CN1619219A - Domestic garbage continuous incinerator - Google Patents
Domestic garbage continuous incinerator Download PDFInfo
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- CN1619219A CN1619219A CNA2004100656888A CN200410065688A CN1619219A CN 1619219 A CN1619219 A CN 1619219A CN A2004100656888 A CNA2004100656888 A CN A2004100656888A CN 200410065688 A CN200410065688 A CN 200410065688A CN 1619219 A CN1619219 A CN 1619219A
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- cloth
- air
- blast pipe
- revolution
- heater
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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 present invention relates to a domestic refuse continuous incinerator. It includes the components of rotary drying and combustion system, chimney, rotary distributor system, furnace body, non-sticky furnace wall, air-inducing and air-feeding system, air inlet tube, slag discharge pipe, high-temp. fan, oxygen-enriching device, water-vapour separator and feeding hopper, etc.
Description
Affiliated technical field
The present invention relates to a kind of environment protection equipment, particularly a kind of domestic garbage continuous incinerator.
Background technology
In actual life, house refuse produces in a large number, can cause great pollution as not handling.The present house refuse particularly processing of domestic waste has caused the attention of various countries.The method of landfill is seldom used.Major part all is to adopt stove, kiln etc. to carry out burning disposal.External stove mostly refuels or auxiliary fuel such as coal helps burning, though treatment effect is better, and the operation cost height.The refuelling that domestic stove has is combustion-supporting, and the need letter sorting rubbish that has could burn.Yet there are no and do not add auxiliary fuel, do not sort the practical stove that rubbish is worthy to be popularized with regard to complete continuous burning.
Summary of the invention
The object of the present invention is to provide a kind of processing cost low, do not add auxiliary fuel, need not sort the domestic garbage continuous incinerator that rubbish just can be burnt away the refuse continuously with practical value.
The present invention is achieved through the following technical solutions.A kind of domestic garbage continuous incinerator, it includes the attached burning of revolution oven dry system, revolution cloth system, body of heater, air inducing supply air system, high temperature resistant blower fan, oxygen-enriching device and steam trap.Upper of furnace body is provided with chimney, and the bottom is provided with residue outlet and blast pipe.
Described revolution dry attached burning system be arranged on body of heater above, the one end is equipped with feed hopper, also order and steam trap, oxygen-enriching device, high temperature resistant blower fan and annular blast pipe device link and communicate this end successively.This system's other end and revolution cloth system link and communicate.The hot flue gas of burner hearth enters the attached burning of revolution oven dry system, and the rubbish that enters from feed hopper is dried and partial combustion, makes the rubbish that enters in the burner hearth reach drying or substantially dry state.The hot-air that comes out from the attached burning of revolution oven dry system through steam trap moisture from after send into the burner hearth combustion-supporting by high temperature resistant blower fan at last through the oxygen-enriching device supplemental oxygen again.
The seal closure that the attached burning of oven dry system is connected is equipped with and turns round above the cloth tube of described revolution cloth system.The cloth bucket that extend in the burner hearth is housed below the cloth tube.Be provided with water sealing device between seal closure and the cloth tube.The cloth tube middle part is connected with variable-frequency motor by deceleration device.The cloth tube length L is a 1.5-2 rice, and its inner diameter of steel flue D is a 0.8-1 rice, and cloth bucket becomes an angle of inclination with vertical line, and its tilt angle alpha is the 20-30 degree, and cloth bucket length L 1 is a 0.8-1.2 rice.Variable-frequency motor drives cloth tube and further drives cloth bucket and rotates.Said structure makes the garbage energy that enters from the attached burning of revolution oven dry system be scattered in the burner hearth equably through the revolution cloth system.
Described air inducing supply air system is made up of annular blast pipe device and central air hose.Annular blast pipe device is linked to each other to communicate by air intake house steward, air loop duct, body of heater blast pipe and body of heater horn mouth order successively and forms.This device is arranged on body of heater medium position place and links by its air intake house steward and high temperature resistant blower fan and communicates.The body of heater horn mouth directly feeds in the burner hearth.Body of heater blast pipe and furnace diameter line are an angle of inclination, and its tilt angle alpha 1 is the 10-18 degree.The central air hose of air inducing supply air system is arranged in the middle of the lower furnace portion, and its height H is the 500-800 millimeter, and diameter D1 is the 500-800 millimeter.Being arranged on the blast pipe of body of heater bottom and central air hose links and communicates.This air inducing supply air system from two in burner hearth for combustion air, particularly annular blast pipe device is also sent into a large amount of oxygen enrichment hot-airs.The particularly a large amount of oxygen enrichment hot-air of secondary air enters can guarantee in the burner hearth that rubbish is by completing combustion in the burner hearth.
Attached burning system is dried in described revolution, and revolution cloth system, furnace wall, air inducing supply air system etc. are made by exotic material, and wherein the furnace wall, limit also cannot not made stickingly by alumina firebrick in the furnace wall.Alumina firebrick can guarantee that rubbish is not bonded on the furnace wall.
Advantage of the present invention is: (1) owing to use the attached burning of revolution oven dry system, and to make the rubbish that enters in the burner hearth be dry or it is dry to be bordering on, and this just provides a prerequisite for the abundant burning of rubbish.(2) owing to adopted the revolution cloth system, the garbage energy that enters burner hearth is scattered in the burner hearth equably, this is burnt garbage energy equably.(3) because the air inducing supply air system has designed secondary air, particularly oxygen-enriching device can be sent into hyperoxic hot-air, central air hose stretches into again in the burner hearth burner hearth is carried out big air quantity air feed, and this has just guaranteed fundamentally that rubbish can be burnt cmpletely in burner hearth.(4) because not sticking furnace wall, limit has been adopted in the furnace wall, rubbish can not sticked on the furnace wall, this has also guaranteed the burning quality of whole burner hearth.It is low to the invention provides a kind of processing cost in sum, need not add auxiliary fuel, does not need rubbish is just sorted the domestic waste incineration with practical value that can burn continuously rubbish.
Description of drawings
The invention will be further described below in conjunction with drawings and Examples.
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the structural representation that the present invention turns round cloth system.
Fig. 3 is the structural representation of the present invention's annular blast pipe device.
Among the figure: 1, feed hopper, 2, the attached burning of revolution oven dry system, 3, chimney, 4, revolution cloth system, 5, body of heater, 6, sticking furnace wall, limit, 7, annular blast pipe device, 8, central air hose, 9, residue outlet, 10, blast pipe, 11, high temperature resistant blower fan, 12, oxygen-enriching device, 13, steam trap, 14, variable-frequency motor, 15, deceleration device, 16, cloth bucket, 17 cloth tubes, 18, water sealing device, 19 seal closures, 20, air loop duct, 21, the body of heater blast pipe, 22, air intake house steward, 23 body of heater horn mouths.
The specific embodiment
Shown in each figure, a kind of domestic garbage continuous incinerator.It includes the attached burning of revolution oven dry system 2, revolution cloth system 4, body of heater 5, air inducing supply air system, high temperature resistant blower fan 11, oxygen-enriching device 12 and steam trap 13.Body of heater 5 tops are provided with chimney 3, and the bottom is provided with residue outlet 9 and blast pipe 10.The attached burning of revolution oven dry system 2 be arranged on body of heater 5 above, the one end is equipped with feed hopper 1, this end also successively order link by steam trap 13, oxygen-enriching device 12, high temperature resistant blower fan 11 and annular blast pipe device 7 and communicate.Revolution cloth system 4 is contained in the top of body of heater 5, and its middle part is a cloth tube 17, and cloth tube top connects seal closure 19, and seal closure and the attached burning of revolution oven dry system 2 join.Cloth tube 17 bottoms connect cloth bucket 16, and cloth bucket extend in the burner hearth.Be provided with water sealing device 18 between seal closure 19 and the cloth tube 17.Cloth tube 17 middle parts are connected with variable-frequency motor 14 by deceleration device 15.The cloth tube length L is 1.6 meters, and its inner diameter of steel flue D is 1 meter, and cloth bucket becomes an angle of inclination with vertical line, and its tilt angle alpha is 20 degree, and cloth bucket length L 1 is 1 meter.The air inducing supply air system is made up of annular blast pipe device 7 and central air hose 8.Wherein annular blast pipe device 7 is arranged on body of heater 5 middle parts, and its air intake house steward 23 1 ends and high temperature resistant blower fan 11 link and communicate.Air intake house steward 23 other ends communicate by air loop duct 20, body of heater blast pipe 22, body of heater horn mouth 23 and body of heater 5 burner hearths successively.The diameter line of body of heater blast pipe 22 and burner hearth of the furnace body becomes the angle of inclination of 15 degree.Central air hose 8 is arranged in the middle of the lower furnace portion, and its height H is 600 millimeters, and diameter D1 is 600 millimeters.Central air hose 8 and blast pipe 10 link and communicate.The attached burning of revolution oven dry system 2, revolution cloth system 4, air inducing supply air system, furnace wall 6 etc. all has exotic material to make, and wherein furnace wall, limit 6 cannot not made stickingly by alumina firebrick in furnace wall 6.
Claims (4)
1, a kind of domestic garbage continuous incinerator, it includes the attached burning of revolution oven dry system, the revolution cloth system, body of heater, the air inducing supply air system, high temperature resistant blower fan, oxygen-enriching device and steam trap, upper of furnace body is provided with chimney, the bottom is provided with residue outlet and blast pipe, it is characterized in that upper of furnace body is provided with the revolution cloth system, and revolution cloth system and the attached burning of revolution oven dry system one end link, the attached burning of the revolution oven dry system other end is equipped with feed hopper, and this end is order and steam trap successively also, oxygen-enriching device, high temperature resistant phoenix machine, annular blast pipe device, burner hearth links and communicates; The air inducing supply air system is made up of annular blast pipe device and central air hose.
2, domestic garbage continuous incinerator according to claim 1, the middle part that it is characterized in that turning round cloth system is a cloth tube, the seal closure of top for being connected with the attached burning of revolution oven dry system, the bottom is the cloth bucket that stretches in burner hearth, be provided with water sealing device between seal closure and the cloth tube, the cloth tube middle part is connected with variable-frequency motor by deceleration device, the cloth tube length L is a 1.5-2 rice, in it simply the footpath D be 0.8-1 rice, cloth bucket becomes an angle of inclination with vertical line, its tilt angle alpha is the 20-30 degree, and cloth bucket length L 1 is a 0.8-1.2 rice.
3, domestic garbage continuous incinerator according to claim 1, the annular blast pipe device that it is characterized in that the air inducing supply air system is arranged on body of heater medium position place and links by its air intake house steward and high temperature resistant blower fan, the air intake house steward other end links to each other with burner hearth with air loop duct, body of heater blast pipe, body of heater horn mouth in proper order successively and communicates, body of heater blast pipe and the furnace diameter line material angle that becomes to incline, its tilt angle alpha 1 is the 10-18 degree; The central air hose of air inducing supply air system is arranged in the middle of the lower furnace portion, and its height H is the 500-800 millimeter, and diameter D1 is the 500-800 millimeter, and central air hose and blast pipe link and communicate.
4, domestic garbage continuous incinerator according to claim 1 is characterized in that the furnace wall cannot not make stickingly the furnace wall, limit by alumina firebrick.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100656888A CN1282849C (en) | 2004-11-09 | 2004-11-09 | Domestic garbage continuous incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100656888A CN1282849C (en) | 2004-11-09 | 2004-11-09 | Domestic garbage continuous incinerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1619219A true CN1619219A (en) | 2005-05-25 |
| CN1282849C CN1282849C (en) | 2006-11-01 |
Family
ID=34764757
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100656888A Expired - Fee Related CN1282849C (en) | 2004-11-09 | 2004-11-09 | Domestic garbage continuous incinerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1282849C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100432532C (en) * | 2006-07-04 | 2008-11-12 | 潘云芳 | Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator |
| WO2010037268A1 (en) * | 2008-09-27 | 2010-04-08 | Yuan Yongyang | Method for processing garbage and comprehensive treatment technology thereof |
| CN103574618A (en) * | 2012-08-12 | 2014-02-12 | 张海明 | Oxygen assisting combustion type household garbage disposer |
-
2004
- 2004-11-09 CN CNB2004100656888A patent/CN1282849C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100432532C (en) * | 2006-07-04 | 2008-11-12 | 潘云芳 | Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator |
| WO2010037268A1 (en) * | 2008-09-27 | 2010-04-08 | Yuan Yongyang | Method for processing garbage and comprehensive treatment technology thereof |
| CN103574618A (en) * | 2012-08-12 | 2014-02-12 | 张海明 | Oxygen assisting combustion type household garbage disposer |
| CN103574618B (en) * | 2012-08-12 | 2016-08-31 | 张海明 | Help oxygen combustion-type domestic garbage treatment machine |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1282849C (en) | 2006-11-01 |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: TENG QINGHUA Free format text: FORMER OWNER: TENG QINGHUA; PAN YUNFANG Effective date: 20071019 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20071019 Address after: 213300, Jiangsu, Liyang Province town front Street No. 16, Liyang city green world science and technology environmental protection Co., Ltd. Patentee after: Teng Qinghua Address before: 213300, Jiangsu, Liyang Province town front Street No. 16, Liyang city green world science and technology environmental protection Co., Ltd. Co-patentee before: Pan Yunfang Patentee before: Teng Qinghua |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20061101 Termination date: 20141109 |
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| EXPY | Termination of patent right or utility model |