CN110260334A - Waste incineration and system for cleaning fume - Google Patents

Waste incineration and system for cleaning fume Download PDF

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Publication number
CN110260334A
CN110260334A CN201910542002.6A CN201910542002A CN110260334A CN 110260334 A CN110260334 A CN 110260334A CN 201910542002 A CN201910542002 A CN 201910542002A CN 110260334 A CN110260334 A CN 110260334A
Authority
CN
China
Prior art keywords
flue gas
grate incinerator
grate
waste incineration
flue
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
CN201910542002.6A
Other languages
Chinese (zh)
Inventor
叶明�
曲云
钱海亮
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.)
WUXI HUAXING ELECTRIC POWER ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
Original Assignee
WUXI HUAXING ELECTRIC POWER ENVIRONMENTAL PROTECTION ENGINEERING Co 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 WUXI HUAXING ELECTRIC POWER ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd filed Critical WUXI HUAXING ELECTRIC POWER ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
Priority to CN201910542002.6A priority Critical patent/CN110260334A/en
Publication of CN110260334A publication Critical patent/CN110260334A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22DPREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
    • F22D1/00Feed-water heaters, i.e. economisers or like preheaters
    • F22D1/50Feed-water heaters, i.e. economisers or like preheaters incorporating thermal de-aeration of feed-water
    • 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
    • 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
    • F23J15/02Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L15/00Heating of air supplied for combustion
    • F23L15/04Arrangements of recuperators
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Treating Waste Gases (AREA)

Abstract

The present invention relates to a kind of waste incineration and system for cleaning fume, comprising the following steps: step S1: crawl is toppled over;Step S2: it burns;The auxiliary burner and start-up burner of grate incinerator are lighted a fire;Step S3: ash disposal;The lime-ash that grate incinerator burning generates is fallen on belt conveyor from the outlet of reserved ashes;Lime-ash is transported to ashpit by belt conveyor;Landfill yard is transported to by loading machine;Step S4: purification;The flue gas that grate incinerator burning generates enters the bottom of reaction tower from flue, by the aditus laryngis of flue and reaction tower ontology;Spray gun is set in aditus laryngis, the lime white of atomization is sprayed by spray gun, with flue gas neutralization reaction;Flue gas after reaction enters bag filter after connecting bridge is discharged under cyclone separator by top;Dust, which enters material returning device and returns to reaction tower, to be recycled;Step S5: curing process;Step S6: discharge.The present invention considers the factors such as economy and operation and maintenance, and the service life is long, good economy performance and does not generate secondary pollution.

Description

Waste incineration and system for cleaning fume
Technical field
The present invention relates to smoke, in particular to a kind of waste incineration and system for cleaning fume.
Background technique
With the rapid development of our country's economy, the continuous improvement of the level of urbanization and living standards of the people, refuse production Growing day by day, environmental pollution is getting worse for bring therefrom, and rubbish processing to be harmless disposition has become ecological environment neck The outstanding problem in domain.The rubbish growth rate in many cities is more than GDP speedup, faces the predicament of " garbage-surrounded city ".
Its energy resource utilization may be implemented in waste incineration, and volume reduction, reduced training are obvious, and processing speed is fast, is not required to Long term storage is wanted, is economized the land resource.The calorific value of rubbish is not only made full use of, and the harmful components that can be generated to burning pass through cigarette Gas processing system is focused on, and the pollution to environment is reduced.Waste incineration and generating electricity have become in the world processing rubbish and The mainstream technology of hazardous waste.
There are many pollutants in the flue gas that waste incineration generates, and need rationally to be purified, in order to avoid environment is generated secondary Pollution.Country has also promulgated that relevant criterion is made that limitation to Index for Garbage Incineration Smoke, mainly includes particulate matter, acidity Gas, dioxin and heavy metal etc..
Summary of the invention
In view of the deficiencies of the prior art, the invention discloses a kind of waste incineration and system for cleaning fume.
The technical solution adopted in the present invention is as follows:
A kind of waste incineration and system for cleaning fume, comprising the following steps:
Step S1: grabbing and topples over;Overhead crane control room manipulates the rubbish in garbage crane crawl garbage pool, the garbage pool Interior rubbish controls discharging by the chute door in discharging hall, and rubbish is poured in grate incinerator;
Step S2: it burns;Flue gas air preheater is heated empty needed for burning using the grate incinerator tail flue gas heat Gas, the primary air of flue gas air preheater heating replace a fire grate left side and the fire grate right side for grate incinerator described in forwards;Steam-air is pre- The steam taken out from steam turbine one is passed through in hot device, and the condensed water in steam air heater is by going oxygen-eliminating device to take away;It steams After vapour-air preheater heating auxiliary air each leads into stokehold and the furnace of the grate incinerator;On front side of grate incinerator Or the auxiliary burner of quadrangle and the start-up burner at grate incinerator rear are lighted a fire;Above the grate incinerator The waste heat recycling that is generated by grate incinerator of waste heat boiler can produce hot water or steam connects main steam pipe to supply it Its workshop section uses;
Step S3: ash disposal;The lime-ash that the grate incinerator burning generates falls in belt conveyor from the outlet of reserved ashes On;Lime-ash is transported to ashpit by belt conveyor;Landfill yard is transported to by loading machine;
Step S4: purification;The flue gas that the grate incinerator burning generates enters the bottom of reaction tower from flue, by cigarette The aditus laryngis in road and reaction tower ontology;Spray gun is set in the aditus laryngis, the lime white of atomization is sprayed by the spray gun, with the flue gas Neutralization reaction;Flue gas after reaction is entering bag filter after cyclone separator effect is discharged by top by connecting bridge; The material returning device that dust enters below cyclone separator returns to the reaction tower and recycles;
Step S5: curing process;The spiral that the byproduct that neutralization reaction generates passes through setting below the bag filter Conveyer is transported to embedded scraper transporter;Byproduct on embedded scraper transporter is fallen into container.
Its further technical characteristic are as follows: the garbage crane is two-beam bridge grab bucket crane.
Its further technical characteristic are as follows: in step sl, the sewage in the garbage pool flows into garbage leachate pond;Rubbish Sewage in cesspool is promoted to decontamination water treatment station by sewage pump.
Its further technical characteristic are as follows: in step s 4, the connection between the cyclone separator and bag filter Activated carbon storehouse is set on pipeline;Activated carbon is added in activated carbon storehouse, activated carbon is passed through in the bag filter.
Its further technical characteristic are as follows: the waste incineration and system for cleaning fume further include step S6: row It puts;Purified flue gas is passed through smoke stack emission by air-introduced machine.
Beneficial effects of the present invention are as follows:
1, the flue-gas temperature of heat boiler outlet is 180~220 DEG C, and the top of cyclone separator is entered by flue.Cigarette Ca (OH) of the gas after entering reaction tower, with the penetrating of high-speed rotating cyclone separator2Slurries are sufficiently mixed, in flue gas The sour gas such as SO, HCl and Ca (OH)2It is removed after carrying out neutralization reaction, meanwhile, flue-gas temperature is lowered to 155 DEG C or so.
2, lower part of the treated flue gas through cyclone separator enters bag filter by connecting flue.From reaction tower After out, flue gas enters sack cleaner after being cooled to about 155 DEG C.On flue between cyclone separator and bag filter Equipped with active carbon storehouse.Neutralization reaction occurs for the sour gas in the carbon powder and flue gas that active carbon storehouse ejects, it is ensured that any Moment acid gas emissions are up to standard.
Detailed description of the invention
Fig. 1 is flow chart of the invention.
Fig. 2 is schematic diagram of the invention.
In figure: 1, chute door;2, garbage pool;3, garbage crane;4, flue gas air preheater;5, sewage pump;6, grate incinerator; 7, waste heat boiler;8, steam air heater;9, belt conveyor;10, ashpit;11, loading machine;12, reaction tower;13, it sprays Rifle;14, cyclone separator;15, bag filter;16, material returning device;17, screw conveyor;18, embedded scraper transporter;19, collect Vanning;20, activated carbon storehouse;21, air-introduced machine;22, chimney;23, garbage leachate pond;24, mucking machine.
Specific embodiment
Aforementioned and other technology contents, feature and effect of the invention are closed, in following cooperation with reference to attached drawing to embodiment In detailed description, can clearly it present.The direction term being previously mentioned in following embodiment, such as: upper and lower, left and right, it is preceding or Afterwards etc., it is only the direction with reference to attached drawing.Therefore, the direction term used is intended to be illustrative and not intended to limit the present invention, in addition, In whole embodiments, identical drawing reference numeral indicates identical element.
With reference to the accompanying drawing, illustrate the specific embodiment of the present embodiment.
Fig. 1 is flow chart of the invention.Fig. 2 is schematic diagram of the invention.A kind of waste incineration and gas cleaning processing system System.The following steps are included:
Step S1: grabbing and topples over.Overhead crane control room manipulates the rubbish in the crawl garbage pool 2 of garbage crane 3.Garbage pool 2 Volume be 6823m3, L × B × H=59m × 17.4m × 8.4m of garbage pool 2.Rubbish in garbage pool 2 is by discharging hall Chute door 1 control discharging, rubbish is poured in grate incinerator 6.W × H=3.8m of chute door 1 × 4.5m.Garbage pool 2 Interior sewage flows into garbage leachate pond 23.The volume in garbage leachate pond 23 is 350m3, the L × B × H=20m in garbage leachate pond 23 ×7m×2.5m.Sewage in garbage leachate pond 23 is promoted to decontamination water treatment station by sewage pump 5.Preferably.Garbage crane 3 For two-beam bridge grab bucket crane.
Step S2: it burns.Air needed for flue gas air preheater 4 heats burning using 6 tail flue gas heat of grate incinerator. A fire grate left side for the primary air alternating forwards grate incinerator 6 that flue gas air preheater 4 heats and fire grate are right.Steam air heater 8 Inside it is passed through the steam taken out from steam turbine one.Steam air heater 8 is tubular heat exchanger, and fin is ellipse.And it steams Condensed water in vapour-air preheater 8 is by going oxygen-eliminating device to take away.The auxiliary air that steam air heater 8 heats leads to respectively After the stokehold and the furnace that enter grate incinerator 6.6 rear of auxiliary burner and grate incinerator of 6 front side of grate incinerator or quadrangle Start-up burner light a fire.Waste heat boiler 7 above grate incinerator 6 passes through the waste heat that grate incinerator 6 generates Recycling can produce hot water or steam connects main steam pipe to supply other workshop sections and use.The pipeline and steam-of flue gas air preheater 4 Electric butterfly valve is set on the pipeline of air preheater 8.
Hydraulic device acts on hopper baffle, dispenser, fire grate and the ash-pushing machine of grate incinerator 6.
Step S3: ash disposal.The lime-ash that the burning of grate incinerator 6 generates is fallen on belt conveyor 9 from the outlet of reserved ashes. Lime-ash is transported to ashpit 10 by mucking machine 24 by belt conveyor 9.Landfill yard is transported to by loading machine 11.
Step S4: purification.The flue gas that the burning of grate incinerator 6 generates enters the bottom of reaction tower 12 from flue.By cigarette The aditus laryngis of 12 ontology of road and reaction tower.In aditus laryngis, spray gun 13 is set.The lime white of atomization is sprayed by spray gun 13.With it is in flue gas and anti- It answers.Flue gas after reaction is entering bag filter 15 after the effect of cyclone separator 14 is discharged by top by connecting bridge.Rotation Activated carbon storehouse 20 is set on the connecting line between wind separator 14 and bag filter 15.Activity is added in activated carbon storehouse 20 Carbon.Activated carbon is passed through in bag filter 15.The material returning device 16 that dust enters 14 lower section of cyclone separator returns to reaction tower 12 and follows Ring utilizes.Flue gas enters the bottom of reaction tower 12 from flue, by aditus laryngis (the cone junction of 12 ontology of flue and reaction tower Point), in aditus laryngis, spray gun 13 is set, thus the lime white of atomization sprays into, since throat section product reduces, the speed of fluid increases, Highly turbulent and air-liquid mixing is generated, the dust of entrained with is mixed among drop in gas, after fluid passes through throat, speed It reduces, is sufficiently reacted convenient for sour gas with lime white.Gas after reaction is acted on by connecting bridge through cyclone separator 14 Enter bag filter 15 after being discharged by top, and dust then enters material returning device 16 and returns to reaction tower 12 and recycles, and passes through object Interior circulation and powerful outer circulation (Matter Transfer number is about at 30~100 times) in reaction tower 12 are expected, so that absorbent With SO2Mass transfer exchange between equal sour gas is strong, and the mass transport process in absorbent is strong, and solid material is in reaction tower 12 Residence time reaches 30-60 minutes, and running temperature can be down near dew point, to substantially increase the utilization rate of absorbent and take off Sulphur rate.The moisture sprayed into neutralizing tower simultaneously evaporates at high temperature, reduces flue-gas temperature, makes the acidity in reactant and flue gas The reaction that gas occurs is more violent, improves gas cleaning efficiency, on the other hand, flue gas can also be made to enter bag filter When temperature control within tolerance band.In lower Ca/S ratio (Ca/S=1.1-1.5), desulfurization degree can be greater than 85%.End reaction object is discharged by 1 bottom of reaction tower and 16 top of material returning device.
Star-shaped dust-discharging valve is arranged in the exit of bag filter 15.
Step S5: curing process.The byproduct that neutralization reaction generates passes through the spiral transferring being arranged below bag filter 15 It send in the transport to embedded scraper transporter 18 of machine 17.Byproduct on embedded scraper transporter 18 is fallen into container 19.
Step S6: discharge.Purified flue gas is passed through the discharge of chimney 22 by air-introduced machine 21.
The present invention considers the factors such as economy and operation and maintenance, and the service life is long, good economy performance and does not generate secondary pollution.
Above description is explanation of the invention, is not intended to limit the invention, and limited range of the present invention is referring to right It is required that the present invention can make any type of modification without prejudice to basic structure of the invention.

Claims (5)

1. a kind of waste incineration and system for cleaning fume, it is characterised in that the following steps are included:
Step S1: grabbing and topples over;Overhead crane control room manipulates the rubbish in garbage crane (3) crawl garbage pool (2), the rubbish Rubbish in pond (2) controls discharging by the chute door (1) in discharging hall, and rubbish is poured in grate incinerator (6);
Step S2: it burns;Flue gas air preheater (4) is heated needed for burning using the grate incinerator (6) tail flue gas heat Air, the primary air of flue gas air preheater (4) heating replace a fire grate left side and the fire grate right side for grate incinerator (6) described in forwards;It steams The steam taken out from steam turbine one is passed through in vapour-air preheater (8), and the condensed water in steam air heater (8) is by going Oxygen-eliminating device is taken away;Steam air heater (8) heating auxiliary air each lead into the grate incinerator (6) stokehold and After furnace;On front side of grate incinerator (6) or the start-up burner at auxiliary burner and grate incinerator (6) rear of quadrangle carries out a little Fire;The waste heat recycling that waste heat boiler (7) above the grate incinerator (6) is generated by grate incinerator (6) can be with Production hot water or steam connect main steam pipe to supply other workshop sections and use;
Step S3: ash disposal;The lime-ash that grate incinerator (6) burning generates falls in belt conveyor from the outlet of reserved ashes (9) on;Lime-ash is transported to ashpit (10) by belt conveyor (9);Landfill yard is transported to by loading machine (11);
Step S4: purification;The flue gas that grate incinerator (6) burning generates enters the bottom of reaction tower (12), warp from flue Cross the aditus laryngis of flue and reaction tower (12) ontology;Spray gun (13) are set in the aditus laryngis, the lime white of atomization is by the spray gun (13) it sprays into, with the flue gas neutralization reaction;Flue gas after reaction is acted on through cyclone separator (14) by pushing up by connecting bridge Enter bag filter (15) after portion's discharge;The material returning device (16) that dust enters below cyclone separator (14) returns to the reaction Tower (12) recycles;
Step S5: curing process;The spiral that the byproduct that neutralization reaction generates passes through setting below the bag filter (15) In conveyer (17) transport to embedded scraper transporter (18);Byproduct on embedded scraper transporter (18) falls into container (19) In.
2. waste incineration according to claim 1 and system for cleaning fume, it is characterised in that: the garbage crane It (3) is two-beam bridge grab bucket crane.
3. waste incineration according to claim 1 and system for cleaning fume, it is characterised in that: in step sl, institute The sewage stated in garbage pool (2) flows into garbage leachate pond (23);Sewage in garbage leachate pond (23) is promoted by sewage pump (5) To decontamination water treatment station.
4. waste incineration according to claim 1 and system for cleaning fume, it is characterised in that: in step s 4, institute State setting activated carbon storehouse (20) on the connecting line between cyclone separator (14) and bag filter (15);Activated carbon storehouse (20) Interior addition activated carbon, activated carbon are passed through in the bag filter (15).
5. waste incineration according to claim 1 and system for cleaning fume, it is characterised in that: the waste incineration and System for cleaning fume further includes step S6: discharge;Purified flue gas is passed through chimney (22) row by air-introduced machine (21) It puts.
CN201910542002.6A 2019-06-21 2019-06-21 Waste incineration and system for cleaning fume Pending CN110260334A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910542002.6A CN110260334A (en) 2019-06-21 2019-06-21 Waste incineration and system for cleaning fume

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Application Number Priority Date Filing Date Title
CN201910542002.6A CN110260334A (en) 2019-06-21 2019-06-21 Waste incineration and system for cleaning fume

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Publication Number Publication Date
CN110260334A true CN110260334A (en) 2019-09-20

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111380058A (en) * 2020-03-31 2020-07-07 无锡市华星东方电力环保科技有限公司 Waste incineration system with waste heat recovery device
CN113719838A (en) * 2021-08-28 2021-11-30 江苏仙盛环保科技有限公司 Smoke purification furnace and operation method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101042239A (en) * 2007-02-12 2007-09-26 中联实业股份有限公司 Wind system of garbage incinerator
CN202494116U (en) * 2012-01-09 2012-10-17 厦门坤跃环保有限公司 Municipal-waste-incinerating power-generating comprehensive treatment system
JP6319931B1 (en) * 2018-02-23 2018-05-09 株式会社タクマ Palm EFB pyrolysis gasification power generation system
CN207514917U (en) * 2017-10-20 2018-06-19 世纪华扬环境工程有限公司 Waste incineration and generating electricity device
CN108679614A (en) * 2018-06-14 2018-10-19 南京凯盛开能环保能源有限公司 A kind of cement kiln synergic processing house refuse electricity generation system and method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101042239A (en) * 2007-02-12 2007-09-26 中联实业股份有限公司 Wind system of garbage incinerator
CN202494116U (en) * 2012-01-09 2012-10-17 厦门坤跃环保有限公司 Municipal-waste-incinerating power-generating comprehensive treatment system
CN207514917U (en) * 2017-10-20 2018-06-19 世纪华扬环境工程有限公司 Waste incineration and generating electricity device
JP6319931B1 (en) * 2018-02-23 2018-05-09 株式会社タクマ Palm EFB pyrolysis gasification power generation system
CN108679614A (en) * 2018-06-14 2018-10-19 南京凯盛开能环保能源有限公司 A kind of cement kiln synergic processing house refuse electricity generation system and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111380058A (en) * 2020-03-31 2020-07-07 无锡市华星东方电力环保科技有限公司 Waste incineration system with waste heat recovery device
CN113719838A (en) * 2021-08-28 2021-11-30 江苏仙盛环保科技有限公司 Smoke purification furnace and operation method thereof

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Application publication date: 20190920