CN101135454A - Dangerous waste incineration device - Google Patents
Dangerous waste incineration device Download PDFInfo
- Publication number
- CN101135454A CN101135454A CNA2007101444014A CN200710144401A CN101135454A CN 101135454 A CN101135454 A CN 101135454A CN A2007101444014 A CNA2007101444014 A CN A2007101444014A CN 200710144401 A CN200710144401 A CN 200710144401A CN 101135454 A CN101135454 A CN 101135454A
- Authority
- CN
- China
- Prior art keywords
- burner hearth
- fire grate
- communicated
- air
- dangerous waste
- 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
Links
Images
Classifications
-
- 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
This invention is an incineration device of dangerous waste which solves the problems of existing incineration device including low combustion efficiency, disability of heat recovery, low adaptability and high investment. The recovery device in this invention is positioned at the top of the furnace, the air pre-heater is positioned inside the tail flue, the air supply device is positioned below the furnace and connected to the furnace, the ridge-type sloped reciprocating grate is positioned on the bottom face of the furnace, the face arch is positioned on the front wall of the furnace while the rear arch is positioned on the back wall. This device has the advantage of independent heat recovery, adaptability for different dangerous waste and low investment.
Description
Technical field
The present invention relates to a kind of incinerator, be specifically related to a kind of hazardous waste be carried out the incinerator that preliminary treatment, high efficiency are burned and heat energy makes full use of.
Background technology
Hazardous waste becomes a key factor that threatens China's environment day by day, needs more the rational and effective mode and handles hazardous waste, reduces it to environment and biological harm.Wherein, dangerous waste incineration subtracts with it and to hold advantages such as decrement, sterilization, secondary pollution are low and be subjected to increasing attention.Different hazardous wastes is for burning the treatment conditions difference that requires, burning disposal equipment is a lot of at present, the scope of application has nothing in common with each other: 1, revolving burner: the agent structure of revolving burner is rotary column type steel cylinder, inner lining refractory, axle center and horizontal line are 3～5 degree angles, act as a fuel with oil or coal.Refuse enters revolving burner from eminence, and residue is discharged from low side, and liquid wastes can be entrained into the stove burning or spray in the stove and burn; 2, fluidized bed incinerator: fluidized bed incinerator is made up of the inert particulate that the vertical container that with the refractory material is lining reaches wherein, air is entered in the stove by the ventilation unit of incinerator bottom, vertical lifting enters the stratum granulosum of fluid bed by a distribution plate, and stratum granulosum is owing to blowing of ascending air caused the bed fluidisation; 3, liquid sprays stove: liquid spray stove be used for handling the various refuses that can carry by pump (be difficult for completing combustion sewage, contain high-octane solvent slop etc.).Refuse by nozzle atomization after fully burning, low-calorie refuse need dispose auxiliary fuel, the energized fluid refuse can be used as fuel supply office reason system.
In above-mentioned several incinerator, revolving burner can turn round continuously, but infrastructure investment is higher, efficiency of combustion is low, and reclaims the waste heat boiler that heat need be other.It is poor to the adaptability of refuse that fluidized bed incinerator and liquid spray stove.To different hazardous wastes, need dissimilar incinerators to handle, increased investment.
Summary of the invention
The present invention exists in order to solve existing burning disposal equipment that efficiency of combustion is low, equipment itself can't carry out heat recovery, poor, the equipment investment problem of higher of apparatus adaptability, and then a kind of dangerous waste incineration device is provided.
Technical scheme of the present invention is: dangerous waste incineration device comprises feeding device 10, burner hearth 40, ash handling equipment 50 and air preheater 31, air supply device 51, horizontal flue 41, back-end ductwork 42; It also comprises heat reclaim unit 52, ridge type inclined reciprocating fire grate 5, face arch 43, rear arch 44, oil burner 29, waste-liquor burner 30, described feeding device 10 is installed on the charging aperture 8 of burner hearth 40 left ends, heat reclaim unit 52 is located at the top of burner hearth 40, upper drum 17 in the heat reclaim unit 52 is arranged on the top of horizontal flue 41, lower drum 21 in the heat reclaim unit 52 is arranged on the top of horizontal flue 41, horizontal flue 41 is communicated with the upper end of burner hearth 40, ash handling equipment 50 is installed in the below of the lower drum 21 in the heat reclaim unit 52, back-end ductwork 42 is communicated with horizontal flue 41, air preheater 31 is installed in the back-end ductwork 42, air supply device 51 is arranged on the below of burner hearth 40 and is communicated with burner hearth 40, pipeline 55 in the air supply device 51 is communicated with the upper end of air preheater 31, ridge type inclined reciprocating fire grate 5 is arranged on the bottom face in the burner hearth 40, face arch 43 is arranged on the front wall in the burner hearth 40, rear arch 44 is arranged on the back wall in the burner hearth 40, oil burner 29, waste-liquor burner 30 is installed on the back wall of burner hearth 40 of rear arch 44 belows, the right-hand member bottom of burner hearth 40 is provided with mud hole 38, and the lower end of back-end ductwork 42 is provided with flue outlet 34.
The present invention has following beneficial effect: the present invention has efficiency of combustion height, equipment self can carry out burning disposal, the lower advantage of investment that heat recovery and utilization, equipment can adapt to various dissimilar hazardous wastes, also has advantages such as good airproof performance, simple in structure, processing ease, reliable, sufficient combustion simultaneously.The design of independent air compartment, ridge type inclined reciprocating fire grate makes the present invention be particularly suitable for burning hazardous waste.This incinerator can collect the burning hazardous waste and energy is used in one, is specially adapted to burn hazardous wastes such as industry or medical treatment.
Description of drawings
Fig. 1 is a front view of the present invention, and Fig. 2 is the A-A profile of Fig. 1, and Fig. 3 is the B-B profile of Fig. 1, and Fig. 4 is the C-C profile of Fig. 1, and Fig. 5 is the D-D profile of Fig. 1.
The specific embodiment
The specific embodiment one: shown in Fig. 1～5, the dangerous waste incineration device of present embodiment is by feeding device 10, burner hearth 40, ash handling equipment 50 and air preheater 31, air supply device 51, horizontal flue 41, back-end ductwork 42, heat reclaim unit 52, ridge type inclined reciprocating fire grate 5, face arch 43, rear arch 44, oil burner 29, waste-liquor burner 30 is formed, described feeding device 10 is installed on the charging aperture 8 of burner hearth 40 left ends, heat reclaim unit 52 is located at the top of burner hearth 40, upper drum 17 in the heat reclaim unit 52 is arranged on the top of horizontal flue 41, lower drum 21 in the heat reclaim unit 52 is arranged on the top of horizontal flue 41, horizontal flue 41 is communicated with the upper end of burner hearth 40, ash handling equipment 50 is installed in the below of the lower drum 21 in the heat reclaim unit 52, back-end ductwork 42 is communicated with horizontal flue 41, air preheater 31 is installed in the back-end ductwork 42, air supply device 51 is arranged on the below of burner hearth 40 and is communicated with burner hearth 40, pipeline 55 in the air supply device 51 is communicated with the upper end of air preheater 31, ridge type inclined reciprocating fire grate 5 is arranged on the bottom face in the burner hearth 40, face arch 43 is arranged on the front wall in the burner hearth 40, rear arch 44 is arranged on the back wall in the burner hearth 40, oil burner 29, waste-liquor burner 30 is installed on the back wall of burner hearth 40 of rear arch 44 belows, the right-hand member bottom of burner hearth 40 is provided with mud hole 38, and the lower end of back-end ductwork 42 is provided with flue outlet 34.
The air preheater 31 of present embodiment, oil burner 29, waste-liquor burner 30 are prior art.
Refuse experiences successively that drying, volatile matter are separated out, coke burns and the after-flame process.The combustion chamber of face arch 43 and rear arch 44 tops is for the fugitive constituent burning.Face arch 43 radiation with high temperature have just entered the refuse of burner hearth, make it dry and pyrolysis.Along with moving of ridge type inclined reciprocating fire grate 5, refuse moves to rear arch 44 belows, and refuse takes fire under the radiation of rear arch, and along with moving of fire grate, refuse moves forward to fire grate afterbody and all burnt, and slag falls into cinder hole.Be positioned at the oil burner and the waste-liquor burner of rear arch below.Treat incinerating waste material in the burner hearth igniting, the temperature of burner hearth is very low, and oil burner sprays into oil firing when igniting, make the temperature field that has to raise gradually in the burner hearth, each parts of protection incinerator.Waste-liquor burner is positioned at the below of oil burner, is used for the hazardous waste of combustion liquid and the liquid that solid-liquid separating machine is separated.Be provided with air preheater 31 in the back-end ductwork 42, utilize the waste heat of flue gas to add hot-air.
The specific embodiment two: as shown in Figure 1, the described air supply device 51 of present embodiment is made up of motor 54, independent air compartment 3, air blast 1, pipeline 55, air door 2, the output of described motor 54 is connected with pipeline 55, air blast 1 is communicated with pipeline 55, independent air compartment 3 is communicated with pipeline 55, and air door 2 is arranged on the independent air compartment 3.Adopt such design, can be according to the corresponding air quantity of different phase supply of trash burning, the air quantity of each air compartment can independent regulation.The combustion chamber of arch top, front and back is for the fugitive constituent burning.Other composition is identical with the specific embodiment one with annexation.
The specific embodiment three: as shown in Figure 1, be provided with four independent air compartments 3 in the described air supply device 51 of present embodiment.Adopt such structure, sufficient combustion, combustion efficiency the best.Other composition is identical with the specific embodiment two with annexation.
The specific embodiment four: shown in Fig. 1～5, the described heat reclaim unit 52 of present embodiment is by upper drum 17, first boiler tube bundle 16, second boiler tube bundle 20, lower drum 21, first down-comer 14, second down-comer, 37, front wall collection case 9, side wall collection case 15, back wall collection case 28, back wall tedge 26, front wall tedge 39, steam outlet valve 36 is formed, described front wall collection case 9 is arranged on the left end of face arch 43, side wall collection case 15 is arranged on the upper end of burner hearth 40, back wall collection case 28 is arranged on the right-hand member of rear arch 44, first boiler tube bundle 16 between upper drum 17 and side wall collection case 15 and with upper drum 17, side wall collection case 15 is communicated with respectively, second boiler tube bundle 20 between upper drum 17 and lower drum 21 and with upper drum 17, lower drum 21 is communicated with respectively, one end of first down-comer 14 is communicated with upper drum 17, the other end of first down-comer 14 is communicated with front wall collection case 9, one end of second down-comer 37 is communicated with lower drum 21, the other end of second down-comer 37 is communicated with back wall collection case 28, front wall tedge 39 is installed in the inner chamber of face arch 43, back wall tedge 26 is installed in the inner chamber of rear arch 44, and steam outlet valve 36 is installed on the upper drum 17.Adopt such structure, can make full use of and burn the heat that produces, and structure is simpler.Other composition is identical with the specific embodiment one with annexation.
The specific embodiment five: as shown in Figure 1, the described ridge type of present embodiment inclined reciprocating fire grate 5 by moving fire grate group 6, decide fire grate group 7, moving fire grate group connector 60, fire grate 4 and form, described moving fire grate group 6 with decide fire grate group 7 alternately, moving fire grate group connector 60 and moving fire grate group 6 are hinged, and the output of fire grate 4 is connected with moving fire grate group connector 60.The drive hazardous waste that moves forward and backward of moving fire grate group 6 moves forward on fire grate, close and the ridge platform variation just by the comb of ridge, realization is to the stirring of material, and improves the condition that material contacts with air, fully realizes the set up effect of dry thermal cracking and burning of material.Other composition is identical with the specific embodiment one with annexation.
The specific embodiment six: as shown in Figure 1, the described ash handling equipment 50 of present embodiment is made up of Machine for cleaning-out ash 27 and ash dropping hopper 23, blowing grey hole 19 is arranged on the horizontal flue 41, ash dropping hopper 23 is arranged on the below of lower drum 21, Machine for cleaning-out ash 27 is arranged on the below of ash dropping hopper 23, and described horizontal flue 41 is provided with gaging hole 18.Blow the flying dust of blowing down in grey hole 19 and be collected in 23 li of ash dropping hoppers, clear out of incinerator by Machine for cleaning-out ash 27.Other composition is identical with the specific embodiment one with annexation.
The specific embodiment seven: as shown in Figure 1 and Figure 2, present embodiment also comprises by-pass flue 35, and described by-pass flue 35 is arranged on the exit of the upper end of burner hearth 40.So design when checking that horizontal flue 41 or cigarette temperature are crossed high situation, can be played the effect of shunting flue gas.Other composition is identical with the specific embodiment one with annexation.
The specific embodiment eight: as shown in Figure 1, present embodiment also comprises secondary air channel 1, overfire air port 1, secondary air channel 2 25, overfire air port 2 24, secondary air channel 1 and overfire air port 1 are arranged on the top of face arch 43, and secondary air channel 2 25 and overfire air port 2 24 are arranged on the top of rear arch 44.So design for pyrolysis gas provides oxygen, and promotes mixing of oxygen and pyrolysis gas, promotes to burn and also emits a large amount of heats.Other composition is identical with the specific embodiment one with annexation.
The specific embodiment nine: as shown in Figure 1, present embodiment also comprises fire door 33, and described fire door 33 is arranged on behind the burner hearth on the wall 70, is provided with peephole 32 behind the burner hearth on the wall 70 in addition.So design is convenient to observe the combustion position in each stage.Other composition is identical with the specific embodiment one with annexation.
The specific embodiment ten: as shown in Figure 1, present embodiment also comprises combustion chamber fire door 11, flue damper 22, and described combustion chamber fire door 11 is arranged on the sidewall of burner hearth 40; Described flue damper 22 is arranged on the upper end of back-end ductwork 42.So design is convenient to refuse and is fully burnt.Other composition is identical with the specific embodiment one with annexation.
Operation principle:
By oil burner 29 igniting, burner hearth 40 is reached a high temperature and foot is lighted refuse, refuse is through after the preliminary treatment, enter burner hearth 40 by feeding device 10 by charging aperture 8, fall on the ridge type inclined reciprocating fire grate 5, fire grate 4 drives moving fire grate group 6 and moves forward and backward, and then the drive refuse moves.Refuse is under the hyperthermia radiation of face arch 43, and drying also decomposites fuel gas, and along with the motion of ridge type inclined reciprocating fire grate 5, refuse moves down and rolls and partial crushing.When refuse moves to rear arch 44 belows, have the refuse that the rear arch 44 radiation pyrolysis of high temperature finish, promote the burning of fixed carbon.Along with the difference of trash burning process, the corresponding air quantity of independent air compartment 3 dispensings guarantees fully carrying out of burning.Liquid waste directly sprays into burner hearth 40 burnings by waste-liquor burner 30, and the slag of all burnt is discharged burner hearth 40 by mud hole 38.Mud hole 38 tops are provided with peephole 32 and fire door 33.The gas that pyrolysis produces rises along burner hearth 40, burns under the effect of secondary wind supply oxygen simultaneously, emits heat.High-temperature flue gas parallel baffled first boiler tube bundle 16 backs arrive furnace outlet.Flue gas arrives back-end ductwork 42 along second boiler tube bundle 20 of horizontal flue 41 transversal flows connection upper drum 17 and lower drum 21.Flue gas washes away air preheater 31 at back-end ductwork 42, discharges incinerator by flue outlet 34 at last.
Enter upper drum 17 through the water that purifies, the part water in the upper drum 17 arrives front wall collection case 9 and side wall collection case 15 through first down-comer 14.Water in the front wall collection case 9 makes progress along the front wall tedge 39 that is arranged on the face arch 43, gets back to upper drum 17.Moisture in the side wall collection case 15 is fitted in first boiler tube bundle 16, is heated by radiation and convection current, finally arrives upper drum 17.Part water enters lower drum 21 through second boiler tube bundle 20 in the horizontal flue 41.Water in the lower drum 21 arrives back wall collection case 28 by second down-comer 37, rises along the back wall tedge on the rear arch 44 26, through burner hearth 40 outlets, arrives upper drum 17.The heat that absorbs the incinerator generation through the water that purifies becomes steam, and steam leaves incinerator by steam outlet valve 36, and water continue to participate in circulation (referring to Fig. 1～5) in upper drum 17 and the lower drum 21.
Claims (10)
1. dangerous waste incineration device, it comprises feeding device (10), burner hearth (40), ash handling equipment (50) and air preheater (31), air supply device (51), horizontal flue (41), back-end ductwork (42); It is characterized in that it also comprises heat reclaim unit (52), ridge type inclined reciprocating fire grate (5), face arch (43), rear arch (44), oil burner (29), waste-liquor burner (30), described feeding device (10) is installed on the charging aperture (8) of burner hearth (40) left end, heat reclaim unit (52) is located at the top of burner hearth (40), upper drum (17) in the heat reclaim unit (52) is arranged on the top of horizontal flue (41), lower drum (21) in the heat reclaim unit (52) is arranged on the below of horizontal flue (41), horizontal flue (41) is communicated with the upper end of burner hearth (40), ash handling equipment (50) is installed in the below of the lower drum (21) in the heat reclaim unit (52), back-end ductwork (42) is communicated with horizontal flue (41), air preheater (31) is installed in the back-end ductwork (42), air supply device (51) is arranged on the below of burner hearth (40) and is communicated with burner hearth (40), pipeline (55) in the air supply device (51) is communicated with the upper end of air preheater (31), ridge type inclined reciprocating fire grate (5) is arranged on the interior bottom face of burner hearth (40), face arch (43) is arranged on the interior front wall of burner hearth (40), rear arch (44) is arranged on the interior back wall of burner hearth (40), oil burner (29), waste-liquor burner (30) is installed on the back wall of the burner hearth (40) below the rear arch (44), the right-hand member bottom of burner hearth (40) is provided with mud hole (38), and the lower end of back-end ductwork (42) is provided with flue outlet (34).
2. dangerous waste incineration device according to claim 1, it is characterized in that described air supply device (51) is made up of motor (54), independent air compartment (3), air blast (1), pipeline (55), air door (2), the output of described motor (54) is connected with pipeline (55), air blast (1) is communicated with pipeline (55), independent air compartment (3) is communicated with pipeline (55), and air door (2) is arranged on the independent air compartment (3).
3. dangerous waste incineration device according to claim 2 is characterized in that being provided with in the described air supply device (51) four independent air compartments (3).
4. dangerous waste incineration device according to claim 1, it is characterized in that described heat reclaim unit (52) is by upper drum (17), first boiler tube bundle (16), second boiler tube bundle (20), lower drum (21), first down-comer (14), second down-comer (37), front wall collection case (9), side wall collection case (15), back wall collection case (28), back wall tedge (26), front wall tedge (39), steam outlet valve (36) is formed, described front wall collection case (9) is arranged on the left end of face arch (43), side wall collection case (15) is arranged on the upper end of burner hearth (40), back wall collection case (28) is arranged on the right-hand member of rear arch (44), first boiler tube bundle (16) be positioned between upper drum (17) and the side wall collection case (15) and with upper drum (17), side wall collection case (15) is communicated with respectively, second boiler tube bundle (20) be positioned between upper drum (17) and the lower drum (21) and with upper drum (17), lower drum (21) is communicated with respectively, one end of first down-comer (14) is communicated with upper drum (17), the other end of first down-comer 14 is communicated with front wall collection case (9), one end of second down-comer 37 is communicated with lower drum (21), the other end of second down-comer (37) is communicated with back wall collection case (28), front wall tedge (39) is installed in the inner chamber of face arch (43), back wall tedge (26) is installed in the inner chamber of rear arch (44), and steam outlet valve (36) is installed on the upper drum (17).
5. dangerous waste incineration device according to claim 1, it is characterized in that described ridge type inclined reciprocating fire grate (5) by moving fire grate group (6), decide fire grate group (7), moving fire grate group connector (60), fire grate (4) and form, described moving fire grate group (6) with decide fire grate group (7) alternately, moving fire grate group connector (60) is hinged with moving fire grate group (6), and the output of fire grate (4) is connected with moving fire grate group connector (60).
6. dangerous waste incineration device according to claim 3, it is characterized in that described ash handling equipment (50) is made up of Machine for cleaning-out ash (27) and ash dropping hopper (23), blowing grey hole (19) is arranged on the horizontal flue (41), ash dropping hopper (23) is arranged on the below of lower drum (21), Machine for cleaning-out ash (27) is arranged on the below of ash dropping hopper (23), and described horizontal flue (41) is provided with gaging hole (18).
7. dangerous waste incineration device according to claim 1 is characterized in that it also comprises by-pass flue (35), and described by-pass flue (35) is arranged on the exit of the upper end of burner hearth (40).
8. dangerous waste incineration device according to claim 1, it is characterized in that it also comprises secondary air channel one (12), overfire air port one (13), secondary air channel two (25), overfire air port two (24), secondary air channel one (12) and overfire air port one (13) are arranged on the top of face arch (43), and secondary air channel two (25) and overfire air port two (24) are arranged on the top of rear arch (44).
9. dangerous waste incineration device according to claim 1 is characterized in that it also comprises fire door (33), and described fire door (33) is arranged on behind the burner hearth on the wall (70), is provided with peephole (32) on the wall behind the burner hearth (70) in addition.
10. dangerous waste incineration device according to claim 1 is characterized in that it also comprises combustion chamber fire door (11), flue damper (22), and described combustion chamber fire door (11) is arranged on the sidewall of burner hearth (40); Described flue damper (22) is arranged on the upper end of back-end ductwork (42).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007101444014A CN100535521C (en) | 2007-09-30 | 2007-09-30 | Dangerous waste incineration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007101444014A CN100535521C (en) | 2007-09-30 | 2007-09-30 | Dangerous waste incineration device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101135454A true CN101135454A (en) | 2008-03-05 |
| CN100535521C CN100535521C (en) | 2009-09-02 |
Family
ID=39159686
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2007101444014A Expired - Fee Related CN100535521C (en) | 2007-09-30 | 2007-09-30 | Dangerous waste incineration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100535521C (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102128446A (en) * | 2011-01-24 | 2011-07-20 | 伟明环保设备有限公司 | Boiler for carrying out mixed combustion on carbon black tail gas and coal |
| CN102168853A (en) * | 2011-04-22 | 2011-08-31 | 哈尔滨工业大学 | Three-dimensional hierarchical air supply combined waste incinerator |
| CN102506405A (en) * | 2011-09-22 | 2012-06-20 | 哈尔滨工业大学 | Reciprocating grate boiler for medium-high voltage power station |
| CN102767823A (en) * | 2012-08-07 | 2012-11-07 | 上海应用技术学院 | Smokeless combustion system for zinc melting furnace |
| CN103148488A (en) * | 2013-04-08 | 2013-06-12 | 丁剑 | Reversed U-shaped two-section type fire grate hazardous waste incinerator |
| CN103791486A (en) * | 2012-10-30 | 2014-05-14 | 国惠环保新能源有限公司 | Stationary bed boiler preheated vertically and burnt sectionally at low temperature |
| CN105716093A (en) * | 2016-03-14 | 2016-06-29 | 哈尔滨工业大学 | Fusion device capable of simultaneously treating polymorphic hazardous wastes |
| CN106678829A (en) * | 2016-12-30 | 2017-05-17 | 安徽海螺川崎工程有限公司 | Incinerator fire grate structure |
| CN106765147A (en) * | 2017-01-13 | 2017-05-31 | 安徽未名鼎和环保有限公司 | A kind of refuse disposal system of stability and high efficiency |
| CN107036075A (en) * | 2017-06-05 | 2017-08-11 | 海伦市利民节能锅炉制造有限公司 | A kind of biomass molding fuel gasification combustion device continuously run |
| CN107238080A (en) * | 2017-06-30 | 2017-10-10 | 中国恩菲工程技术有限公司 | Waste melts disposal system |
| CN107363072A (en) * | 2017-06-30 | 2017-11-21 | 中国恩菲工程技术有限公司 | The fused bath smelting method of waste |
| CN108361716A (en) * | 2018-04-20 | 2018-08-03 | 大连航化能源装备有限公司 | A kind of three industrial wastes mixed combustion furnace |
| CN110360584A (en) * | 2019-07-17 | 2019-10-22 | 湖北长方缘环保设备有限公司 | A kind of anti-backfire automatic discharge boiler |
-
2007
- 2007-09-30 CN CNB2007101444014A patent/CN100535521C/en not_active Expired - Fee Related
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102128446A (en) * | 2011-01-24 | 2011-07-20 | 伟明环保设备有限公司 | Boiler for carrying out mixed combustion on carbon black tail gas and coal |
| CN102128446B (en) * | 2011-01-24 | 2012-11-21 | 伟明环保设备有限公司 | Boiler for carrying out mixed combustion on carbon black tail gas and coal |
| CN102168853A (en) * | 2011-04-22 | 2011-08-31 | 哈尔滨工业大学 | Three-dimensional hierarchical air supply combined waste incinerator |
| CN102168853B (en) * | 2011-04-22 | 2012-11-21 | 哈尔滨工业大学 | Three-dimensional hierarchical air supply combined waste incinerator |
| CN102506405A (en) * | 2011-09-22 | 2012-06-20 | 哈尔滨工业大学 | Reciprocating grate boiler for medium-high voltage power station |
| CN102767823A (en) * | 2012-08-07 | 2012-11-07 | 上海应用技术学院 | Smokeless combustion system for zinc melting furnace |
| CN103791486A (en) * | 2012-10-30 | 2014-05-14 | 国惠环保新能源有限公司 | Stationary bed boiler preheated vertically and burnt sectionally at low temperature |
| CN103791486B (en) * | 2012-10-30 | 2016-04-06 | 国惠环保新能源有限公司 | Vertical preheating segmentation low-temperature burning fixed bed boiler |
| CN103148488A (en) * | 2013-04-08 | 2013-06-12 | 丁剑 | Reversed U-shaped two-section type fire grate hazardous waste incinerator |
| CN105716093A (en) * | 2016-03-14 | 2016-06-29 | 哈尔滨工业大学 | Fusion device capable of simultaneously treating polymorphic hazardous wastes |
| CN106678829A (en) * | 2016-12-30 | 2017-05-17 | 安徽海螺川崎工程有限公司 | Incinerator fire grate structure |
| CN106765147A (en) * | 2017-01-13 | 2017-05-31 | 安徽未名鼎和环保有限公司 | A kind of refuse disposal system of stability and high efficiency |
| CN107036075A (en) * | 2017-06-05 | 2017-08-11 | 海伦市利民节能锅炉制造有限公司 | A kind of biomass molding fuel gasification combustion device continuously run |
| CN107036075B (en) * | 2017-06-05 | 2023-04-18 | 海伦市利民节能锅炉制造有限公司 | Biomass briquette gasification burner capable of continuously running |
| CN107036075B9 (en) * | 2017-06-05 | 2023-05-30 | 海伦市利民节能锅炉制造有限公司 | Continuously-running biomass briquette gasification burner |
| CN107238080A (en) * | 2017-06-30 | 2017-10-10 | 中国恩菲工程技术有限公司 | Waste melts disposal system |
| CN107363072A (en) * | 2017-06-30 | 2017-11-21 | 中国恩菲工程技术有限公司 | The fused bath smelting method of waste |
| CN107238080B (en) * | 2017-06-30 | 2023-01-24 | 中国恩菲工程技术有限公司 | Waste melting disposal system |
| CN108361716A (en) * | 2018-04-20 | 2018-08-03 | 大连航化能源装备有限公司 | A kind of three industrial wastes mixed combustion furnace |
| CN110360584A (en) * | 2019-07-17 | 2019-10-22 | 湖北长方缘环保设备有限公司 | A kind of anti-backfire automatic discharge boiler |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100535521C (en) | 2009-09-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100535521C (en) | Dangerous waste incineration device | |
| CN102607033B (en) | One way of life refuse gasification melting incineration system and incinerating method thereof | |
| CN101963356B (en) | Combustion system of vertical incinerator for household refuse suitable for power generation and control method thereof | |
| CN101561144B (en) | Clean incineration system of refuse and organic wastes and device thereof | |
| CN102168853B (en) | Three-dimensional hierarchical air supply combined waste incinerator | |
| CN106224974B (en) | Waste incineration processing system | |
| CN100432532C (en) | Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator | |
| CA2624054C (en) | A boiler producing steam from flue gases with high electrical efficiency and improved slag quality | |
| CN107726367A (en) | A kind of biomass granule fuel heating-cooking dual-purpose stove | |
| CN102759111A (en) | Garbage cracking furnace | |
| CN108613194A (en) | A kind of method and device for villages and small towns consumer waste incineration | |
| CS198243B2 (en) | Method of and apparatus for combusting wet waste fuel,especially of vegetal origin | |
| CN207646043U (en) | Municipal sludge desiccation pyrolytic gasification is controlled oneself incineration system | |
| CN106989400B (en) | A kind of application method of absorption VOCs exhaust gas solid waste accumulation of heat Boiling Combustion subsiding and purifying devices | |
| CN107023839B (en) | A kind of application method of processing absorption VOCs exhaust gas solid waste accumulation of heat fluidizing combustion furnaces | |
| CN109210539A (en) | A kind of bulky refuse incinerator | |
| WO1988002834A1 (en) | Furnace | |
| CN110986056B (en) | Multilayer fluidized bed incineration system and incineration method | |
| CN107023836B (en) | A kind of absorption VOCs exhaust gas solid waste accumulation of heat Boiling Combustion subsiding and purifying device | |
| CN201034321Y (en) | Burning decontamination plant treating life refuse by employing air-swept mill | |
| CN205746865U (en) | High temperature garbage gasification spray combustion tunnel system | |
| CN210511704U (en) | Multilayer fluidized bed burning system | |
| CN202056889U (en) | Boiler with rotary water-cooled grates | |
| CN201273569Y (en) | Rubbish and organic waste clean incineration system and equipment | |
| CN107987855A (en) | Box-like pyrolysis gasification furnace in one kind |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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 | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090902 Termination date: 20130930 |