CN109654502A - A method of using hot plate furnace Direct Disposal multiphase solid waste - Google Patents

A method of using hot plate furnace Direct Disposal multiphase solid waste Download PDF

Info

Publication number
CN109654502A
CN109654502A CN201810535001.4A CN201810535001A CN109654502A CN 109654502 A CN109654502 A CN 109654502A CN 201810535001 A CN201810535001 A CN 201810535001A CN 109654502 A CN109654502 A CN 109654502A
Authority
CN
China
Prior art keywords
hot plate
solid waste
plate furnace
furnace
kiln
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.)
Pending
Application number
CN201810535001.4A
Other languages
Chinese (zh)
Inventor
张应中
泥卫东
沈序辉
唐盛伟
陈美男
张小军
薛朝辉
金彩珍
梁国勋
莫正选
蒋文伟
张春辉
周轮
李琦
周家顺
孙幸福
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ai Fa Smith Co Ltd
Environmental Protection Engineering Co Ltd
Huarun Environmental Protection Engineering Investment Ltd
Original Assignee
Ai Fa Smith Co Ltd
Environmental Protection Engineering Co Ltd
Huarun Environmental Protection Engineering Investment Ltd
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 Ai Fa Smith Co Ltd, Environmental Protection Engineering Co Ltd, Huarun Environmental Protection Engineering Investment Ltd filed Critical Ai Fa Smith Co Ltd
Priority to CN201810535001.4A priority Critical patent/CN109654502A/en
Publication of CN109654502A publication Critical patent/CN109654502A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/033Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/442Waste feed arrangements
    • F23G5/444Waste feed arrangements for solid waste
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/02Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material

Abstract

The invention discloses a kind of methods using hot plate furnace Direct Disposal multiphase solid waste.The following steps are included: A, different solid waste pass through effective inner diameter of pipeline in the round or rectangular solid waste blanking pipe of 800~1400mm, pipeline can be independent, it is also possible to common three air valves of close discharging end side configuration in entrance hot plate boiler tube road, controls the incorporation of cold wind;B, hot plate furnace configures Multipoint temperature detecting device, and cement kiln tail C4 blanking system is transformed, and absorbs thermal control temperature using carbonate decomposition of the hot raw material of C4 on hot plate furnace;C, it introduces into the cold raw material of kiln elevator as emergency fire-fighting equipment, for the stable operation for guaranteeing kiln system, mating setting bypass facility;D, the transformation of hot plate furnace is implanted in cement kiln tail uptake flue to decomposition furnace bottom vertebra portion region;Solid waste burns uncombusted remains in hot plate furnace, falls into cement kiln uptake flue continuous high temperature incineration disposal.The present invention realizes the great-leap-forward progress using hot plate furnace Direct Disposal ecosystem urban and rural domestic refuse, the application of hot plate furnace has been expanded, it can be achieved that simple and reliable using a variety of solid wastes, processing methods such as the synchronous disposition house refuse of hot plate furnace, sludge, industrial solid wastes, safety and environmental protection, it is at low cost.

Description

A method of using hot plate furnace Direct Disposal multiphase solid waste
Technical field
The present invention relates to Solid Waste Treatment technical fields, and in particular to a kind of to use hot plate furnace Direct Disposal multiphase The method of solid waste.
Background technique
Traditional incinerator is used for cement kiln synergic processing waste, and the solid waste object of processing is relatively simple, answers The higher cost of incinerator processing solid waste narrow with object range and traditional, equipment is more, and energy consumption is high, coal conservation It is less, not environmentally, and then result in low in economic efficiency.
In conclusion the present invention devises a kind of method using hot plate furnace Direct Disposal multiphase solid waste.
Summary of the invention
In view of the shortcomings of the prior art, using hot plate furnace Direct Disposal the purpose of the invention is to provide a kind of The method of multiphase solid waste realizes the great-leap-forward progress using hot plate furnace Direct Disposal ecosystem urban and rural domestic refuse, opens up The application of hot plate furnace has been opened up, it can be achieved that a variety of using the synchronous disposition house refuse of hot plate furnace, sludge, industrial solid wastes etc. Solid waste, processing method is simple and reliable, safety and environmental protection, at low cost.
To achieve the goals above, the present invention is to realize by the following technical solutions: a kind of direct using hot plate furnace The method for disposing multiphase solid waste, comprising the following steps:
A, current stabilization is fed: different solid waste is by effective inner diameter of pipeline under the round or rectangular solid waste of 800~1400mm Pipe material, pipeline can be it is independent, be also possible to it is common, enter hot plate boiler tube road close discharging end side configure three Air valve controls the incorporation of cold wind;
B, hot plate furnace configures Multipoint temperature detecting device, cement kiln tail C4 blanking system is transformed, using the hot raw material of C4 in hot plate Carbonate decomposition on furnace absorbs thermal control temperature;
C, it introduces into the cold raw material of kiln elevator as emergency fire-fighting equipment, for the stable operation for guaranteeing kiln system, by mating setting Leak informaton facility on road;
D, the transformation of hot plate furnace is implanted in cement kiln tail uptake flue to decomposition furnace bottom vertebra portion region;Solid waste is in hot plate furnace Burn uncombusted remains, falls into cement kiln uptake flue continuous high temperature incineration disposal.
It is only passed through preferably, the different solid waste in the step A can be ecosystem urban and rural domestic refuse That crosses simple crushing reaches 90% < 160~200mm of granularity, is also possible to ecosystem urban and rural domestic refuse, is in pretreatment System is prepared into moisture < 40%, the city of 90% < 160~200mm of granularity by techniques preprocessing process such as broken, biological dewatered, extruding Township's house refuse;It can also be the domestic sludge or industrial sludge mud cake squeezed by sheet frame, 90% < 300mm of granularity;In particle To crumby industrial waste, independent storage is then needed to configure if it is dangerous waste waste, conveying facility is fed, granularity 90%<300mm。
Beneficial effects of the present invention: realize great-leap-forward using hot plate furnace Direct Disposal ecosystem urban and rural domestic refuse into Step has expanded the application of hot plate furnace, it can be achieved that using the synchronous disposition house refuse, sludge, industrial solid wastes of hot plate furnace Etc. a variety of solid wastes, processing method is simple and reliable, and safety and environmental protection is at low cost.
Detailed description of the invention
Fig. 1 is flow chart of the invention;Wherein 1, hot plate furnace;2, solid waste blanking pipe;3, three air valve;4, temperature is examined Survey device;5,C4;6, C4 blanking system;7, enter kiln elevator;8, cement kiln;9, bypass facility;10, uptake flue;11, Dore furnace;12, dore furnace tapering;13, it grabs bucket;14, plate feeds machine;15, weighing belt;16, rubber conveyer;17, solid waste feeder pipe Road;18, air seal set;19, feeding-distribution device;20, smoke-box slope;21, air bubble;22, deodoration system;23, pretreatment workshop; 24,C5;25, kiln tail smokestack.
Specific embodiment
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below with reference to Specific embodiment, the present invention is further explained.
Referring to Fig.1, present embodiment uses following technical scheme: a kind of to use hot plate furnace Direct Disposal multiphase solid The method of waste, comprising the following steps:
A, current stabilization is fed: different solid waste is by effective inner diameter of pipeline under the round or rectangular solid waste of 800~1400mm Pipe material, pipeline can be it is independent, be also possible to it is common, enter hot plate boiler tube road close discharging end side configure three Air valve controls the incorporation of cold wind;
B, hot plate furnace configures Multipoint temperature detecting device, cement kiln tail C4 blanking system is transformed, using the hot raw material of C4 in hot plate Carbonate decomposition on furnace absorbs thermal control temperature;
C, it introduces into the cold raw material of kiln elevator as emergency fire-fighting equipment, for the stable operation for guaranteeing cement kiln, by mating setting Leak informaton facility on road;
D, the transformation of hot plate furnace is implanted in cement kiln tail uptake flue to decomposition furnace bottom vertebra portion region;Solid waste is in hot plate furnace Burn uncombusted remains, falls into cement kiln uptake flue continuous high temperature incineration disposal.
It is worth noting that, the different solid waste in the step A can be ecosystem urban and rural domestic refuse Reach 90% < 160~200mm of granularity merely through simple crushing, is also possible in advance to locate ecosystem urban and rural domestic refuse Reason system is prepared into moisture < 40%, 90% < 160~200mm of granularity by techniques preprocessing process such as broken, biological dewatered, extruding Urban and rural domestic refuse;It can also be the domestic sludge or industrial sludge mud cake squeezed by sheet frame, 90% < 300mm of granularity;It is in Particle then needs to configure independent storage if it is dangerous waste waste, conveying facility is fed, grain to crumby industrial waste Spend 90% < 300mm.
It is worth noting that, the detailed process that the current stabilization of the step A is fed are as follows:
(1) using multiple blowing operation of grabbing bucket, and machine is fed in lower section configuration plate and is fed, guarantee material metering and transport process In, the basis equalization of flow is stablized, and reduces in transmission process and blanking process, and stream concentrates the technology accident wind for causing blocking Danger.
(2) plate feeds the configuration of the conveying equipments such as machine, weighing belt, rubber conveyer using angle steel as skeleton, is formed using transparent material close Sealing cover seals all transloading equipments setting equipment, and guarantee leaks without foul smell.
(3) for all devices according to 5~12m spacing configure air draft pipe, suction opening pipe diameter DN350~ 500, by maintaining -5~-8Pa of equipment negative pressure after sealing, realize to all effective capture containing gas with foreign flavor.
(4) different for multiphase solid waste granularity, and exist and glue wet component and easily winding braided fabric, solid waste blanking pipe Inside castable refractory uses smooth surface disposal type template, and it is several to reduce bridging of the solid waste in pipeline by using this template Rate.
(5) in order to reduce leaking into for a large amount of cold wind of solid waste blanking pipe, discharging point configuration is non-above solid waste blanking pipe Marking device seals suction opening, and necessary positive pressure jet port is arranged;By the open and close of three valves, sealed using the material of material Lock wind.
It is worth noting that, the detailed process of described step B, C, D are as follows:
(1) in C4 feeding-distribution device along the motion profile tangential direction of valve, the clear blowpipe hole of compressed air is configured, periodic, Inhibit thermal material skinning on the inside of valve body, improves the reliability of valve working.
(2) it according to the mating bypass system of the ratio of kiln ventilation quantity 3~8%, controls because having caused by cooperative disposal waste Evil element is enriched in high-temperature area, influences the stability of manufacture of cement.
(3) on hot plate furnace body, dore furnace vertebra portion, uptake flue, smoke-box slope etc. because cooperative disposal waste easily forms knot The region of skin configures one layer of air bubble, tangential direction annular configuration of the air bubble along flow cross-sectional according to every 1~1.8m.
(4) hot plate furnace body, dore furnace vertebra portion, uptake flue, smoke-box slope castable use anti-strip high strength type Castable.
(5) kiln tail smoke-box slope increases the configuration of castable anchoring piece according to 150~200% level of encryption, and selection is discarded Cooler grate plate be welded on the fixed form on anchoring piece as castable construction, increase shock resistance of the slope to bulk blanking Ability.
In addition, the environmentally friendly disposal process of the step D are as follows:
(1) device is maintained to all transloading equipments of solid waste setting negative pressure, reinforcing sealing is carried out to equipment, it is mating and perfect negative Air draft pipe is pressed, is collected all on the spot containing peculiar smell, dusty gas, system is centrally disposed by heating and ventilating pipeline feeding.
(2) the similar gas for converging pretreatment workshop containing peculiar smell, dusty gas collected in solid waste transloading equipment leads to It crosses after heating and ventilating pipeline completes directional collecting, cement kiln is sent into when cement producing line runs well as combustion air incineration disposal, Matched professional deodoration system, the qualified discharge after disposing then are sent into when cement kiln is stopped transport.
(3) according to the combustion characteristics for entering hot plate furnace material, revolving speed, the ignition temperature, ventilation quantity of hot plate furnace is adjusted, is stablized Ignition temperature is at 900~1050 DEG C, air-fuel ratio 7.5~9.5,3~20 turn/hour of revolving speed, it is ensured that enters manufacture of cement high-temperature region The all materials in domain are thermal material, optimize burning condition, realize the abundant decomposition of organic pollutant.
(4) enter the SO of the hot raw material of kiln according to C53、Cl、M2O content detection data, switch bypass leak informaton system.Bypass The kiln ash of system carries out heavy metal, the analysis test of harmful element access, is dissolved after closing rule as cement grinding mill mixing material.Bypass The discharge of kiln tail smokestack is imported after the tails dedusting that leaks informaton purification.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its Equivalent thereof.

Claims (5)

1. a kind of method using hot plate furnace Direct Disposal multiphase solid waste, which comprises the following steps:
(A) current stabilization is fed: different solid waste is by effective inner diameter of pipeline under the round or rectangular solid waste of 800~1400mm Pipe material (2), pipeline can be it is independent, be also possible to it is common, enter hot plate boiler tube road close discharging end side configuration Three air valves (3), control the incorporation of cold wind;
(B) cement kiln tail C4(5 is transformed in hot plate furnace (1) configuration Multipoint temperature detecting device (4)) blanking system (6), utilize C4 (5) carbonate decomposition of the hot raw material on hot plate furnace (1) absorbs thermal control temperature;
(C) it introduces into the cold raw material of kiln elevator (7) as emergency fire-fighting equipment, it is mating for the stable operation for guaranteeing kiln (8) system It is arranged bypass facility (9);
(D) hot plate furnace (1) transformation is implanted in cement kiln (8) Uptake flue at kiln end (10) to dore furnace (11) bottom vertebra portion (12) area Domain;The solid waste remains uncombusted in hot plate furnace (1) burning, fall at cement kiln uptake flue (10) continuous high temperature burning It sets.
2. a kind of method using hot plate furnace Direct Disposal multiphase solid waste according to claim 1, which is characterized in that Different solid waste in the step (A) reach granularity merely through simple crushing for ecosystem urban and rural domestic refuse 90% < 160~200mm's, or by ecosystem urban and rural domestic refuse, in pretreatment system by broken, biological dewatered, extruding Etc. techniques preprocessing process be prepared into moisture < 40%, the urban and rural domestic refuse of 90% < 160~200mm of granularity;Or pass through sheet frame The domestic sludge or industrial sludge mud cake of extruding, 90% < 300mm of granularity;Or in particle to crumby industrial waste, dangerous waste Waste then needs to configure independent storage, conveying facility is fed, 90% < 300mm of granularity.
3. a kind of method using hot plate furnace Direct Disposal multiphase solid waste according to claim 1, which is characterized in that The detailed process of the current stabilization feed of the step (A) are as follows:
(1) using grab bucket (13) repeatedly blowing operation, and machine (14) are fed in lower section configuration plate and are fed, guarantee material metering and In transport process, the basis equalization of flow is stablized, and reduces stream in transmission process and blanking process and concentrates the technique for causing blocking Accident risk;
(2) plate feeds the conveying equipments configuration such as machine (14), weighing belt (15), rubber conveyer (16) using angle steel as skeleton, using saturating Bright material forms seal closure, seals to all transloading equipments setting equipment, guarantee is revealed outward without foul smell;
(3) air draft pipe is configured according to the spacing of 5~12m for all devices, suction opening pipe diameter leads in DN350~500 Overstocked be honored as a queen maintains equipment negative pressure in -5~-8Pa, realizes to all effective capture containing gas with foreign flavor;
(4) different for multiphase solid waste granularity, and exist and glue wet component and easily winding fibre object, solid waste blanking pipe (17) Inside castable refractory uses smooth surface disposal type template, and it is several to reduce bridging of the solid waste in pipeline by using such template Rate;
(5) in order to reduce leaking into for a large amount of cold wind of solid waste blanking pipe (2), the discharging point configuration above solid waste blanking pipe (2) Non-standard equipment seals suction opening, and necessary positive pressure jet port (18) is arranged;Pass through the open and close of three valves (3), benefit Wind is blocked with the material of material.
4. a kind of method using hot plate furnace Direct Disposal multiphase solid waste according to claim 1, which is characterized in that The detailed process of described step B, C, D are as follows:
(1) in C4(5) feeding-distribution device (19) along the motion profile tangential direction of valve, determine by the configuration clear blowpipe hole of compressed air Phase operation inhibits thermal material skinning on the inside of valve body, improves the reliability of valve working;
(2) it according to the mating bypass system (9) of the ratio of kiln ventilation quantity 3~8%, controls because having caused by cooperative disposal waste Evil element is enriched in high-temperature area, influences the stability of manufacture of cement;
(3) in hot plate furnace body (1), dore furnace vertebra portion (12), uptake flue (10), smoke-box slope (20) etc. because cooperative disposal is useless The region that object easily forms skinning configures one layer of air bubble (21) according to every 1~1.8m, and air bubble is along the tangent line side of flow cross-sectional To annular configuration;
(4) hot plate furnace body (1), dore furnace vertebra portion (12), uptake flue (10), smoke-box slope (20) castable use anti-stripping Drop height intensity type castable;
(5) kiln tail smoke-box slope (20) increase the configuration of castable anchoring piece according to 150~200% level of encryption, and selection is discarded Cooler grate plate be welded on the fixed form on anchoring piece as castable construction, increase shock resistance of the slope to bulk blanking Ability.
5. a kind of method using hot plate furnace Direct Disposal multiphase solid waste according to claim 1, which is characterized in that The environmentally friendly disposal process of the step D are as follows:
(1) device is maintained to all transloading equipments of solid waste setting negative pressure, reinforcing sealing is carried out to equipment, comprehensive is negative Air draft pipe is pressed, is collected all on the spot containing peculiar smell, dusty gas, system is centrally disposed by heating and ventilating pipeline feeding (22);
(2) the similar gas for converging pretreatment workshop (23) containing peculiar smell, dusty gas collected in solid waste transloading equipment, leads to After crossing heating and ventilating pipeline completion directional collecting, cement kiln (8) are sent into when cement producing line runs well as at combustion air burning It sets, matched professional deodoration system (22), the qualified discharge after disposing then is sent into when cement kiln is stopped transport;
(3) according to the combustion characteristics for entering hot plate furnace (1) material, revolving speed, the ignition temperature, ventilation quantity of hot plate furnace (1) are adjusted, surely Ignition temperature is determined at 900~1050 DEG C, air-fuel ratio is 7.5~9.5, and revolving speed is in 3~20 turns/hour, it is ensured that enter manufacture of cement High-temperature area all materials are thermal material, optimize burning condition, realize the abundant decomposition of organic pollutant;
(4) enter the SO of the hot raw material of kiln according to C5(24)3、Cl、M2O content detection data, switch bypass leak informaton system (9);Bypass is put The kiln ash of wind system (9) carries out heavy metal, the analysis test of harmful element access, disappears after closing rule as cement grinding mill mixing material It receives;Kiln tail smokestack (25) discharge is imported after the purification of bypass (9) tails dedusting.
CN201810535001.4A 2018-05-30 2018-05-30 A method of using hot plate furnace Direct Disposal multiphase solid waste Pending CN109654502A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810535001.4A CN109654502A (en) 2018-05-30 2018-05-30 A method of using hot plate furnace Direct Disposal multiphase solid waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810535001.4A CN109654502A (en) 2018-05-30 2018-05-30 A method of using hot plate furnace Direct Disposal multiphase solid waste

Publications (1)

Publication Number Publication Date
CN109654502A true CN109654502A (en) 2019-04-19

Family

ID=66110193

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810535001.4A Pending CN109654502A (en) 2018-05-30 2018-05-30 A method of using hot plate furnace Direct Disposal multiphase solid waste

Country Status (1)

Country Link
CN (1) CN109654502A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110566971A (en) * 2019-10-11 2019-12-13 成都铭炬环保工程技术有限公司 Device and method for cooperatively treating various wastes in cement kiln
CN112254134A (en) * 2020-10-15 2021-01-22 成都建筑材料工业设计研究院有限公司 System and method for cooperatively treating household garbage by using cement kiln
CN112728545A (en) * 2020-12-23 2021-04-30 蓝天众成环保工程有限公司 Online hot plate furnace cooperative hazardous waste disposal device and use method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050039638A1 (en) * 2000-02-08 2005-02-24 Ching Chiu Leung Method and process for co-combustion in a waste to-energy facility
WO2013143450A1 (en) * 2012-03-30 2013-10-03 杭州恒明环境技术有限公司 Municipal solid waste treatment and utilization system
CN204494414U (en) * 2015-03-03 2015-07-22 中建材(北京)环保工程发展有限公司 Hot pan burner burner
CN205402733U (en) * 2016-02-19 2016-07-27 武汉建筑材料工业设计研究院有限公司 Domestic waste and/or industrial waste's processing production line
CN106322387A (en) * 2015-06-18 2017-01-11 中建材(北京)环保工程发展有限公司 Rubbish disposal method
CN107339702A (en) * 2017-04-06 2017-11-10 蓝天众成环保工程有限公司 A kind of method of cement kiln synergic processing urban and rural domestic refuse

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050039638A1 (en) * 2000-02-08 2005-02-24 Ching Chiu Leung Method and process for co-combustion in a waste to-energy facility
WO2013143450A1 (en) * 2012-03-30 2013-10-03 杭州恒明环境技术有限公司 Municipal solid waste treatment and utilization system
CN204494414U (en) * 2015-03-03 2015-07-22 中建材(北京)环保工程发展有限公司 Hot pan burner burner
CN106322387A (en) * 2015-06-18 2017-01-11 中建材(北京)环保工程发展有限公司 Rubbish disposal method
CN205402733U (en) * 2016-02-19 2016-07-27 武汉建筑材料工业设计研究院有限公司 Domestic waste and/or industrial waste's processing production line
CN107339702A (en) * 2017-04-06 2017-11-10 蓝天众成环保工程有限公司 A kind of method of cement kiln synergic processing urban and rural domestic refuse

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110566971A (en) * 2019-10-11 2019-12-13 成都铭炬环保工程技术有限公司 Device and method for cooperatively treating various wastes in cement kiln
CN110566971B (en) * 2019-10-11 2024-04-05 成都铭炬环保工程技术有限公司 Device and method for cooperatively disposing various wastes in cement kiln
CN112254134A (en) * 2020-10-15 2021-01-22 成都建筑材料工业设计研究院有限公司 System and method for cooperatively treating household garbage by using cement kiln
CN112254134B (en) * 2020-10-15 2021-11-30 成都建筑材料工业设计研究院有限公司 System and method for cooperatively treating household garbage by using cement kiln
CN112728545A (en) * 2020-12-23 2021-04-30 蓝天众成环保工程有限公司 Online hot plate furnace cooperative hazardous waste disposal device and use method thereof

Similar Documents

Publication Publication Date Title
CN104759203B (en) A kind of fluidized-bed process of directly trapping mineralising carbon dioxide in flue gas and system
CN102381877B (en) Method for brickmaking by comprehensive utilization of desiccated sludge
US20070251433A1 (en) Method and plant for processing waste
CN102070308B (en) Device technology configuration method for treating house refuses by using rotary cement kiln
CN1270988C (en) Sludge burning treatment method and system
CN109654502A (en) A method of using hot plate furnace Direct Disposal multiphase solid waste
CN109987813B (en) Oily sludge pyrolysis treatment system
CN106440838A (en) Calcium carbide furnace purification ash gas conveying and incineration device
JP5003036B2 (en) Waste treatment method and apparatus in a calciner
CN102294340A (en) Harmless treatment system for city refuse burning, and method thereof
CN106693629A (en) System and method for reducing output of waste incineration fly ash
CN104633667A (en) Incineration disposal and comprehensive utilization production technology for household rubbish
CN204756944U (en) High -efficient dust removal deodorization waste incinerator
CN105674281B (en) A kind of fuel is from supply type waste disposal method
CN104310732B (en) A kind of sludge high temperature plasma vitrifying device and treatment process thereof
CN208332267U (en) A kind of refuse pyrolysis treatment device with prebake
CN205782951U (en) A kind of environment protection garbage incineration device
CN206222951U (en) Furnace of calcium carbide purification ash gas conveying incinerator
CN204918383U (en) One set of raw material roll -in refuse handling installation
CN206504334U (en) A kind of temperature garbage pyrolysis oven
CN101413667B (en) Method for processing urban domestic garbage of kiln external incineration furnace
CN103759272B (en) Mud mixture burning control system and control method thereof
CN107477568A (en) A kind of ashes recovery type environment-friendly boiler
CN100364907C (en) Sludge drying system using combination of smoke residual heat and two external heat supply sources
CN203682639U (en) Closed pebble coal collecting and discharging system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination