CN1877197A - Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator - Google Patents

Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator Download PDF

Info

Publication number
CN1877197A
CN1877197A CNA2006100882074A CN200610088207A CN1877197A CN 1877197 A CN1877197 A CN 1877197A CN A2006100882074 A CNA2006100882074 A CN A2006100882074A CN 200610088207 A CN200610088207 A CN 200610088207A CN 1877197 A CN1877197 A CN 1877197A
Authority
CN
China
Prior art keywords
incinerator
furnace
oxygen
oxygen debt
swinging
Prior art date
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.)
Granted
Application number
CNA2006100882074A
Other languages
Chinese (zh)
Other versions
CN100432532C (en
Inventor
潘云芳
王煦
Original Assignee
潘云芳
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 潘云芳 filed Critical 潘云芳
Priority to CNB2006100882074A priority Critical patent/CN100432532C/en
Publication of CN1877197A publication Critical patent/CN1877197A/en
Application granted granted Critical
Publication of CN100432532C publication Critical patent/CN100432532C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

The invention relates to a waste combined burning processing method and special upright abundant oxygen continuous burning furnace, with low cost, non auxiliary fuel and non separation, and secondary burning. Wherein, it comprises the first burning furnace (17), the second burning furnace (19) connected to the first one, and the rotating oxygen-lack drying furnace (20) connected to the second burning furnace (19); there is oxygen-lack furnace gas transmit tube (15) between the inlet of rotating oxygen-lack drying furnace (2) and the oxygen-lack furnace gas wind hole (13) on the wall of second burning furnace (19); the oxygen-lack furnace gas wind hole (13), the oxygen-lack furnace gas transmit tube (15), the passive fan (20), the rotating oxygen-lack drying furnace (2) and the second burning room (4) form one passive oxygen-lack smoke circuit. The invention has simple structure and better burning effect without auxiliary fuel.

Description

A kind of rubbish combination incineration treatment method and special vertical oxygen-enriched continuous burning wind fire furnace
Technical field
The present invention relates to a kind of waste disposal method and equipment, especially a kind of house refuse, medical refuse burning processing method and device specifically a kind ofly will be dried, the combustion thermal cycle of second-time burning is in the rubbish combination incineration treatment method and the special vertical oxygen-enriched continuous burning wind fire furnace thereof of one.
Background technology
At present, garbage disposal day by day becomes one of environmental issue of national governments' pay attention to day by day, and along with improving constantly of Increase of population and living standard, quantity of refuse grows with each passing day, and it and people strive environment with striving, and very easily causes environmental pollution.
Garbage disposal at present develops to burning and fully utilize direction from traditional landfill, wherein house refuse and medical waste be because its calorific value is higher and burn and can remove the advantage of germ effectively and more and more be subject to people's attention, and purpose such as the heat that produces in the combustion process also can be used for generating electricity, heat supply and be it is believed that it is one of best domestic garbage was harmlessly treated method.Existing incinerating method generally is to adopt stove to burn, need refuel during burning or auxiliary fuel such as coal combustion-supporting, the operation cost height, the employing grate furnace is also arranged, fluid bed furnace, rotary kiln, vertical direct combustion stove, combustion furnaces such as vertical pyrolysis oven carry out waste incineration, but because the moisture content in the rubbish is bigger, its combustion efficiency is all not very good, people have expected rubbish is dried for this reason, remove the method that moisture content improves efficiency of combustion to greatest extent, but owing to need to increase independent drying unit, add auxiliary fuel, thereby make that whole incinerator floor space is big, investment increases, the flow process complexity, therefore operating cost improves greatly, and no practicality is badly in need of the problem that innoxious burning that a kind of new incinerating method of invention and equipment solves present rubbish and medical waste is handled.
Summary of the invention
The objective of the invention is at the efficiency of combustion that exists in existing rubbish and the medical waste processing not high, equipment investment is excessive, technological process is complicated problems too, it is low to invent a kind of processing cost, do not add auxiliary fuel, need not sort the rubbish combination incineration treatment method and the special vertical oxygen-enriched continuous burning wind fire furnace of the combustion thermal cycle that integrates oven dry, second-time burning that just can burn fully continuously.
Technical scheme of the present invention is:
A kind of rubbish combination incineration treatment method is characterized in that it may further comprise the steps:
At first, incinerator and secondary incinerator are integrated, form a vertical oxygen-enriched continuous burning wind fire furnace, and make incinerator down, the secondary incinerator is last;
Other, the oxygen debt furnace gas that the secondary incinerator is produced is introduced in the oxygen debt drying oven of swinging the rubbish that is about to enter in the secondary incinerator is carried out oxygen debt oven dry, enters the moisture content of the rubbish in the secondary incinerator with minimizing, improves combustion efficiency;
The 3rd designs the secondary air mouth respectively on the top of an incinerator and the lower position of secondary incinerator, and air inlet is arranged so that enter the wind of body of heater along the body of heater tangential direction formed whirlwind to improve the uniformity of efficiency of combustion and burning in body of heater, the air-vent that will introduce the oxygen debt furnace gas in the oxygen debt drying oven simultaneously is arranged between the secondary air mouth of a described incinerator and secondary incinerator;
At last, the rubbish after from oxygen debt drying oven stove is done is entered in the secondary incinerator through the high temperature resistant distributing device of speaking out of turn of single-revolution.
The vertical oxygen-enriched continuous burning wind fire furnace that matches with said method of the present invention is characterized in that it comprises:
An incinerator 17, one one combustion of its inner formation chamber 5, the bottom of one combustion chamber 5 is provided with a high-end tower discharger 6 by transmission device 7 drivings, be provided with a burner 18 in the bottom of an incinerator and the relative position place, upper end of high-end tower discharger 6, a furnace bottom wind air inlet 10 that is provided with slag notch 8 in the bottom of high-end tower discharger 6 and communicates with a combustion chamber 5 is provided with a combustion chamber secondary wind air inlet 11 on furnace wall, incinerator 17 top;
A secondary incinerator 19 that links to each other with incinerator 17, the inside of secondary incinerator 19 forms a dual firing chamber 4, the bottom of described dual firing chamber 4 communicates with a combustion chamber 5, its top is garbage inlet, the high temperature resistant distributing device 3 of speaking out of turn of swinging is installed on described garbage inlet, on the furnace wall of secondary incinerator 19 bottoms, be provided with dual firing chamber's secondary wind air inlet 12, on the furnace wall of the secondary incinerator 19 between a described combustion chamber secondary wind air inlet 11 and the dual firing chamber's secondary wind air inlet 12, be provided with oxygen debt furnace gas air-vent 13; On the furnace wall on secondary incinerator 19 tops, also be provided with the flue gas that communicates with dual firing chamber 4 and recycle gas outlet 9;
The oxygen debt drying oven 2 of swinging, it is installed in the top of described secondary incinerator 19, its charging aperture is equipped with feed hopper 1, the upper end of its discharging opening and the high temperature resistant distributing device 3 of speaking out of turn of aforesaid swinging links to each other and seals mutually with the charging aperture of secondary incinerator 19, between the oxygen debt furnace gas air-vent 13 on the furnace wall of the charging aperture of the oxygen debt drying oven 2 of swinging and secondary incinerator 19, be connected with oxygen debt furnace gas conveyance conduit 15, on described oxygen debt furnace gas conveyance conduit 15, negative-pressure air fan 20 is installed, oxygen debt furnace gas air-vent 13, oxygen debt furnace gas conveyance conduit 15, negative-pressure air fan 20, swinging is oxygen debt to form the oxygen debt flue gas of negative pressure loop between drying oven 2 and the dual firing chamber 4.
A described combustion chamber secondary wind air inlet 11, dual firing chamber's secondary wind air inlet 12, oxygen debt furnace gas air-vent 13 are along furnace wall inwall arranged tangential, and its quantity is weekly 3-8.
Described swinging is high temperature resistant, and the distributing device 3 of speaking out of turn is made up of cylindrical shell 301, dividing plate 302, discharging mouth 303, its median septum 302 is evenly arranged in the cylindrical shell 301, and the discharging mouth 303 equal with dividing plate 302 quantity is positioned at the bottom of cylindrical shell 301 and links to each other with corresponding dividing plate 302.
Each swinging is high temperature resistant, and the distributing device 3 of speaking out of turn is provided with 2-6 discharging mouth 303.
Described swinging is oxygen debt, and drying oven 2 is made up of body of heater 201 and the helical form guide plate 202 and the pivoting support 203 that are installed in the body of heater 201, and body of heater 201 is bearing on the pivoting support 203, and pivoting support 203 is driven by drive unit.
The present invention has the following advantages:
1, oven dry of the present invention, two combustions, a combustion structure combining form be simplified structure greatly, reduces floor space, and the oxygen debt flue gas of high temperature that makes full use of dual firing chamber dries, and can save the heating, drying device, makes structural reduction reasonable.
2, reasonably design of cloth wind and air intake direction help improving efficiency of combustion, form a favourable raising efficiency of combustion, the eddy airstream of the prolongation oxygen enrichment time of staying of wind in the combustion chamber in the combustion chamber.Help abundant burning, make wind and fire reach sufficient combination at combustion chamber and sole.
3, a large amount of toxic and harmfuls in the drying chamber can be introduced in two combustions through pyrolytic by air return system, very favourable to environmental protection.
4, simple in structure, manufacturing cost and garbage disposal cost are low, need not to add auxiliary fuel except that igniting, need not to sort the recycling that just can realize burning and burning continuously heat, and need not existing retracting device is done any change.
Description of drawings
Fig. 1 is an operation principle schematic diagram of the present invention.
Fig. 2 is a structural representation of the present invention.
Fig. 3 is the high temperature resistant distributing device of speaking out of turn of swinging of the present invention.
Fig. 4 is the upward view of Fig. 3.
Fig. 5 is the structural representation of air inlet of the present invention and air outlet.
The specific embodiment
The present invention is further illustrated for following structure drawings and Examples.
Method principle of the present invention as shown in Figure 1.
At first, incinerator and secondary incinerator are integrated, form a vertical oxygen-enriched continuous burning wind fire furnace, and make incinerator down, the secondary incinerator is last;
Other, the oxygen debt furnace gas that the secondary incinerator is produced is introduced in the oxygen debt drying oven of swinging by a negative-pressure air fan rubbish that is about to enter in the secondary incinerator is carried out oxygen debt oven dry, enters the moisture content of the rubbish in the secondary incinerator with minimizing, improves combustion efficiency;
The 3rd designs the secondary air mouth respectively on the top of an incinerator and the lower position of secondary incinerator, and air inlet is arranged so that enter the wind of body of heater along the body of heater tangential direction formed whirlwind to improve the uniformity of efficiency of combustion and burning in body of heater, the air-vent that will introduce the oxygen debt furnace gas in the oxygen debt drying oven simultaneously is arranged between the secondary air mouth of a described incinerator and secondary incinerator;
At last, the rubbish after from oxygen debt drying oven stove is done is entered in the secondary incinerator through the high temperature resistant distributing device of speaking out of turn of single-revolution.
Vertical oxygen-enriched continuous burning wind fire furnace of the present invention is shown in Fig. 2-5, and it comprises:
An incinerator 17, one one combustion of its inner formation chamber 5, the bottom of one combustion chamber 5 is provided with a high-end tower discharger 6 that is driven by transmission device 7 (can adopt general dynamo-electric gear to be realized) and (can designs voluntarily with reference to relevant handbook, also can adopt the commercially available prod to be realized), be provided with a burner 18 in the bottom of an incinerator and the relative position place, upper end of high-end tower discharger 6, a furnace bottom wind air inlet 10 that is provided with slag notch 8 in the bottom of high-end tower discharger 6 and communicates with a combustion chamber 5, on furnace wall, incinerator 17 top, be provided with a combustion chamber secondary wind air inlet 11, as Fig. 2, should be provided with heat-resisting heat-insulation layer 14 in the furnace wall;
A secondary incinerator 19 that links to each other with incinerator 17, the inside of secondary incinerator 19 forms a dual firing chamber 4, the bottom of described dual firing chamber 4 communicates with a combustion chamber 5, its top is garbage inlet, the high temperature resistant distributing device 3 of speaking out of turn of swinging is installed on described garbage inlet, this swinging is high temperature resistant speaks out of turn distributing device 3 by cylindrical shell 301, dividing plate 302, discharging mouth 303 is formed, as Fig. 3, shown in 4, its median septum 302 is evenly arranged in the cylindrical shell 301, the discharging mouth 303 equal with dividing plate 302 quantity is positioned at the bottom of cylindrical shell 301 and links to each other with corresponding dividing plate 302, and wherein the quantity of discharging mouth 303 can be 2-6.On the furnace wall of secondary incinerator 19 bottoms, be provided with dual firing chamber's secondary wind air inlet 12, on the furnace wall of the secondary incinerator 19 between a described combustion chamber secondary wind air inlet 11 and the dual firing chamber's secondary wind air inlet 12, be provided with oxygen debt furnace gas air-vent 13; On the furnace wall on secondary incinerator 19 tops, also be provided with the flue gas that communicates with dual firing chamber 4 and recycle gas outlet 9;
The oxygen debt drying oven 2 of swinging, it is installed in the top of described secondary incinerator 19, its charging aperture is equipped with feed hopper 1, the upper end of its discharging opening and the high temperature resistant distributing device 3 of speaking out of turn of aforesaid swinging links to each other and seals mutually with the charging aperture of secondary incinerator 19, between the oxygen debt furnace gas air-vent 13 on the furnace wall of the charging aperture of the oxygen debt drying oven 2 of swinging and secondary incinerator 19, be connected with oxygen debt furnace gas conveyance conduit 15, on described oxygen debt furnace gas conveyance conduit 15, negative-pressure air fan 20 is installed, oxygen debt furnace gas air-vent 13, oxygen debt furnace gas conveyance conduit 15, negative-pressure air fan 20, swinging is oxygen debt to form the oxygen debt flue gas of negative pressure loop between drying oven 2 and the dual firing chamber 4.This swinging is oxygen debt, and drying oven 2 can be made up of body of heater 201 and the helical form guide plate 202 and the pivoting support 203 that are installed in the body of heater 201, and body of heater 201 is bearing on the pivoting support 203, and pivoting support 203 is driven by drive unit.
An above-mentioned combustion chamber secondary wind air inlet 11, dual firing chamber's secondary wind air inlet 12, oxygen debt furnace gas air-vent 13 are along furnace wall inwall arranged tangential, its quantity is weekly 3-8, as shown in Figure 5, the number of plies of a combustion chamber secondary wind air inlet 11, dual firing chamber's secondary wind air inlet 12, oxygen debt furnace gas air-vent 13 also can increase as required during concrete enforcement, present embodiment has only provided the structure of each one deck, but is not limited to this structure.
The part that present embodiment does not relate to such as heat-insulation layer 14, burner 18 etc. are all same as the prior art.
The course of work of the present invention is:
Rubbish enters the oxygen debt drying oven 2 of swinging the high-temperature oxygen-enriched burning of carrying out of firing through the bottom and that the high temperature resistant distributing device 3 of speaking out of turn evenly enters dual firing chamber 4 from swinging, preliminary oven dry back between the top of chamber 5 from feed hopper 1 charging, uncombusted part is met with the wind facies of a combustion chamber secondary wind air inlet 11 in the vertical drop process in a combustion chamber 5 and is become slag charge after fully burning is continued in the back and fall into the high-end tower cylinder glassware 6 broken backs with broken function and discharge out of the furnace from slag notch 8, contain the oxygen normal temperature air and not only make the slag cooling and a furnace bottom wind air inlet 10 of furnace bottom blasts, the surplus charcoal of uncombusted is burnt to the greatest extent grill thoroughly.Temperature in the dual firing chamber 4 can reach about 1000 degree, the dioxin of going into through the negative power traction of negative pressure in the dioxin that produces in the combustion process and the oxygen debt drying oven 2 of swinging can be carried out pyrolytic it can not polluted environment, guarantee simultaneously after follow-up smoke processing system is handled, to get final product compliance with environmental protection requirements from the flue gas that the waste heat recovery mouth is discharged.

Claims (6)

1, a kind of rubbish combination incineration treatment method is characterized in that it may further comprise the steps:
At first, incinerator and secondary incinerator are integrated, form a vertical oxygen-enriched continuous burning wind fire furnace, and make incinerator down, the secondary incinerator is last;
Other, the oxygen debt furnace gas that the secondary incinerator is produced is introduced in the oxygen debt drying oven of swinging the rubbish that is about to enter in the secondary incinerator is carried out oxygen debt oven dry, enters the moisture content of the rubbish in the secondary incinerator with minimizing, improves combustion efficiency;
The 3rd designs the secondary air mouth respectively on the top of an incinerator and the lower position of secondary incinerator, and air inlet is arranged so that enter the wind of body of heater along the body of heater tangential direction formed whirlwind to improve the uniformity of efficiency of combustion and burning in body of heater, the air-vent that will introduce the oxygen debt furnace gas in the oxygen debt drying oven simultaneously is arranged between the secondary air mouth of a described incinerator and secondary incinerator;
At last, the rubbish after from oxygen debt drying oven stove is done is entered in the secondary incinerator through the high temperature resistant distributing device of speaking out of turn of single-revolution.
2, a kind of vertical oxygen-enriched continuous burning wind fire furnace of realizing the described method of claim 1 is characterized in that it comprises:
An incinerator (17), one one combustion of its inner formation chamber (5), the bottom of one combustion chamber (5) is provided with a high-end tower discharger (6) by transmission device (7) driving, be provided with a burner (18) in the bottom of an incinerator and the relative position place, upper end of high-end tower discharger (6), a furnace bottom wind air inlet (10) that is provided with slag notch (8) in the bottom of high-end tower discharger (6) and communicates with a combustion chamber (5) is provided with a combustion chamber secondary wind air inlet (11) on an incinerator (17) furnace wall, top;
A secondary incinerator (19) that links to each other with an incinerator (17), the inside of secondary incinerator (19) forms a dual firing chamber (4), the bottom of described dual firing chamber (4) communicates with a combustion chamber (5), its top is garbage inlet, the high temperature resistant distributing device of speaking out of turn of swinging (3) is installed on described garbage inlet, on the furnace wall of secondary incinerator (19) bottom, be provided with dual firing chamber's secondary wind air inlet (12), on the furnace wall of the secondary incinerator (19) between a described combustion chamber secondary wind air inlet (11) and the dual firing chamber's secondary wind air inlet (12), be provided with oxygen debt furnace gas air-vent (13); On the furnace wall on secondary incinerator (19) top, also be provided with the flue gas that communicates with dual firing chamber (4) and recycle gas outlet (9);
An oxygen debt drying oven of swinging (2), it is installed in the top of described secondary incinerator (19), its charging aperture is equipped with feed hopper (1), the upper end of its discharging opening and the high temperature resistant distributing device of speaking out of turn of aforesaid swinging (3) links to each other and seals mutually with the charging aperture of secondary incinerator (19), between the oxygen debt furnace gas air-vent (13) on the furnace wall of the charging aperture of the oxygen debt drying oven of swinging (2) and secondary incinerator (19), be connected with oxygen debt furnace gas conveyance conduit (15), negative-pressure air fan (20) is installed, oxygen debt furnace gas air-vent (13) on described oxygen debt furnace gas conveyance conduit (15), oxygen debt furnace gas conveyance conduit (15), negative-pressure air fan (20), form the oxygen debt flue gas of negative pressure loop between oxygen debt drying oven of swinging (2) and the dual firing chamber (4).
3, vertical oxygen-enriched continuous burning wind fire furnace according to claim 2, it is characterized in that a described combustion chamber secondary wind air inlet (11), dual firing chamber's secondary wind air inlet (12), oxygen debt furnace gas air-vent (13) along furnace wall inwall arranged tangential, its quantity is weekly 3-8.
4, vertical oxygen-enriched continuous burning wind fire furnace according to claim 2, it is characterized in that the high temperature resistant distributing device of speaking out of turn of described swinging (3) is made up of cylindrical shell (301), dividing plate (302), discharging mouth (303), its median septum (302) is evenly arranged in the cylindrical shell (301), and the discharging mouth (303) equal with dividing plate (302) quantity is positioned at the bottom of cylindrical shell (301) and links to each other with corresponding dividing plate (302).
5, vertical oxygen-enriched continuous burning wind fire furnace according to claim 4 is characterized in that the high temperature resistant distributing device of speaking out of turn of described swinging (3) is provided with 2-6 discharging mouth (303).
6, vertical oxygen-enriched continuous burning wind fire furnace according to claim 2, it is characterized in that the oxygen debt drying oven of described swinging (2) is made up of body of heater (201) and the helical form guide plate (202) and the pivoting support (203) that are installed in the body of heater (201), body of heater (201) is bearing on the pivoting support (203), and pivoting support (203) is driven by drive unit.
CNB2006100882074A 2006-07-04 2006-07-04 Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator Expired - Fee Related CN100432532C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2006100882074A CN100432532C (en) 2006-07-04 2006-07-04 Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2006100882074A CN100432532C (en) 2006-07-04 2006-07-04 Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator

Publications (2)

Publication Number Publication Date
CN1877197A true CN1877197A (en) 2006-12-13
CN100432532C CN100432532C (en) 2008-11-12

Family

ID=37509706

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2006100882074A Expired - Fee Related CN100432532C (en) 2006-07-04 2006-07-04 Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator

Country Status (1)

Country Link
CN (1) CN100432532C (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103075734A (en) * 2012-12-27 2013-05-01 中信重工机械股份有限公司 Waste incineration ash slag cooling machine
CN104676603A (en) * 2015-01-27 2015-06-03 上海煜工环保科技有限公司 U-shaped bottom-hanging type ash and slag melting treatment device
CN104819470A (en) * 2015-05-25 2015-08-05 山东百川同创能源有限公司 Biomass solid waste and hazardous waste treatment system
CN104819472A (en) * 2015-05-25 2015-08-05 山东百川同创能源有限公司 Biomass solid waste and hazardous waste combustion gas production system
CN106076204A (en) * 2016-08-10 2016-11-09 茂名重力石化机械制造有限公司 A kind of pressure vessel and air inlet thereof

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4063521A (en) * 1976-08-19 1977-12-20 Econo-Therm Energy Systems Corporation Incinerator having gas flow controlling separator
CN1089023A (en) * 1992-12-26 1994-07-06 祁英 A kind of novel castoff burning method and device
CN2381894Y (en) * 1999-07-23 2000-06-07 王煦 Rotary combined firing kiln
JP2002372217A (en) * 2001-06-15 2002-12-26 Goro Takagi Turning combustion type fluidized bed incinerator
CN2521499Y (en) * 2002-01-08 2002-11-20 中国船舶重工集团公司第七一○研究所 Garbage incinerator
CN2563443Y (en) * 2002-08-30 2003-07-30 上海多灵环保工程设备有限公司 Illiptically rotary unloading garbage incinerator
CN1317528C (en) * 2004-05-09 2007-05-23 溧阳市环境卫生管理处 Domestic garbage incinerator
CN1282849C (en) * 2004-11-09 2006-11-01 滕清华 Domestic garbage continuous incinerator
CN2856734Y (en) * 2006-07-04 2007-01-10 潘云芳 Vertical oxygen-enriched continuous incinerator

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103075734A (en) * 2012-12-27 2013-05-01 中信重工机械股份有限公司 Waste incineration ash slag cooling machine
CN104676603A (en) * 2015-01-27 2015-06-03 上海煜工环保科技有限公司 U-shaped bottom-hanging type ash and slag melting treatment device
CN104819470A (en) * 2015-05-25 2015-08-05 山东百川同创能源有限公司 Biomass solid waste and hazardous waste treatment system
CN104819472A (en) * 2015-05-25 2015-08-05 山东百川同创能源有限公司 Biomass solid waste and hazardous waste combustion gas production system
CN104819472B (en) * 2015-05-25 2017-04-26 山东百川同创能源有限公司 Biomass solid waste and hazardous waste combustion gas production system
CN106076204A (en) * 2016-08-10 2016-11-09 茂名重力石化机械制造有限公司 A kind of pressure vessel and air inlet thereof

Also Published As

Publication number Publication date
CN100432532C (en) 2008-11-12

Similar Documents

Publication Publication Date Title
CN2809450Y (en) Continuous and controllable pyrogenation integrated refuse incinerator
CN105444183B (en) Stoker fired grate formula rubbish list furnace gas CIU and its processing method
CN106224974A (en) Waste incineration processing system
CN1301384C (en) Technique for burning domestic garbage and garbage incinerator
CN100432532C (en) Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator
CN200958757Y (en) Vertical thermal-decomposition incinerator
CN207514917U (en) Waste incineration and generating electricity device
CN106322439B (en) A kind of normal pressure smokeless environment-friendly combustion stove
CN206191599U (en) Refuse disposal system
CN206191597U (en) Small -size rural garbage pyrolytic gasification equipment
CN2856734Y (en) Vertical oxygen-enriched continuous incinerator
CN1282849C (en) Domestic garbage continuous incinerator
CN206514307U (en) It is a kind of to reduce the device and waste incineration processing system of unburned thing discharge capacity
CN2788032Y (en) High temperature carbonizing refuse incinerator
CN206094168U (en) Burning furnace utensil is fired in smokeless environmental protection of ordinary pressure
CN201034321Y (en) Burning decontamination plant treating life refuse by employing air-swept mill
CN2733185Y (en) Domestic incinerator
CN106568087A (en) Garbage treatment system
CN2323269Y (en) Vertical multipurpose incinerating and water heating furnace
CN2166314Y (en) Energy-saving garbage purifying furnace
CN106594745A (en) Garbage partitioning efficient treatment device
CN100501239C (en) Burning and purifying device for processing daily garbage using wind swept mill
CN207828184U (en) Box-like pyrolysis gasification furnace in one kind
CN211650258U (en) Garbage pyrolysis furnace
CN2260243Y (en) Incineration furnace for dangerour and urban garbage

Legal Events

Date Code Title Description
PB01 Publication
C06 Publication
SE01 Entry into force of request for substantive examination
C10 Entry into substantive examination
GR01 Patent grant
C14 Grant of patent or utility model
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20081112

Termination date: 20120704

C17 Cessation of patent right