CN110296421A - A kind of solid waste melting disposal system and its method - Google Patents

A kind of solid waste melting disposal system and its method Download PDF

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Publication number
CN110296421A
CN110296421A CN201910449012.5A CN201910449012A CN110296421A CN 110296421 A CN110296421 A CN 110296421A CN 201910449012 A CN201910449012 A CN 201910449012A CN 110296421 A CN110296421 A CN 110296421A
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CN
China
Prior art keywords
solid waste
melting furnace
storage facility
additive
control system
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
CN201910449012.5A
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Chinese (zh)
Inventor
邢立淑
杨华
张毅杰
曹彤
杨帆
孙钟华
田君国
李要建
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.)
Jiangsu Tianying Environmental Protection Energy Equipment Co Ltd
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Jiangsu Tianying Environmental Protection Energy Equipment Co Ltd
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Application filed by Jiangsu Tianying Environmental Protection Energy Equipment Co Ltd filed Critical Jiangsu Tianying Environmental Protection Energy Equipment Co Ltd
Priority to CN201910449012.5A priority Critical patent/CN110296421A/en
Publication of CN110296421A publication Critical patent/CN110296421A/en
Pending legal-status Critical Current

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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
    • 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
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/04Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
    • 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
    • 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
    • F23G5/50Control or safety arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • 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
    • 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
    • F23J15/06Arrangements of devices for treating smoke or fumes of coolers

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)

Abstract

The invention discloses a kind of solid waste melting disposal system and its methods, the discharge port of pretreatment system is connect with the feed inlet of solid waste storage facility, the discharge port of solid waste storage facility and the discharge port of additive storage facility are connect with two feed inlets of mixing arrangement respectively, the discharge port of mixing arrangement is connect with the feed inlet of melting furnace system, monitor on-line LIBS device respectively with pretreatment system, solid waste storage facility is connected with additive storage facility for monitoring solid waste ingredient on-line, control system respectively with on-line monitoring LIBS device, solid waste storage facility is connected with additive storage facility to be used to calculate additive additive amount by solid waste ingredient and controls the additive amount of additive.The present invention is realized solid waste and it can be formed with on-line checking before entering melting furnace, is realized automatic compatibility, is melted solid waste adequately, it is ensured that unharmful substance is discharged with slag.

Description

A kind of solid waste melting disposal system and its method
Technical field
The present invention relates to a kind of melting disposal system and its method, especially a kind of solid waste melting disposal system and its Method.
Background technique
With the rapid development of industry, the yield of solid waste increases year by year, causes serious harm to environment.Largely Solid waste be discharged into environment, not only land occupation, but also ambient enviroment will also be caused sternly in solid waste containing heavy metal It destroys again, while seriously threatening the health of the mankind.
Traditional solid waste burning processing is mainly rotary kiln and cement kiln synergic processing, and melt process is current fixed-end forces The new technology of development, mostly uses greatly " pretreatment+compatibility+melt process+gas cleaning " method of disposal, and the source of solid waste is multiple Miscellaneous, composition fluctuation is big, therefore needs to carry out detailed analysis of physical and chemical feature to solid waste before handling.But traditional sampling Analysis method detection cycle is long, and there are two defects: one, solid waste carries out the side of chemical composition analysis before entering melting furnace In method, it is unable to real-time control due to spending overlong time, is difficult to carry out stable melt process, if without adequately melting, Harmful substance will be discharged together with slag, cause the Environmental security quality of melting and solidification body (Leaching) not up to standard;Two, should Method lacks the control to melting furnace operating condition (such as deslagging temperature), excessively high not only to cause heat waste, while reducing melting furnace And service life of refractory material, it is too low then exist cannot smoothly deslagging risk.
Summary of the invention
Technical problem to be solved by the invention is to provide a kind of solid waste melting disposal system and its methods, guarantee solid The abundant melting of body waste.
In order to solve the above technical problems, the technical scheme adopted by the invention is that:
A kind of solid waste melting disposal system, it is characterised in that: include pretreatment system, solid waste storage facility, addition Developing agent storage device, mixing arrangement, on-line monitoring LIBS device, control system and melting furnace system, the discharge port of pretreatment system It is connect with the feed inlet of solid waste storage facility, the discharging of the discharge port and additive storage facility of solid waste storage facility Mouth is connect with two feed inlets of mixing arrangement respectively, and the discharge port of mixing arrangement is connect with the feed inlet of melting furnace system, Line monitoring LIBS device is connect respectively for supervising online with pretreatment system, solid waste storage facility and additive storage facility Solid waste ingredient is surveyed, control system is filled with on-line monitoring LIBS device, solid waste storage facility and addition developing agent storage respectively Connection is set to be used to calculate additive additive amount by solid waste ingredient and control the additive amount of additive.
Further, in-furnace temperature monitoring device, deslagging temperature monitoring device and electricity are provided on the melting furnace system Source, in-furnace temperature monitoring device are arranged in melting furnace system for the temperature inside real-time monitoring melting furnace, deslagging temperature prison It surveys device and temperature of the slag-drip opening of melting furnace system for real-time monitoring melting furnace slag-drip opening slag, power supply and melting furnace is set System connection is for controlling the operating power of melting furnace system, in-furnace temperature monitoring device, deslagging temperature monitoring device and power supply It connect with control system and is controlled by control system respectively.
Further, the melting furnace system is provided with flue gas purification system, and flue gas purification system is arranged in melting furnace system On the exhaust vent of system.
Further, the pretreatment system is crushed solid waste, is dried, granularity after solid waste is broken No more than 5cm, moisture content is not more than 10%.
Further, the solid waste storage facility, additive storage facility discharge port be provided with meter.
Further, the temperature of the melting furnace system is maintained at 1300-1700 DEG C.
Further, the in-furnace temperature monitoring device uses pyrometer couple, and deslagging temperature monitoring device is using infrared Temperature measurer.
A kind of solid waste melting method of disposal, it is characterised in that comprise the steps of:
Step 1: solid waste is pre-processed in pretreatment system;
Step 2: solid waste is sent into solid waste storage facility and is kept in after pretreatment, will be in solid waste storage facility Solid waste be added mixing arrangement in, then monitor on-line LIBS device monitoring solid waste component, which is fed back To control system, control system controls additive storage facility and additive is added, and on-line monitoring LIBS device continues monitoring mixing It component and repeats the above steps in device, until mixing arrangement component and control system preset group split-phase are the same as completing solid waste Compatibility;
Step 3: melting furnace system is added in the good solid waste of compatibility, is melted, is produced at a high temperature of 1300-1700 DEG C Raw molten state waste residue is discharged from bottom slag discharge, and the exhaust gas of generation discharges after being purified by flue gas purification system.
Further, solid waste is sent into solid waste storage facility and is carried out temporarily after the step 2 specially pre-processes It deposits, the solid waste in solid waste storage facility is added in mixing arrangement, then monitor LIBS device on-line and monitor solid The component is fed back to control system, melts optimal proportion to various types of solid waste in control system by the component of waste It is preset, control system receives solid waste component information and carries out identification to the information to judge solid waste For which type of solid waste, then according to judging that structure reads preset optimal proportion and by preset ratio and solid waste Measurement component compare, calculate corresponding difference and obtain needing the dosage of each additive to be added, control system control Additive is added according to calculated result in additive storage facility processed, while monitoring LIBS device on-line and continuing to monitor in mixing arrangement Component simultaneously repeats the above steps, until mixing arrangement component and control system preset group split-phase are the same as the compatibility for completing solid waste.
Further, the step 3 is specially that melting furnace system is added in the good solid waste of compatibility, in 1300-1700 It is melted at a high temperature of DEG C, the molten state waste residue of generation is discharged from bottom slag discharge, and the exhaust gas of generation is passed through gas cleaning system System discharges after waste heat recycling, deacidification, flying dust collection and denitration process, in solid waste melting process, in-furnace temperature prison It surveys device and acquires the melting temperature melted in furnace system in real time, deslagging temperature monitoring device acquires melting furnace system bottom row in real time The slag temperature of cinder notch, control system adjust the operating power of power supply according to the melting temperature in melting furnace system, control simultaneously System is modified power work power according to slag temperature, and control system is added in melting furnace system according to mixing arrangement The quality of compatibility solid waste carries out preposition amendment to power control.
Compared with prior art, the present invention having the following advantages that and effect:
1, the present invention can dispose a plurality of types of solid waste, including bottom ash, flying dust, electroplating sludge, wirerope sludge Deng;
2, the present invention is realized solid waste and it can be formed with on-line checking before entering melting furnace, and real automatic compatibility keeps solid useless Object adequately melts, it is ensured that unharmful substance is discharged with slag;
3, the present invention is in melting furnace and temperature monitoring device is arranged in slag-drip opening, in melting furnace and deslagging temperature is monitored; The present invention is by being obtained in the real-time component of solid waste and melting furnace using control system and deslagging real time temperature controls melting Furnace operating state can extend the service life of melting furnace and resistance to material again while guaranteeing that melting furnace is stable.
Detailed description of the invention
Fig. 1 is a kind of schematic diagram of solid waste melting disposal system of the invention.
Fig. 2 is the power control logic figure of the embodiment of the present invention.
Specific embodiment
Below by embodiment, the present invention is described in further detail, following embodiment be explanation of the invention and The invention is not limited to following embodiments.
As shown in Figure 1, a kind of solid waste of the invention melts disposal system, store comprising pretreatment system, solid waste Cryopreservation device, additive storage facility, mixing arrangement, on-line monitoring LIBS device, control system and melting furnace system, pretreatment system The discharge port of system is connect with the feed inlet of solid waste storage facility, the discharge port and addition developing agent storage of solid waste storage facility The discharge port of device is connect with two feed inlets of mixing arrangement respectively, the charging of the discharge port and melting furnace system of mixing arrangement Mouth connection, on-line monitoring LIBS device are connect with pretreatment system, solid waste storage facility and additive storage facility respectively For monitoring solid waste ingredient on-line, control system respectively with on-line monitoring LIBS device, solid waste storage facility and add Add the connection of developing agent storage device to be used to calculate additive additive amount by solid waste ingredient and controls the additive amount of additive.
In-furnace temperature monitoring device, deslagging temperature monitoring device and power supply, in-furnace temperature prison are provided on melting furnace system It surveys device to be arranged in melting furnace system for the temperature inside real-time monitoring melting furnace, the setting of deslagging temperature monitoring device is molten The slag-drip opening for melting furnace system is used for the temperature of real-time monitoring melting furnace slag-drip opening slag, and power supply is connect with melting furnace system for controlling System melting furnace system operating power, in-furnace temperature monitoring device, deslagging temperature monitoring device and power supply respectively with control system Connection is controlled by control system.Melting furnace system is provided with flue gas purification system, and flue gas purification system setting is in melting furnace system Exhaust vent on.
Pretreatment system is crushed solid waste, is dried, and granularity is not more than 5cm after solid waste is broken, contains Water rate is not more than 10%.Solid waste storage facility, additive storage facility discharge port be provided with meter.Melting furnace system The temperature of system is maintained at 1300-1700 DEG C.In-furnace temperature monitoring device uses pyrometer couple, and deslagging temperature monitoring device uses Infrared radiation thermometer.
A kind of solid waste melting method of disposal comprising the steps of:
Step 1: solid waste is pre-processed in pretreatment system;Solid waste is successively crushed, is dried, it is right Solid waste carries out break process, and granularity is not more than 5cm, broken waste is thermally dried, moisture content is not more than 10%。
Step 2: solid waste is sent into solid waste storage facility and is kept in after pretreatment, and solid waste is stored and is filled Solid waste in setting is added in mixing arrangement, the component of LIBS device monitoring solid waste is then monitored on-line, by the component Control system is fed back to, various types of solid waste melting optimal proportion is preset in control system, control system connects It receives solid waste component information and identification is carried out to the information to judge that solid waste gives up for which type of solid Object, then according to judging that structure reads preset optimal proportion and carry out the measurement component of preset ratio and solid waste pair Than calculating corresponding difference and obtaining needing the dosage of each additive to be added, control system controls additive storage facility Additive is added according to calculated result, while monitoring LIBS device on-line and continuing to monitor component in mixing arrangement and repeat above-mentioned step Suddenly, until mixing arrangement component and control system preset group split-phase are the same as the compatibility for completing solid waste.
Step 3: melting furnace system is added in the good solid waste of compatibility, is melted at a high temperature of 1300-1700 DEG C Melt, the molten state waste residue of generation is discharged from bottom slag discharge, forms vitreum after water cooled, the exhaust gas of generation is passed through gas cleaning System is recycled by waste heat, is discharged after deacidification, flying dust collection and denitration process, in solid waste melting process, in-furnace temperature Monitoring device acquires the melting temperature in melting furnace system in real time, and deslagging temperature monitoring device acquires melting furnace system bottom in real time The slag temperature of slag-drip opening, control system adjust the operating power of power supply, same time control according to the melting temperature in melting furnace system System processed is modified power work power according to slag temperature, and control system is added in melting furnace system according to mixing arrangement The quality of compatibility solid waste preposition amendment is carried out to power control.
Power supply adjustment process is, as shown in Fig. 2, being decomposed according to serials control to be feedovered
Feedover revise signal are as follows: M*F1 (s);
Tandem inner looping output are as follows: Y2=(Y1-T2) * G2 (s);
Tandem external loop output are as follows: Y1=(R-T1) * G1 (s);
System always exports are as follows: Y=Y2+M*F1 (s)=[(R-T1) * G1 (s)-T2] * G2 (s)+M*F1 (s);
Wherein, M be measurement obtain enter furnace solid waste quality, F1 (s) is front feeding transfer function, and G1 (s) is that tandem external loop transmits Function, G2 (s) are tandem inner looping transmission function, and R is melting furnace temperature setting value, and T1 is melting furnace temperature, and T2 is slag temperature.
The present invention can dispose a plurality of types of solid waste, including the dirt of bottom ash, flying dust, electroplating sludge, wirerope Mud etc.;The present invention is realized solid waste and it can be formed with on-line checking before entering melting furnace, realizes automatic compatibility, keeps solid useless Object adequately melts, it is ensured that unharmful substance is discharged with slag;The present invention is in melting furnace and slag-drip opening setting temperature monitoring fills It sets, in melting furnace and deslagging temperature is monitored;The present invention by using control system obtain the real-time component of solid waste and In melting furnace and deslagging real time temperature controls melting furnace operating state, can extend again while guaranteeing that melting furnace is stable The service life of melting furnace and resistance to material.
Above content is only illustrations made for the present invention described in this specification.Technology belonging to the present invention The technical staff in field can do various modifications or supplement or is substituted in a similar manner to described specific embodiment, only It should belong to guarantor of the invention without departing from the content or beyond the scope defined by this claim of description of the invention Protect range.

Claims (10)

1. a kind of solid waste melts disposal system, it is characterised in that: comprising pretreatment system, solid waste storage facility, add Add developing agent storage device, mixing arrangement, on-line monitoring LIBS device, control system and melting furnace system, the discharging of pretreatment system Mouth is connect with the feed inlet of solid waste storage facility, the discharge port of solid waste storage facility and going out for additive storage facility Material mouth is connect with two feed inlets of mixing arrangement respectively, and the discharge port of mixing arrangement is connect with the feed inlet of melting furnace system, On-line monitoring LIBS device is connect respectively for online with pretreatment system, solid waste storage facility and additive storage facility Monitor solid waste ingredient, control system respectively with on-line monitoring LIBS device, solid waste storage facility and addition developing agent storage Device connection is used to calculate additive additive amount by solid waste ingredient and controls the additive amount of additive.
2. a kind of solid waste described in accordance with the claim 1 melts disposal system, it is characterised in that: on the melting furnace system It is provided with in-furnace temperature monitoring device, deslagging temperature monitoring device and power supply, in-furnace temperature monitoring device is arranged in melting furnace system For the temperature inside real-time monitoring melting furnace in system, the slag-drip opening that melting furnace system is arranged in deslagging temperature monitoring device is used for The temperature of real-time monitoring melting furnace slag-drip opening slag, power supply connect the work function for controlling melting furnace system with melting furnace system Rate, in-furnace temperature monitoring device, deslagging temperature monitoring device and power supply connect with control system controlled by control system respectively.
3. a kind of solid waste described in accordance with the claim 1 melts disposal system, it is characterised in that: the melting furnace system is set It is equipped with flue gas purification system, flue gas purification system is arranged on the exhaust vent of melting furnace system.
4. a kind of solid waste described in accordance with the claim 1 melts disposal system, it is characterised in that: the pretreatment system pair Solid waste is crushed, is dried, and granularity is not more than 5cm after solid waste is broken, and moisture content is not more than 10%.
5. a kind of solid waste described in accordance with the claim 1 melts disposal system, it is characterised in that: the solid waste storage Device, additive storage facility discharge port be provided with meter.
6. a kind of solid waste described in accordance with the claim 1 melts disposal system, it is characterised in that: the melting furnace system Temperature is maintained at 1300-1700 DEG C.
7. a kind of solid waste melts disposal system according to claim 2, it is characterised in that: the in-furnace temperature monitoring Device uses pyrometer couple, and deslagging temperature monitoring device uses infrared radiation thermometer.
8. a kind of solid waste melts method of disposal, it is characterised in that comprise the steps of:
Step 1: solid waste is pre-processed in pretreatment system;
Step 2: solid waste is sent into solid waste storage facility and is kept in after pretreatment, will be in solid waste storage facility Solid waste be added mixing arrangement in, then monitor on-line LIBS device monitoring solid waste component, which is fed back To control system, control system controls additive storage facility and additive is added, and on-line monitoring LIBS device continues monitoring mixing It component and repeats the above steps in device, until mixing arrangement component and control system preset group split-phase are the same as completing solid waste Compatibility;
Step 3: melting furnace system is added in the good solid waste of compatibility, is melted, is produced at a high temperature of 1300-1700 DEG C Raw molten state waste residue is discharged from bottom slag discharge, and the exhaust gas of generation discharges after being purified by flue gas purification system.
9. a kind of solid waste melts method of disposal according to claim 8, it is characterised in that: the step 2 is specially Solid waste is sent into solid waste storage facility and is kept in after pretreatment, and the solid waste in solid waste storage facility is added Enter in mixing arrangement, then monitors the component of LIBS device monitoring solid waste on-line, which is fed back into control system, control Various types of solid waste melting optimal proportion is preset in system processed, control system receives solid waste component letter It ceases and identification is carried out to the information to judge that solid waste is which type of solid waste, then according to judging structure It reads preset optimal proportion and compares the measurement component of preset ratio and solid waste, calculate corresponding difference simultaneously Obtain needing the dosage of each additive to be added, control system controls additive storage facility and addition is added according to calculated result Agent, while monitoring LIBS device on-line and continuing to monitor component in mixing arrangement and repeat the above steps, until mixing arrangement component With control system preset group split-phase with the compatibility for completing solid waste.
10. a kind of solid waste melts method of disposal according to claim 8, it is characterised in that: the step 3 is specific For melting furnace system is added in the good solid waste of compatibility, melted at a high temperature of 1300-1700 DEG C, the molten state of generation Waste residue from bottom slag discharge be discharged, the exhaust gas of generation be passed through flue gas purification system by waste heat recycling, deacidification, flying dust collect and It is discharged after denitration process, in solid waste melting process, in-furnace temperature monitoring device acquires the melting in melting furnace system in real time Temperature, deslagging temperature monitoring device acquire the slag temperature of melting furnace system bottom slag-drip opening in real time, and control system is according to melting Melting temperature in furnace system adjusts the operating power of power supply, at the same control system according to slag temperature to power work power into The quality of row amendment, the compatibility solid waste that control system is added in melting furnace system according to mixing arrangement controls power Carry out preposition amendment.
CN201910449012.5A 2019-05-28 2019-05-28 A kind of solid waste melting disposal system and its method Pending CN110296421A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111468524A (en) * 2020-05-09 2020-07-31 广东飞南资源利用股份有限公司 Multi-metal recovery system, method and device
CN114811596A (en) * 2022-04-29 2022-07-29 江苏锦明再生资源有限公司 Dry sludge treatment cleaning incinerator

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008096067A (en) * 2006-10-13 2008-04-24 Takuma Co Ltd Control method for plasma melting furnace
CN204730190U (en) * 2015-04-22 2015-10-28 大唐武安发电有限公司 A kind of dynamic self-adapting control system of CFBB lime stone feeding coal
CN206494912U (en) * 2017-02-28 2017-09-15 江苏华旭环保股份有限公司 A kind of integrated high-temperature gasification device handled available for hazardous waste
CN107366913A (en) * 2017-07-07 2017-11-21 南京福昌环保有限公司 A kind of compatibility processing method based on incineration of waste
CN108435751A (en) * 2018-03-11 2018-08-24 沈阳银海再生资源科技有限公司 A kind of aluminium electroloysis waste lining is innoxious and resource utilization method and device
CN109253453A (en) * 2018-09-28 2019-01-22 新中天环保股份有限公司 A kind of pre-treatment medicine compatibility method of hazardous waste

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008096067A (en) * 2006-10-13 2008-04-24 Takuma Co Ltd Control method for plasma melting furnace
CN204730190U (en) * 2015-04-22 2015-10-28 大唐武安发电有限公司 A kind of dynamic self-adapting control system of CFBB lime stone feeding coal
CN206494912U (en) * 2017-02-28 2017-09-15 江苏华旭环保股份有限公司 A kind of integrated high-temperature gasification device handled available for hazardous waste
CN107366913A (en) * 2017-07-07 2017-11-21 南京福昌环保有限公司 A kind of compatibility processing method based on incineration of waste
CN108435751A (en) * 2018-03-11 2018-08-24 沈阳银海再生资源科技有限公司 A kind of aluminium electroloysis waste lining is innoxious and resource utilization method and device
CN109253453A (en) * 2018-09-28 2019-01-22 新中天环保股份有限公司 A kind of pre-treatment medicine compatibility method of hazardous waste

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111468524A (en) * 2020-05-09 2020-07-31 广东飞南资源利用股份有限公司 Multi-metal recovery system, method and device
CN111468524B (en) * 2020-05-09 2021-08-03 广东飞南资源利用股份有限公司 Multi-metal recovery system, method and device
CN114811596A (en) * 2022-04-29 2022-07-29 江苏锦明再生资源有限公司 Dry sludge treatment cleaning incinerator
CN114811596B (en) * 2022-04-29 2023-01-31 江苏锦明再生资源有限公司 Dry sludge treatment cleaning incinerator

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Application publication date: 20191001