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 PDFInfo
- 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
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- China
- Prior art keywords
- hot plate
- solid waste
- plate furnace
- furnace
- kiln
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements 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
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.
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Cited By (3)
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)
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 |
-
2018
- 2018-05-30 CN CN201810535001.4A patent/CN109654502A/en active Pending
Patent Citations (6)
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)
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 |
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