in the air inlet position of described preheater, this oxygen conten analyser is connected with described combustion air compensator, the import of described heat exchanger tube is connected with described Burning Room, the outlet of heat exchanger tube is connected with Burning Room and heat exchanger by valve, the outlet of described equal pressure chamber as described preheater outlet and be connected with the import of described Burning Room;
Described Burning Room is connected with described heat exchanger by high temperature valve, is provided with the heat exchanger tube that turns back in described heat exchanger, and the end of this heat exchanger tube that turns back is provided with gas discharge pipe.
2. drying room waste gases incinerator as claimed in claim 1, it is characterized in that, the connector of described heat exchanger tube and heat exchanger is heat exchanger low-temperature inlet, be provided with the low-temperature outlet be connected with described low-temperature inlet on heat exchangers, described Burning Room and the connector of heat exchanger are heat exchanger high temperature inlet, be provided with the hot outlet be connected with described high temperature inlet on heat exchangers, described hot outlet is connected with described gas discharge pipe with described low-temperature outlet.
3. drying room waste gases incinerator as claimed in claim 1, is characterized in that, described heat exchanger tube and described Burning Room closed communication, and described heat exchanger tube is inner to be sealed mutually with outside.
4. drying room waste gases incinerator as claimed in claim 1, is characterized in that, be provided with choke net between the heat exchanger tube of described preheater inside.
5. drying room waste gases incinerator as claimed in claim 1, it is characterized in that, described heat exchange pipe external surface is provided with ceramic heat layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520469715.1U CN204901784U (en) | 2015-06-30 | 2015-06-30 | Drying chamber waste gas burns burning furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520469715.1U CN204901784U (en) | 2015-06-30 | 2015-06-30 | Drying chamber waste gas burns burning furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204901784U true CN204901784U (en) | 2015-12-23 |
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ID=54923956
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520469715.1U Expired - Fee Related CN204901784U (en) | 2015-06-30 | 2015-06-30 | Drying chamber waste gas burns burning furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204901784U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731446A (en) * | 2017-02-22 | 2017-05-31 | 郭满强 | One kind is for processing VOC gas pyrolysis ovens |
| CN107305014A (en) * | 2016-04-21 | 2017-10-31 | 沈阳铝镁科技有限公司 | A kind of baking flue gas purifies incinerator |
| CN108031633A (en) * | 2018-01-09 | 2018-05-15 | 天津市赛洋工业炉有限公司 | A kind of nuisanceless japanning drying equipment and its method |
-
2015
- 2015-06-30 CN CN201520469715.1U patent/CN204901784U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107305014A (en) * | 2016-04-21 | 2017-10-31 | 沈阳铝镁科技有限公司 | A kind of baking flue gas purifies incinerator |
| CN106731446A (en) * | 2017-02-22 | 2017-05-31 | 郭满强 | One kind is for processing VOC gas pyrolysis ovens |
| CN108031633A (en) * | 2018-01-09 | 2018-05-15 | 天津市赛洋工业炉有限公司 | A kind of nuisanceless japanning drying equipment and its method |
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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 |
Granted publication date: 20151223 Termination date: 20170630 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |