CN201096352Y - Gas-solid mixing combustion purifying and heat distribution system - Google Patents
Gas-solid mixing combustion purifying and heat distribution system Download PDFInfo
- Publication number
- CN201096352Y CN201096352Y CNU2007201900084U CN200720190008U CN201096352Y CN 201096352 Y CN201096352 Y CN 201096352Y CN U2007201900084 U CNU2007201900084 U CN U2007201900084U CN 200720190008 U CN200720190008 U CN 200720190008U CN 201096352 Y CN201096352 Y CN 201096352Y
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- Prior art keywords
- gas
- incinerator
- combustion
- heat boiler
- heating system
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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
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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- Incineration Of Waste (AREA)
Abstract
The utility model relates to a gas-solid mixed burning purification and heating system, which comprises a combustion chamber, a revolving carbonization furnace, a dust chamber, an incinerator, a burning channel, a waste-heat boiler and a dust catcher, wherein the smoke outlet opening of the combustion chamber is connected with one end of the revolving carbonization furnace, the other end of the revolving carbonization furnace is connected with the gas inlet opening of the dust chamber, the gas outlet opening of the dust chamber is connected with the inlet end of the incinerator, the outlet end of the incinerator is connected with the gas inlet end of the burning channel, the gas outlet end of the burning channel is connected with the inlet end of the waste-heat boiler, and the outlet end of the waste-heat boiler is connected with the inlet end of the dust catcher. By using the gas-solid mixed burning purification and heating system of the utility model, air containing volatile substance and air containing coal dust which are exhausted from a drying furnace can be introduced into the incinerator, and a superheater and the waste-heat boiler which are installed behind the burning channel can be utilized for heating heat medium, therefore the heat energy utilization efficiency can be improved, the energy can be saved, and the emission of noxious gas and environment pollution can be reduced.
Description
Technical field
The utility model relates to a kind of purification heat supply, relates in particular to a kind of gas-solid and mixes combustion purification heating system.
Background technology
Existing gas-solid mixes combustion and purifies heating system in use, be that the mass transport that needs are handled is arrived in the revolution retort, and the interior material of the high-temperature flue gas heating rotary retort that has a large amount of combustible gas components that utilizes the combustion chamber to produce, high-temperature flue gas can pass dust storage chamber then and enter in the incinerator, owing to have a large amount of combustibles in the high-temperature flue gas, in order to prevent its contaminated environment, so need utilize incinerator that it is burnt, high-temperature flue gas is directly discharged by chimney then.Because entering the gas of chimney is unburnt hot gas, the utilization efficiency of heat energy that makes the mixed combustion of gas-solid purify energy supplying system is lower, and energy resource consumption is higher, and is also bigger to the pollution of environment.
Summary of the invention
The purpose of this utility model provides a kind of energy savings, reduces noxious gas emission, reduces the pollution to environment, and the gas-solid that improves the utilization efficiency of heat energy of system mixes combustion and purifies heating system.
The utility model gas-solid mixes combustion and purifies heating system, comprise combustion chamber, revolution retort, dust storage chamber, incinerator, fire trough, waste heat boiler and deduster, the combustion chamber outlet flue links to each other with an end of revolution retort, the other end of revolution retort links to each other with the air inlet of dust storage chamber, wherein: the gas outlet of described dust storage chamber links to each other with the entrance point of incinerator, the port of export of incinerator links to each other with the inlet end of fire trough, the outlet side of fire trough links to each other with the entrance point of waste heat boiler, and the heat boiler outlet end links to each other with the deduster entrance point;
The utility model gas-solid mixes combustion and purifies heating system, and wherein: described incinerator also has air inlet, introduces burning mixture from this air inlet;
The utility model gas-solid mixes combustion and purifies heating system, wherein: in the described waste heat boiler superheater is housed;
The utility model gas-solid mixes combustion and purifies heating system, and wherein: described deduster is cyclone dust collectors;
The utility model gas-solid mixes combustion and purifies heating system, wherein: have manhole on the described fire trough;
The utility model gas-solid mixes combustion and purifies heating system, and wherein: described incinerator is or mixed coal or combustion gas or fuel oil incinerator.
Gas-solid of the present utility model mixes combustion and purifies heating system, can in incinerator, introduce containing volatile air and containing the air of coal dust of from drying oven, getting rid of, and can utilize the superheater and the waste heat boiler that are installed in the fire trough back, thermal medium is heated, thereby can improve utilization efficiency of heat energy, energy savings reduces noxious gas emission, reduces the pollution to environment.
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
Description of drawings
Fig. 1 is that the utility model gas-solid mixes the structural representation that combustion purifies heating system.
The specific embodiment
Referring to Fig. 1, the utility model gas-solid mixes combustion and purifies heating system, comprise combustion chamber 1, revolution retort 2, dust storage chamber 3, incinerator 4, fire trough 5, waste heat boiler 8 and deduster 9, combustion chamber 1 outlet flue links to each other with an end of revolution retort 2, the other end of revolution retort 2 links to each other with the air inlet of dust storage chamber 3, the gas outlet of dust storage chamber 3 links to each other with the entrance point of incinerator 4, the port of export of incinerator 4 links to each other with the inlet end of fire trough 5, the outlet side of fire trough 5 links to each other with the entrance point of waste heat boiler 8, and waste heat boiler 8 ports of export link to each other with deduster 9 entrance points.
Above-mentioned incinerator 4 also has air inlet 10, can introduce burning mixture from this air inlet 10, for example; That discharges from drying oven contains volatile air or contains the air of coal dust.Incinerator 4 is the moulded coal incinerator, can reduce the discharging of particle like this, reaches the purpose of depositing dust.
In the above-mentioned waste heat boiler 8 superheater 7 is housed, flow into heat transferring medium in the pipeline of superheater 7 as water, the heat of waste heat boiler 8 is taken away, fully utilize, flow into heat transferring medium in the pipeline of waste heat boiler 8 as water or air, take heat to place that other system needs.
Have manhole 6 on the above-mentioned fire trough 5, be beneficial to observe the state of burning.
Above-mentioned deduster 9 be the standard cleaner as: be X.ND/G type cyclone dust collectors.
Gas-solid of the present utility model mixes combustion and purifies heating system in use, the carbonized material that needs are handled can be transported in the revolution retort 2, and utilize carbonized material in the high-temperature flue gas heating rotary retort that has a large amount of combustible gas components 2 that combustion chamber 1 produces, high-temperature flue gas can pass dust storage chamber 3 then and enter in the incinerator 4, the air inlet 10 of incinerator 4 has also been introduced the air that contains volatile air and contain coal dust, they are in incinerator 4 internal combustion, high-temperature flue gas is by fire trough 5 then, burn fully, being installed in wherein in the waste heat boiler 8 of high-temperature flue gas to fire trough 5 back, the pipeline of superheater 7 and waste heat boiler 8 heats, make ducted air or water in superheater 7 and the waste heat boiler 8 be preheated to higher temperature, thereby can improve gas-solid and mix the utilization efficiency of heat energy that combustion purifies heating system, reduce energy resource consumption, reduce pollution environment.
High-temperature flue gas is by behind the waste heat boiler 8, and temperature reduces, after deduster 9 dedustings, and gas or directly enter atmosphere, or turn back to the drier of other system, use as heated air.
Above embodiment is not the qualification to utility model just to explanation of the present utility model, and the utility model institute restricted portion is referring to claim, and under the situation of spirit of the present utility model, the utility model can be done any type of modification.
Claims (6)
1. a gas-solid mixes combustion and purifies heating system, comprise combustion chamber (1), revolution retort (2), dust storage chamber (3), incinerator (4), fire trough (5), waste heat boiler (8) and deduster (9), combustion chamber (1) outlet flue links to each other with an end of revolution retort (2), the other end of revolution retort (2) links to each other with the air inlet of dust storage chamber (3), it is characterized in that: the gas outlet of described dust storage chamber (3) links to each other with the entrance point of incinerator (4), the port of export of incinerator (4) links to each other with the inlet end of fire trough (5), the outlet side of fire trough (5) links to each other with the entrance point of waste heat boiler (8), and waste heat boiler (8) port of export links to each other with deduster (9) entrance point.
2. gas-solid according to claim 1 mixes combustion and purifies heating system, and it is characterized in that: described incinerator (4) also has air inlet (10), introduces burning mixture from this air inlet (10).
3. gas-solid according to claim 2 mixes combustion and purifies heating system, it is characterized in that: superheater (7) is housed in the described waste heat boiler (8).
4. gas-solid according to claim 3 mixes combustion and purifies heating system, and it is characterized in that: described deduster (9) is cyclone dust collectors.
5. gas-solid according to claim 1 mixes combustion and purifies heating system, it is characterized in that: have manhole (6) on the described fire trough (5).
6. mix combustion according to the described gas-solid of any one claim in the claim 1 to 5 and purify energy supplying system, it is characterized in that: described incinerator (4) is moulded coal or mixed coal or combustion gas or fuel oil incinerator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201900084U CN201096352Y (en) | 2007-11-05 | 2007-11-05 | Gas-solid mixing combustion purifying and heat distribution system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201900084U CN201096352Y (en) | 2007-11-05 | 2007-11-05 | Gas-solid mixing combustion purifying and heat distribution system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201096352Y true CN201096352Y (en) | 2008-08-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201900084U Expired - Lifetime CN201096352Y (en) | 2007-11-05 | 2007-11-05 | Gas-solid mixing combustion purifying and heat distribution system |
Country Status (1)
| Country | Link |
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| CN (1) | CN201096352Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101469868B (en) * | 2008-08-28 | 2011-06-22 | 邹炎 | Comprehensive utilization method for activation furnace flue gas |
| CN103292333A (en) * | 2012-02-29 | 2013-09-11 | 太原嘉能动力科技有限公司 | System and method for utilizing waste heat of low-concentration combustible material in tail gas of Slapple furnace |
| CN103604128A (en) * | 2012-02-29 | 2014-02-26 | 中北大学 | Method for utilizing waste heat of low-concentration combustible materials in tail gas of Slapple furnace |
| CN103968673A (en) * | 2014-05-13 | 2014-08-06 | 神华集团有限责任公司 | Waste heat utilization device of tail gas of Serp activation furnace and tail gas utilization method |
-
2007
- 2007-11-05 CN CNU2007201900084U patent/CN201096352Y/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101469868B (en) * | 2008-08-28 | 2011-06-22 | 邹炎 | Comprehensive utilization method for activation furnace flue gas |
| CN103292333A (en) * | 2012-02-29 | 2013-09-11 | 太原嘉能动力科技有限公司 | System and method for utilizing waste heat of low-concentration combustible material in tail gas of Slapple furnace |
| CN103292333B (en) * | 2012-02-29 | 2013-12-25 | 太原嘉能动力科技有限公司 | System for utilizing waste heat of low-concentration combustible material in tail gas of Slapple furnace |
| CN103604128A (en) * | 2012-02-29 | 2014-02-26 | 中北大学 | Method for utilizing waste heat of low-concentration combustible materials in tail gas of Slapple furnace |
| CN103604128B (en) * | 2012-02-29 | 2014-12-24 | 中北大学 | Method for utilizing waste heat of low-concentration combustible materials in tail gas of Slapple furnace |
| CN103968673A (en) * | 2014-05-13 | 2014-08-06 | 神华集团有限责任公司 | Waste heat utilization device of tail gas of Serp activation furnace and tail gas utilization method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170714 Address after: 102200, room 21, 420 torch street, Changping District science and Technology Park, Beijing Patentee after: Beijing Nuomansibai Environmental Protection Technology Co., Ltd. Address before: 100086 No. 505, building 939, Haidian District, Beijing, Zhongguancun Co-patentee before: Li Xiaoyun Patentee before: Zou Yan Co-patentee before: Yao Wenda |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20080806 |