CN101498455A - Process technique for incineration tail gas of medical waste, hazardous waste and consumer waste - Google Patents

Process technique for incineration tail gas of medical waste, hazardous waste and consumer waste Download PDF

Info

Publication number
CN101498455A
CN101498455A CNA2008101974053A CN200810197405A CN101498455A CN 101498455 A CN101498455 A CN 101498455A CN A2008101974053 A CNA2008101974053 A CN A2008101974053A CN 200810197405 A CN200810197405 A CN 200810197405A CN 101498455 A CN101498455 A CN 101498455A
Authority
CN
China
Prior art keywords
tail gas
cooling
gas
temperature
waste
Prior art date
Application number
CNA2008101974053A
Other languages
Chinese (zh)
Other versions
CN100584434C (en
Inventor
尹加强
王久高
惠阳
张庆
张向
谢荣
尹礼加
尹礼平
Original Assignee
黄石市祥和环保设备有限责任公司
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 黄石市祥和环保设备有限责任公司 filed Critical 黄石市祥和环保设备有限责任公司
Priority to CN200810197405A priority Critical patent/CN100584434C/en
Publication of CN101498455A publication Critical patent/CN101498455A/en
Application granted granted Critical
Publication of CN100584434C publication Critical patent/CN100584434C/en

Links

Classifications

    • Y02E20/363

Abstract

The invention relates to the technical field of environment protection, in particular to a process for treating the incineration tail gas of medical waste, dangerous waste and domestic garbage. The process flow comprises the following steps: (1) firstly cooling tail gas discharged from ht-air chambers of two combustion chambers of an incinerator to 650-700 DEG C by an air cooler; (2) cooling the tail gas to not higher than 600 DEG C by a cold-smoke-gas heat-exchanger; (3) cooling the tail gas to not higher than 500 DEG C by a water cooler; (4) sharply cooling the tail gas to not higher than 200 DEG C in one minute by a primary middle-temperature fast quench tower and continuously washing and cooling the cooling the tail gas to not higher than 80 DEG C through a duplex base of the fast quench tower; (5) cooling the tail gas to not higher than 50 DEG C through neutralization and absorption in a secondary washing and deacidifying tower; (6) cooling the tail gas to not higher than 35 DEG C through condensation and dehydration; (7) drying and absorbing the cooling the tail gas at low temperature; (8) backing to the cold-smoke-gas heat-exchanger in the step (2) to heat the tail gas to 70-90 DEG C; (8) and finally dedusting by a cloth bag; and (10) exhausting the purified tail gas by an exhaust system. The invention solves the problems of incomplete purifying treatment, failures of high-temperature neutralization reaction and high-temperature absorption, low efficiency and poor effect in the prior tail gas treatment process and is especially suitable for treating harmful incineration tail gas of medical waste, dangerous waste and domestic garbage.

Description

Clinical waste, hazardous waste, consumer waste incineration tail gas treatment process

(1) technical field:

The present invention relates to environmental technology field, is a kind of clinical waste, hazardous waste, consumer waste incineration tail gas treatment process.

(2) background technology:

Clinical waste, hazardous waste, the tail gas of house refuse after burning contain a large amount of harmful substances, deal with improperly, will cause serious secondary environmental pollution.The technological process of present similar processing tail gas comprises that the tail gas that 1. incinerators are discharged at first is cooled to 850-950 ℃ through air cooler; 2. be cooled to 650-750 ℃ through water cooler; 3. through≤200 ℃ of chilling extracting tower coolings; 4. through applicator, adsorption tower adsorb and be cooled to 130-180 ℃ in advance; 5. through bag-type dust, temperature is controlled at 130-170 ℃; 6. discharge cleaning of off-gas through exhaust system.Process conscientiously being researched and analysed and putting into practice above-mentioned technology, and we find that there is following problem in above-mentioned technology:

(1) one-level air cooler, the secondary water cooler, existing problems:

Because like product waste incinerator structure in the stove is backward in technique, causes one-level air cooler secondary water cooler, can only directly accepts dual firing chamber 〉=850-1100 ℃ of high temperature cigarette and handle.A) accept the flue-gas temperature height, handle load and increase the weight of, specification of equipment strengthens thereupon; B) harmful waste high-temperature process flue gas, temperature height, moisture content are heavy, harmful, corrosion component is complicated, and high temperature corrosion is very serious.C) indirect heat transfer body material type selecting difficulty, cost an arm and a leg, the life-span is short.And then causing the project construction investment to increase, the overhaul maintenance cost increases, the operating cost height.Project owner's profit margin is low, and the stable normal operation of the project that can influence probably causes the project owner not according to normal running, and effect is disposed in influence, continues contaminated environment.

(2) three grades of chilling extracting towers, existing problems:

A. inlet temperature 〉=500 ℃, outlet temperature≤200 ℃, the chilling period national Specification must be finished in 1 second, and semidry method alkali lye amount is few, is difficult to finish chilling requirement in 1 second, and control bioxin pollutant secondary synthetic effect reduces, and disposes not thorough;

B. in the chilling alkali lye and the depickling disposing technique, dispose together in same process equipment, two kinds of disposing technique specification requirement itself is opposite service behaviour principles, and it is fast that chilling is wanted; Need a large amount of cold media fluids to take away heat fast; In and depickling want slow, mix fully, in and the time to grow, temperature is low, deacidification effect could improve.Thus: bi-level treatment technology is mixed into one and disposes, the effect extreme difference.

C. in the gas washing and depickling after exit gas temperature too high, particularly the semidry method treatment technology of Cai Yonging sprays into a small amount of alkali lye and all evaporates, volatileness and water-soluble heavy metal toxicity thing can still be stored in the saturated gas moisture content.

D. outlet temperature is too high: influence follow-up active carbon adsorption effect, do not have the effect of effective absorption bioxin and other pollutant at all, cause secondary environmental pollution.

E. partly the heavy metal toxicity thing of volatileness can not make its cooling condensation and adsorb, and will discharge the secondary pollution environment with boil-off gas.

F. partly water-soluble heavy metal toxicity thing can not be washed the liquid absorption, discharges the secondary pollution environment with boil-off gas;

G. outlet temperature is too high, sprays into alkali lye and all evaporates, and desulfurization, denitration neutralization reaction effect are extremely low; Exhaust gas volumn increases, and causes the subsequent treatment load to increase the weight of; Flue gas moisture content height, seriously corroded, the specification of equipment investment is high.

H. have a strong impact on the anticorrosive main material of follow-up equipment and select for use, preservative treatment expense height, maintenance cost is big.

(3) the pre-applicator of level Four, the adsorption tower existing problems:

The too high influence of flue-gas temperature of technology control before the problem that exists mainly is subjected to, cause sorbing materials such as activated carbon, do not have the effect of effective absorption, because the best effectively adsorption temp of active carbon adsorption material is a normal temperature, generally is advisable at 30-40 ℃, be release temperature more than 100 ℃, in similar technology cause this process equipment running temperature for 160-180 ℃, having formed in fact is the invalid process equipment of one-level, and has increased ineffective investment and invalid operating cost.

(4) Pyatyi sack cleaner, existing problems:

The influence of technological control temperature technology before this equipment is subjected to must be accepted〉160-180 ℃ high-temperature flue gas, up to high moisture content flue gas operation more than 40%.

A. accept the operation of high moisture content flue gas, particularly start shooting, the shutdown stage is with variation of temperature, will cause dewfall to stick with paste bag, resistance increases, and power strengthens, and deashing difficulty, and the stable negative pressure operation of process equipment and incinerator before can influencing are polluted working environment;

B. accept the high-temperature flue gas operation, cause deduster main body inner wall preservative treatment difficulty, expense height, high temperature resistance, anti-(high moisture content) dewfall to filter cloth bag price extra-high-speed, the life-span is short; The necessary preferred high-grade high temperature resistance anticorrosive material of bag cage, investment is big, maintenance cost is high.

C. this equipment is that the harmful waste incineration tail gas is disposed one process equipment in back, continue to accept high temperature, high moisture content saturated gas operation, about 40% saturation water still is stored in the gas in the flue gas, through exhaust blower, atmosphere is discharged in the chimney motion cooling that 35M is high, particularly winter, the exhanst gas outlet temperature plunged, saturated moisture content in the flue gas will condensation form water droplet, the heavy metal toxicity thing of part volatileness, partly water-soluble heavy metal toxicity thing will fall into the earth with the water droplet ejection, partly will become the globule to flow to following discharge with the inner wall of stack dewfall, particularly in the semidry method chilling of Xuan Zeing and the deacidifying process technology, do not go up sewage treatment process, the chimney bottom sewage of discharging thus, all serious secondary pollution environment.

Comprehensive conclusion, similar prior art is not in place to UTILIZATION OF VESIDUAL HEAT IN, the process configuration of harmful waste high temperature incineration vent gas treatment, technological process control temperature is unreasonable, the hot operation of vent gas treatment overall process, high temperature neutralization reaction, high temperature absorption, high moisture content 〉=130-170 ℃ high temperature saturated gas discharging.The heat recovery rate is low, energy consumption is high, and high temperature neutralization reaction, high temperature absorption were lost efficacy, low, the weak effect of efficient, and it is not thorough to purify disposal.The heavy metal toxicity thing of most volatileness and the water-soluble heavy metal toxicity thing of part will enter atmosphere with high-temperature, high moisture content saturated gas, or the chimney breast condensation forms water droplet and is sprinkled into the earth and causes secondary pollution, exhaust system place hot operation corrosion-resistant treatments difficulty, investment is big, maintenance cost is high, and is difficult to reach the purpose of thorough harmless treatment.

(3) summary of the invention:

It is not in place to the objective of the invention is to solve existing tail gas treatment process configuration, and temperature control is unreasonable, purifies to dispose halfway problem, and a kind of clinical waste, hazardous waste, consumer waste incineration tail gas treatment process are provided.

Technical scheme of the present invention is that it is characterized in that: comprise following technological process: (1) at first is cooled to 650-700 ℃ through air cooler from the hot gas chamber tail gas discharged of incinerator dual firing chamber to the improvement of existing tail gas treatment process and perfect; (2) through the cold flue gas heat exchanger be cooled to≤600 ℃; (3) through water cooler be cooled to≤500 ℃; (4) in one-level warm rapid quench tower be chilled in 1 second≤200 ℃, and continue washing through the duplex base of quench tower and be cooled to≤80 ℃; (5) in secondary washing extracting tower and absorbing, cooling to≤50 ℃; (6) through condensation dehydration be cooled to≤35 ℃; (7) low temperature drying absorption; (8) return step (2) cold flue gas heat exchanger and be warming up to 70-90 ℃; (9) bag-type dust, second adsorption; (10) exhaust system is discharged cleaning of off-gas.

For improving the utilization rate of waste heat recovery, help the temperature control of subsequent technique, the present invention carried out UTILIZATION OF VESIDUAL HEAT IN before incinerator dual firing chamber outlet tail gas enters air cooler, heat in dry cracking room going into stokehold rubbish, and make tail gas be cooled to≤800 ℃.

The present invention shows to have following characteristics through experiment:

1. improve the heat recovery rate, have comprehensive advantage and effect;

2. the middle temperature of Cai Yonging (500-≤200 ℃) flue gas wet gas cleaning rapid quench technology, the secondary of effectively controlling the bioxin pollutant is synthetic;

3. in the low temperature of Cai Yonging (≤65 ℃) the flue gas alkali liquid washing and absorb lime block, activated carbon low temperature (30-50 ℃) efficient drying gas adsorbing process;

4. the condensation cooling of augmenting, dehydration, depositing dust decontamination process for purifying;

A. thoroughly remove De bioxin in the flue gas;

B. effectively remove the heavy metal toxicity thing of the part volatileness in the flue gas;

C. remove effectively in the flue gas that part can't be condensed, absorption, water-soluble heavy metal chloride;

D. the compound (hydrogen chloride, hydrogen bromide) that absorbs oxysulfide, halogen and hydrogen in the flue gas that effectively neutralizes plays high-efficiency desulfurization, denitration effect;

E. effectively remove noxious pollutants such as fluoride in the flue gas, mercury, benzene exhaust air;

F. effectively remove the high moisture content in the flue gas, eliminate chimney breast cooling water droplet spray (stream) and go out;

G. guarantee reaches and is better than HBC33-2004, GB19128-2003, H/T177-2005, HJ/T176-2005, the discharging of GB18181-2001 national standard, is an energy-saving and emission-reduction advanced technology that country advocates.

5. the cold flue gas heating process of Zeng Jiaing: will effectively adsorb dew-point temperature (30-50 ℃) cold flue gas of loss through washing, condensation cooling dehydration, low temperature, and utilize native system waste heat heat temperature raising (〉=70-≤90 ℃) back to enter sack cleaner by utilidor.

A. ensure cloth bag not dewfall, do not stick with paste bag;

B. be easy to deashing, reduce resistance, the safeguards system flue gas is unimpeded, stablize negative pressure moves;

C. operation can improve service life of equipment, energy-saving run maintenance cost continuously.

(4) description of drawings:

Accompanying drawing is a process chart of the present invention.

(5) specific embodiment:

The present invention is used for the processing technological flow of medical waste (or dangerous goods, house refuse) incineration tail gas, referring to accompanying drawing, may further comprise the steps:

1. the flue gas of discharging through incinerator dual firing chamber afterbody is about 1050 ℃, sends into drying garbage cracking room heating rubbish through hot gas chamber thermal conductor indirect heat transfer, carries out UTILIZATION OF VESIDUAL HEAT IN, and make flue-gas temperature reduce to≤800 ℃;

2. be cooled to 650-700 ℃ through air cooler, its inner core is the high-temperature flue gas passage, and exocoel is a secondary oxygenating air duct, and stove oxygenating air, heat recovery are gone in heating;

Through the cold flue gas heat exchanger be cooled to≤600 ℃, heat exchanger cavity is middle temperature exhaust gases passes, exocoel is a condensation cooling dehydration back dew-point temperature exhaust gases passes, by thermal conductor to exocoel indirec radiation temperature, the dew-point temperature flue gas is heated up, get rid of the dew-point temperature operation of sack cleaner place, the waste heat recovery comprehensive utilization;

Through water cooler be cooled to≤500 ℃, for follow-up emergency cooling process equipment provides stable purification condition, waste heat recovery comprehensive utilization, outer heat supply water;

5. directly enter " warm rapid quench tower in the one-level " by temperature (≤500 ℃) flue gas in the water cooler outlet, spray into the direct exchange of appropriate amount of fluid or alkali lye and flue gas and take away heat fast, reduce flue-gas temperature, by reduce in 500 ℃ of 1 second<200 ℃, control bioxin secondary is synthetic.

The quench tower bottom is during quench tower extremely washs and extracting tower (intermediate alkali liquid washing) duplex base, and standby liquid-jet device and sludge settling are housed concentrate extrusion device, main effect: prevention chilling, elementary washing feed flow, spray system fault, in time replenish the stable purification of hydrojet, adopt temperature detection and the interconnected automatic control measure of standby liquid-jet device, wash be cooled to≤80 ℃.

6. duplex base outlet low temperature (≤80 ℃) flue gas by warm rapid quench tower bottom in the one-level directly enters " secondary washing extracting tower ", high pressure sprays into fogged lye, fully mix neutralization deacidification, desulfurization, denitration, toxin expelling with low-temperature flue gas, control outlet temperature≤50 ℃, average running temperature≤65 ℃.Effectively remove " a small amount of oxysulfide ", " compound of halogen and hydrogen, (hydrogen chloride, hydrogen bromide etc.) ", " heavy metal contaminants of volatileness ", " partly water-soluble heavy metal chloride " and other nuisance in the flue gas.

7. carrying heat radiation to enter " condensation cooling dehydrating tower " by secondary washing extracting tower top outlet low temperature (≤50 ℃) flue gas by pipeline adopts cold water and flue gas indirect exchange cooling (the low more effect of supply water temperature is good more) to set up the water conservancy diversion device that blocks water to reduce flow velocity and dewater.

Main heavy water part of removing in the flue gas is effectively removed saturated part noxious pollutant remaining in flue gas moisture content, improves clean-up effect, for following road absorbing process provides good cryogenic absorption condition, plays effective suction-operated.

8. deliver into " dry adsorption tower " by exporting low temperature (≤35 ℃) flue gas above the plash of condensation dehydrating tower bottom through pipeline, inner chamber is equipped with fixedly absorption material such as graininess " lime block ", " drier ", " activated carbon ", and dispose pulverized limestone, activated carbon powder mixed high-voltage, spraying feedway, under low temperature environment, have the good adsorption effect and continue to remove moisture drying gas.

9. the low-temperature flue gas after the drying absorption returns and enters aforementioned the 3rd step cold flue gas heat exchanger, utilizes the native system waste heat to carry out indirect exchange heating flue gas, the dew-point temperature flue gas is warmed up on the dew point 〉=70 ℃-<90 ℃.

10. be inhaled into sack cleaner through utilidor, avoid the bag-type dust dewfall and stick with paste bag, be easy to deashing and reduce resistance, guarantee that the total system negative pressure normally moves, effectively remove flue dust in the gas and cryogenic temperature condensation and be attracted to heavy metal toxicity thing in the flue dust.

11. enter atmosphere by exhaust system through the tail gas after the sack cleaner purification.

The present invention adopts and has realized:

1. adopt high-temperature flue gas level Four UTILIZATION OF VESIDUAL HEAT IN technology: secondary recovery is advanced stove self utilization, the secondary recovery comprehensive utilization;

2. warm flue gas first class purification technology in adopting: wet scrubbing rapid quench;

3. adopt three grades of process for purifying of low-temperature flue gas: one-level washing neutralization reaction, one-level condensation dehydration depositing dust toxin expelling, a grade low-temp effectively adsorb;

4. adopt low temperature, low moisture content, low concentration, flue gas one-level bag-type dust, second adsorption technology in 70-90 ℃ of cold flue gas heat temperature raising: the activated carbon powder second adsorption that is brought into is beneficial to and prolongs adsorption time and raise the efficiency.Dry gas on the dew-point temperature, cloth bag trap filter flue dust, no dewfall is not stuck with paste bag, and it is low to be easy to the deashing resistance, and it is unimpeded to help the exhaust system flue gas, ensures full CIU negative pressure operation.

Ten road technologies have been finished: high-temperature flue gas waste heat high efficiency is recycled, and is energy-saving and cost-reducing; In warm flue gas rapid quench, the secondary of controlling bioxin pollutant is synthetic; The washing neutralization reaction of low-temperature flue gas, absorption, dehydration depositing dust toxin expelling provide effective purifying exhaust air condition, efficient purifying exhaust air; Temperature, the second adsorption of low-concentration flue gas, cloth bag dust removal by filtration in low have been finished last thoroughly harmless treatment together.

Realized " efficient energy-saving and emission-reducing ", dustless, smokeless, odorless, nontoxic discharging, chimney does not have high moisture content (being harmful to) saturated gas and enters atmosphere, stably reaching standard, the discharging of excellent mark.

Claims (2)

1. clinical waste, hazardous waste, consumer waste incineration tail gas treatment process, its technological process may further comprise the steps: (1) at first is cooled to 650-700 ℃ through air cooler from the hot gas chamber tail gas discharged of incinerator dual firing chamber; (2) through the cold flue gas heat exchanger be cooled to≤600 ℃; (3) through water cooler be cooled to≤500 ℃; (4) in one-level warm rapid quench tower be chilled in 1 second≤200 ℃, and continue washing through the duplex base of quench tower and be cooled to≤80 ℃; (5) in secondary washing extracting tower and absorbing, cooling to≤50 ℃; (6) through condensation dehydration be cooled to≤35 ℃; (7) low temperature drying absorption; (8) return step (2) cold flue gas heat exchanger and be warming up to 70-90 ℃; (9) bag-type dust, second adsorption; (10) exhaust system is discharged cleaning of off-gas.
2. medical treatment according to claim 1, hazardous waste, consumer waste incineration vent gas treatment new technology, it is characterized in that: before incinerator dual firing chamber outlet tail gas enters air cooler, carry out UTILIZATION OF VESIDUAL HEAT IN, heat in dry cracking room going into stokehold rubbish, and make tail gas be cooled to≤800 ℃.
CN200810197405A 2008-10-24 2008-10-24 Processing technology for medical waste, dangerous waste, domestic garbage and burning tail gas CN100584434C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200810197405A CN100584434C (en) 2008-10-24 2008-10-24 Processing technology for medical waste, dangerous waste, domestic garbage and burning tail gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200810197405A CN100584434C (en) 2008-10-24 2008-10-24 Processing technology for medical waste, dangerous waste, domestic garbage and burning tail gas

Publications (2)

Publication Number Publication Date
CN101498455A true CN101498455A (en) 2009-08-05
CN100584434C CN100584434C (en) 2010-01-27

Family

ID=40945647

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200810197405A CN100584434C (en) 2008-10-24 2008-10-24 Processing technology for medical waste, dangerous waste, domestic garbage and burning tail gas

Country Status (1)

Country Link
CN (1) CN100584434C (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103196144A (en) * 2013-03-29 2013-07-10 汤广斌 Harmless resource comprehensive utilization device and method of pharmaceutical solid and gas waste
CN103292339A (en) * 2013-06-24 2013-09-11 湖南科技大学 Comprehensive processing recycling process and device of bromine-contained high temperature flue gas
CN103706210A (en) * 2013-09-30 2014-04-09 安徽天之都环保科技股份有限公司 Small size domestic garbage incinerator dry tail gas treatment system and treatment method
CN104654874A (en) * 2015-02-10 2015-05-27 成都阿斯特克国龙环保工程有限公司 Acid and acid regeneration unit waste gas residual heat recovery and waste gas processing system and method
CN105617833A (en) * 2016-03-14 2016-06-01 江正云 Medical waste burning flue gas treatment system
CN105805764A (en) * 2016-03-14 2016-07-27 江正云 Medical waste incineration technological method
CN106016279A (en) * 2016-05-12 2016-10-12 安徽国能亿盛环保科技有限公司 Waste plastic treatment method
CN106178892A (en) * 2016-08-24 2016-12-07 湖南顶立科技有限公司 Exhaust gas treating method and system are reclaimed in a kind of enamel-covered wire pyrolysis
CN108332210A (en) * 2017-12-27 2018-07-27 四川天壹环保科技有限公司 A kind of integrated small-sized efficient domestic solid waste incinerator system of movable type
CN108970308A (en) * 2018-07-04 2018-12-11 北京矿冶科技集团有限公司 A kind of high-temp chlorination flue gas processing method containing gold

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103196144A (en) * 2013-03-29 2013-07-10 汤广斌 Harmless resource comprehensive utilization device and method of pharmaceutical solid and gas waste
CN103196144B (en) * 2013-03-29 2016-03-09 河南弘康环保科技有限公司 Pharmacy is solid, the innoxious comprehensive utilization of resources device and method of gas discarded object
CN103292339A (en) * 2013-06-24 2013-09-11 湖南科技大学 Comprehensive processing recycling process and device of bromine-contained high temperature flue gas
CN103292339B (en) * 2013-06-24 2015-06-17 湖南科技大学 Comprehensive processing recycling process and device of bromine-contained high temperature flue gas
CN103706210A (en) * 2013-09-30 2014-04-09 安徽天之都环保科技股份有限公司 Small size domestic garbage incinerator dry tail gas treatment system and treatment method
CN104654874A (en) * 2015-02-10 2015-05-27 成都阿斯特克国龙环保工程有限公司 Acid and acid regeneration unit waste gas residual heat recovery and waste gas processing system and method
CN104654874B (en) * 2015-02-10 2016-03-16 成都阿斯特克国龙环保工程有限公司 Acid regeneration unit waste gas residual heat reclaims and exhaust treatment system and method
CN105617833A (en) * 2016-03-14 2016-06-01 江正云 Medical waste burning flue gas treatment system
CN105805764A (en) * 2016-03-14 2016-07-27 江正云 Medical waste incineration technological method
CN106016279A (en) * 2016-05-12 2016-10-12 安徽国能亿盛环保科技有限公司 Waste plastic treatment method
CN106178892A (en) * 2016-08-24 2016-12-07 湖南顶立科技有限公司 Exhaust gas treating method and system are reclaimed in a kind of enamel-covered wire pyrolysis
CN108332210A (en) * 2017-12-27 2018-07-27 四川天壹环保科技有限公司 A kind of integrated small-sized efficient domestic solid waste incinerator system of movable type
CN108970308A (en) * 2018-07-04 2018-12-11 北京矿冶科技集团有限公司 A kind of high-temp chlorination flue gas processing method containing gold

Also Published As

Publication number Publication date
CN100584434C (en) 2010-01-27

Similar Documents

Publication Publication Date Title
JP4988864B2 (en) Use of SO2 from flue gas in ammonia acid cleaning
US4844721A (en) Air scrubbing process
CN101288820B (en) Active carbon fiber organic gas recovery method and system using nitrogen as desorption medium
TWI336269B (en) Equipment for and method of treating exhausted combustion gas
CN102120130B (en) Complete set of device and method for treating tail gas from sludge incineration through semidry method
CN101362076B (en) Regeneration method of active carbon absorbent
CN101829468B (en) Flue-gas cleaning method and system for waste incineration
CN1332736C (en) Process and plant for ultrapurifying fumes or gasses
CN203750409U (en) Flue gas purifying treatment device in waste incineration process
CN102068890B (en) Method and device for treating complex industrial organic waste gas
CN201333374Y (en) Device capable of collecting carbon dioxide contained in flue gases of power plant through ammonia by utilizing void tower
CN105080332B (en) Agglomerates of sintered pellets reclamation system and process
CN101797472A (en) Smoke processing technology
CN202028294U (en) Desulfuration denitration waste gas treatment system for casting dust
CN105090997A (en) Method for treating high-concentration salty waste water and waste residue at low cost, and device thereof
WO2008128465A1 (en) System and progress for treating wet sludge by drying and incinerating
JP4155898B2 (en) High moisture waste incineration facility equipped with gas turbine
CN202973140U (en) Efficient flue gas purification and waste heat utilization system
KR100949037B1 (en) Eliminating apparatus of effluent gas comes from an organic waste
CN101708414B (en) System and method for desulphurizing waste gas by cyclic absorption and application thereof
CN103429317A (en) Apparatus and system for NOX reduction in wet flue gas
CN102143795A (en) A method and a device for removing nitrogen oxides and sulphur trioxide from a process gas
CN100571842C (en) A kind of improvement method and device of fish powder waste gases
CN206566727U (en) Waste gas cleaning system for injection machine
CN101628201A (en) Clearing device for smoke pollutants of glass kiln and clearing method thereof

Legal Events

Date Code Title Description
PB01 Publication
C06 Publication
SE01 Entry into force of request for substantive examination
C10 Entry into substantive examination
GR01 Patent grant
C14 Grant of patent or utility model
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100127

Termination date: 20121024

C17 Cessation of patent right