CN102120132B - Purification treatment device for incineration flue gas - Google Patents

Purification treatment device for incineration flue gas Download PDF

Info

Publication number
CN102120132B
CN102120132B CN 201110038059 CN201110038059A CN102120132B CN 102120132 B CN102120132 B CN 102120132B CN 201110038059 CN201110038059 CN 201110038059 CN 201110038059 A CN201110038059 A CN 201110038059A CN 102120132 B CN102120132 B CN 102120132B
Authority
CN
China
Prior art keywords
outlet
pipeline
flue gas
purification treatment
treatment device
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.)
Active
Application number
CN 201110038059
Other languages
Chinese (zh)
Other versions
CN102120132A (en
Inventor
王玮
吴桐
李大涛
肖成龙
鲁琦
陈曦
邢啸林
尹荔堃
李伯森
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.)
101 Institute Of Ministry Of Civil Affairs Of People's Rupublic Of China
Original Assignee
101 Institute Of Ministry Of Civil Affairs Of People's Rupublic Of China
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 101 Institute Of Ministry Of Civil Affairs Of People's Rupublic Of China filed Critical 101 Institute Of Ministry Of Civil Affairs Of People's Rupublic Of China
Priority to CN 201110038059 priority Critical patent/CN102120132B/en
Publication of CN102120132A publication Critical patent/CN102120132A/en
Application granted granted Critical
Publication of CN102120132B publication Critical patent/CN102120132B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The invention discloses a purification treatment device for incineration flue gas. A condensate pipe is arranged in a cold and hot exchanger; a combustor is arranged on a flue gas combustion chamber; the flue gas combustion chamber is provided with an inlet and an outlet; the outlet of the flue gas combustion chamber is connected to the inlet of the cold and hot exchanger through a pipeline; the outlet of the cold and hot exchanger is connected to the inlet of a deacidification system through a pipeline; the outlet of the deacidification system is connected to the inlet of a dry-wet separator through a pipeline; the outlet of the dry-wet separator is connected to the inlet of a mixing chamber through a pipeline; an activated carbon storage tank is arranged on the mixing chamber; the outlet of the mixing chamber is connected to the inlet of a bag-type dust collector through a pipeline; the outlet of the bag-type dust collector is provided with a draught fan; the outlet of a dosing device is connected to the deacidification system through a pipeline; a first outlet of a blowing device is connected to the deacidification system through a pipeline; and a second outlet of the blowing device is connected to the mixing chamber through a pipeline.

Description

Purification treatment device for incineration flue gas
Technical field
The present invention relates to a kind of cremate technology of funeral profession, specifically, relate to a kind of purification treatment device for incineration flue gas.
Background technology
At present, China's funeral profession all adopts in line mode to discharge cremate waste gas in the Cremation Machine overwhelming majority of usefulness, cremating, it is very serious to pollute, because the atmosphere pollution that produces of cremating had both comprised the inorganic pollutions such as flue dust, carbon monoxide, nitric oxide, nitrogen dioxide, sulfur dioxide, hydrogen sulfide, ammonia, mercury, comprise again the dioxin organic pollution materials.As effectively not controlled, certainly will cause the abominable destruction of severe contamination and the peripheral ecological environment of funeral place air." the national civil administration science and technology Long-and Medium-term Development planning outline (2009-2020) " that issue in 2009 is implemented, classify funeral and interment science and technology as giving priority to field, and classify " research of field of funeral and interment severe toxicity dioxin pollution thing emission-reduction technology ", " technical research of clean energy resource cremate remains " as great scientific and technological engineering.
Existing funeral profession incinerating smoke cleaning device mainly is the dry cleaning system take sack cleaner as chief component, and the system for wet purification take the water curtain sprinkling device as chief component.The shortcoming of prior art is: one, the soot dust granule thing can only be removed by the wet cleaning system take the water curtain sprinkling device as chief component, and a small amount of sour gas can not effectively be removed the dioxin organic pollution.Two, the dry cleaning system take sack cleaner as chief component does not have removal effect substantially for the sour gas pollutant.And because two types purifier inlet temperature (approximately below 500 ℃) on the low side, this temperature is exactly again synthetic needed temperature of dioxin-like chemical just, therefore, follow-up the total amount to be processed or dioxin-like chemical of discharging is bigger than normal, can not effectively purify the cremate flue gas.
Summary of the invention
Technical problem solved by the invention provides a kind of purification treatment device for incineration flue gas, can effectively remove acid inorganic pollution and dioxin organic pollution in the cremate flue gas simultaneously.
Technical scheme is as follows:
A kind of purification treatment device for incineration flue gas, comprise sack cleaner and air-introduced machine, also comprise chemicals dosing plant, blowing device, smoke combustion chamber, burner, condensate pipe, cool-heat-exchanger, remove acid system, separating dry space from moist space device, activated carbon powder storage tank and mixing chamber; It is inner that described condensate pipe is arranged on described cool-heat-exchanger, and described burner is arranged on the smoke combustion chamber; Described smoke combustion chamber is provided with entrance and exit, the outlet of described smoke combustion chamber is connected to the entrance of described cool-heat-exchanger by pipeline, the outlet of described cool-heat-exchanger connects described entrance except acid system by pipeline, described outlet except acid system connects the entrance of described separating dry space from moist space device by pipeline, the outlet of described separating dry space from moist space device is connected to the entrance of described mixing chamber by pipeline, described activated carbon powder storage tank is arranged on the described mixing chamber, the outlet of described mixing chamber is connected to by pipeline on the entrance of described sack cleaner, and the outlet of described sack cleaner is provided with air-introduced machine; The outlet of described chemicals dosing plant is connected to described except on the acid system by pipeline, the first outlet of described blowing device is connected to described except on the acid system by pipeline, and the second outlet of described blowing device is connected on the described mixing chamber by pipeline.
Further: the end of described mixing chamber is equipped with the negative pressure indicator.
Further: described chemicals dosing plant comprises lye tank (vat), tank diameter, dosing pump and force (forcing) pump, described dosing pump is arranged on described lye tank (vat) and the pipeline that tank diameter is connected, described force (forcing) pump is arranged on the outlet of described tank diameter, and described pressurization delivery side of pump is connected to described except on the acid system by pipeline.
Further: described blowing device comprises air compressor machine and the compressed air reservoir that is connected, and described the first outlet and the second outlet are arranged on the described compressed air reservoir.
Further: described blowing device also comprises the 3rd outlet, and described the 3rd outlet is connected to the entrance of described sack cleaner by pipeline.
Further: in the described lye tank (vat) sodium hydroxide solution is housed.
Further: in the described activated carbon powder storage tank activated carbon powder is housed.
Further: described lye tank (vat) is provided with dosing mouth, and described tank diameter is provided with water supplement port.
Compared with prior art the technology of the present invention effect comprises:
1, in the prior art, the flue outlet temperature all is lower than 500 ℃, just directly flue gas is carried out quenching in the situation that do not install the smoke combustion chamber additional, and the effect of removing dioxin-like chemical is also not obvious.Among the present invention, install additional after the smoke combustion chamber, can effectively guarantee the chilling effect, the again fully burning of flue gas that flue is discharged, both prolonged the holdup time of flue gas at high-temperature area, imperfect combustion part is fully burnt, the cigarette temperature is raise again, be next step flue gas quenching, cross dioxin-like chemical more synthetic temperature province carried out sufficient place mat.
2, the present invention is provided with except acid system, mixing chamber and sack cleaner, under the acting in conjunction of activated carbon powder, can effectively remove acid inorganic pollution and dioxin organic pollution in the cremate flue gas simultaneously, makes purification more thorough more comprehensively.The scene has entrusted the relevant expert of national environmental protection section that it is carried out Contaminant measurement, and test result all reaches the funeral profession national standard.
3, the design of the separating dry space from moist space device among the present invention is very ingenious, and very crucial for whole purification process, and the dehydrating effect of separating dry space from moist space device will directly affect the removal efficiency of sack cleaner.If this device not, the cloth bag in the sack cleaner will be in dampness for a long time, and the blowback effect of air compressor machine will be had a greatly reduced quality.
4, the target contaminant that removes in the flue gas of the present invention is comprehensive, has both comprised conventional atmosphere inorganic pollution, such as flue dust, carbon monoxide, nitric oxide, nitrogen dioxide, sulfur dioxide, hydrogen sulfide, ammonia, mercury etc., comprises again the dioxin organic pollution materials.
5, has huge Social benefit and economic benefit.Social benefit: the pollution problem of funeral profession cremate technique always is the problem of the Chinese government and broad masses of the people's headache, and existing funeral and interment science and technology also is in the starting stage, also can't resolve the problem of environmental pollution that cremation of remains brings at present; Apparatus of the present invention can effectively be removed the cremate pollutant, take the lead in proposing in funeral profession take conventional pollutant and dioxin organic pollution as the main concept of removing object, for contribution has been made in the establishment of China BAT/BEP in this field.Economic benefit: according to " civil administration career development statistical report in 2009 " by the end of the end of the year in 2009,1729 in the total funeral parlor, the whole nation, 5123 of Cremation Machine, year cremate remains 454.2 ten thousand tools, the situation of post processing is installed according to current funeral profession, conservative prediction needs 4500 cover cremate flue gas after-treatment devices at least, and economic benefit and market prospects are very considerable.
Description of drawings
Fig. 1 is the structure chart of purification treatment device for incineration flue gas of the present invention.
The specific embodiment
The present invention reasonably combines the advantage of existing purifier, remove target contaminant more extensive, and increased the micro smoke combustion chamber, the flue gas that the cremate horizontal flue is discharged carries out second-time burning, namely prolonged the holdup time of cremate flue gas, it is fully burnt, realized again the secondary temperature elevation to flue gas, for next step quenching apparatus widens the temperature difference, be down to the cigarette temperature below 300 ℃ more than 500 ℃ rapidly, the jump over synthesis temperature district of dioxin-like chemical, concentration and total amount with pollutant from the source drop to minimum.
Below with reference to accompanying drawing and preferred embodiment technical solution of the present invention is described in detail.
As shown in Figure 1, be the structure chart of purification treatment device for incineration flue gas of the present invention.The structure of purification treatment device for incineration flue gas comprises: lye tank (vat) 1, tank diameter 2, dosing pump 3, force (forcing) pump 4, air compressor machine 5, compressed air reservoir 6, smoke combustion chamber 7, burner 8, condensate pipe 9, cool-heat-exchanger 10, except acid system 11, separating dry space from moist space device 12, activated carbon powder storage tank 13, mixing chamber 14, negative pressure indicator 15, sack cleaner 16, air-introduced machine 17.
The cremate flue gas that forms after the corpse burning enters smoke combustion chamber 7, and burner 8 is arranged on the smoke combustion chamber 7, and burner 8 is used for second-time burning and heats the cremate flue gas.
The outlet of smoke combustion chamber 7 is connected to the entrance of cool-heat-exchanger 10 by pipeline, condensate pipe 9 is arranged on cool-heat-exchanger 10 inside.
The outlet of cool-heat-exchanger 10 connects the entrance that removes acid system 11 by pipeline, be used for removing the sour gas of cremate flue gas except acid system 11, connects the entrance of separating dry space from moist space device 12 by pipeline except the outlet of acid system 11.Chemicals dosing plant comprises lye tank (vat) 1, tank diameter 2, dosing pump 3, force (forcing) pump 4, and dosing pump 3 is arranged on lye tank (vat) 1 is connected with tank diameter on the pipeline that connects, and force (forcing) pump 4 is arranged in the outlet of tank diameter 2, and the outlet of force (forcing) pump 4 is connected to except on the acid system by pipeline.In the lye tank (vat) 1 NaOH is housed among the present invention, removes sour gas in the cremate flue gas by NaOH, certainly, also can in lye tank (vat) 1, fill the alkali lye of other kinds.Lye tank (vat) 1 is provided with dosing mouth 101, and tank diameter 2 is provided with water supplement port 201, adds alkali lye by dosing mouth 101 to lye tank (vat) 1, by water supplement port 201 supplementing water, to regulate concentration of lye.
Separating dry space from moist space device 12 is used for carbonated drink separation, and the outlet of separating dry space from moist space device 12 is connected to the entrance of mixing chamber 14 by pipeline; Be provided with activated carbon powder storage tank 13 on the mixing chamber 14, in the activated carbon powder storage tank 13 active carbon be housed, mixing chamber 14 is used for removing the dioxin organic pollution, and the outlet of mixing chamber 14 is connected on the entrance of sack cleaner 16 by pipeline; Sack cleaner 16 is used for the activated carbon powder that removes dust and adsorbed organic pollution, and the outlet of sack cleaner 16 is provided with air-introduced machine 17, and tail gas is extracted and sent into to air-introduced machine 17 out chimney 18.
Blowing device comprises air compressor machine 5 and compressed air reservoir 6, blowing device is provided with three outlets, the first outlet is connected to except on the acid system 11 by pipeline, and the second outlet is connected on the mixing chamber 14 by pipeline, and the 3rd outlet is connected to the entrance of sack cleaner 16 by pipeline.
The cremate flue gas enters smoke combustion chamber 7 from the left side, by the burning of burner 8 and then again heating, after flue gas again burns and heats up, enter cool-heat-exchanger 10, with the cremate flue gas after condensate pipe carries out cold and hot exchange, enter except acid system 11, except in the acid system 11, the alkali lye (NaOH) that flue gas and tank diameter 2 inject except acid system 11 fully reacts by spray, drip washing, removes the most sour gas in the cremate flue gas.NaOH stoste in the lye tank (vat) 1 pumps into tank diameter 2 through dosing pump 3, pumps into except acid system 11 by force (forcing) pump 4 after NaOH mixes with water.Except the spray flow process in the acid system 11 realizes by air compressor machine 5 and compressed air reservoir 6.Remove the flue gas of sour gas through entering separating dry space from moist space device 12 except acid system 11, under the impact of gravitational field, moisture content sinks in the flue gas, and gas spiral is up.The flue gas that has taken off moisture then enters mixing chamber 14, and flue gas fully mixes with the activated carbon powder that activated carbon powder storage tank 13 pneumatics enter 14 li of mixing chambers.Mixing chamber 14 ends are equipped with negative pressure indicator 15, monitor at any time the pressure condition of mixing chamber 14, in the suction-operated of this main activated carbon, and the dioxin organic pollution in the absorption flue gas.Then flue gas enters sack cleaner 16, removes dust and adsorbs the activated carbon powder of organic pollution.Tail gas after removing, the effect by air-introduced machine 17 enters chimney 18, and is then emptying.

Claims (8)

1. purification treatment device for incineration flue gas, comprise sack cleaner and air-introduced machine, it is characterized in that: also comprise chemicals dosing plant, blowing device, smoke combustion chamber, burner, condensate pipe, cool-heat-exchanger, remove acid system, separating dry space from moist space device, activated carbon powder storage tank and mixing chamber; It is inner that described condensate pipe is arranged on described cool-heat-exchanger, and described burner is arranged on the smoke combustion chamber; Described smoke combustion chamber is provided with entrance and exit, the outlet of described smoke combustion chamber is connected to the entrance of described cool-heat-exchanger by pipeline, the outlet of described cool-heat-exchanger connects described entrance except acid system by pipeline, described outlet except acid system connects the entrance of described separating dry space from moist space device by pipeline, the outlet of described separating dry space from moist space device is connected to the entrance of described mixing chamber by pipeline, described activated carbon powder storage tank is arranged on the described mixing chamber, the outlet of described mixing chamber is connected to by pipeline on the entrance of described sack cleaner, and the outlet of described sack cleaner is provided with air-introduced machine; The outlet of described chemicals dosing plant is connected to described except on the acid system by pipeline, the first outlet of described blowing device is connected to described except on the acid system by pipeline, and the second outlet of described blowing device is connected on the described mixing chamber by pipeline.
2. purification treatment device for incineration flue gas as claimed in claim 1, it is characterized in that: the end of described mixing chamber is equipped with the negative pressure indicator.
3. purification treatment device for incineration flue gas as claimed in claim 1, it is characterized in that: described chemicals dosing plant comprises lye tank (vat), tank diameter, dosing pump and force (forcing) pump, described dosing pump is arranged on described lye tank (vat) and the pipeline that tank diameter is connected, described force (forcing) pump is arranged on the outlet of described tank diameter, and described pressurization delivery side of pump is connected to described except on the acid system by pipeline.
4. purification treatment device for incineration flue gas as claimed in claim 1, it is characterized in that: described blowing device comprises air compressor machine and the compressed air reservoir that is connected, described the first outlet and second exports and is arranged on the described compressed air reservoir.
5. such as claim 1 or 4 described purification treatment device for incineration flue gas, it is characterized in that: described blowing device also comprises the 3rd outlet, and described the 3rd outlet is connected to the entrance of described sack cleaner by pipeline.
6. purification treatment device for incineration flue gas as claimed in claim 3 is characterized in that: in the described lye tank (vat) sodium hydroxide solution is housed.
7. purification treatment device for incineration flue gas as claimed in claim 3 is characterized in that: in the described activated carbon powder storage tank activated carbon powder is housed.
8. purification treatment device for incineration flue gas as claimed in claim 3, it is characterized in that: described lye tank (vat) is provided with dosing mouth, and described tank diameter is provided with water supplement port.
CN 201110038059 2011-02-14 2011-02-14 Purification treatment device for incineration flue gas Active CN102120132B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201110038059 CN102120132B (en) 2011-02-14 2011-02-14 Purification treatment device for incineration flue gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201110038059 CN102120132B (en) 2011-02-14 2011-02-14 Purification treatment device for incineration flue gas

Publications (2)

Publication Number Publication Date
CN102120132A CN102120132A (en) 2011-07-13
CN102120132B true CN102120132B (en) 2013-02-27

Family

ID=44248852

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201110038059 Active CN102120132B (en) 2011-02-14 2011-02-14 Purification treatment device for incineration flue gas

Country Status (1)

Country Link
CN (1) CN102120132B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103047668B (en) * 2011-10-14 2015-02-18 威海鲁源科技环保设备有限公司 Tail gas purification treatment system of cremation machine
CN103157338B (en) * 2012-12-19 2015-09-09 威海航泰环保设备有限公司 Cremation machine all-dry-method posttreatment system
CN104406184B (en) * 2014-12-16 2016-11-30 威海鲁源科技环保设备有限公司 A kind of Cremation Machine device for purifying and treating tail gas
CN104566386A (en) * 2014-12-23 2015-04-29 福寿园环保机械制造有限公司 Environment-friendly and energy-saving full-automatic cremation machine fume cleaning device
CN105056707A (en) * 2015-09-09 2015-11-18 梁峰 Restaurant lampblack treatment device adopting nano filter balls
CN105233576A (en) * 2015-09-28 2016-01-13 民政部一零一研究所 Funeral home indoor waste gas purification method and device thereof
CN107469485A (en) * 2017-09-11 2017-12-15 郭玉连 A kind of method for industrial waste gas processing
CN112221319A (en) * 2020-10-09 2021-01-15 内蒙古工业大学 Reactive type cooperative purification method and device for smoke pollutants

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3651075B2 (en) * 1995-09-19 2005-05-25 石川島播磨重工業株式会社 Olimar John-fired boiler flue gas treatment facility
CN100549522C (en) * 2006-09-29 2009-10-14 刘立竹 Medical destructor system
CN201628227U (en) * 2010-03-24 2010-11-10 民政部一零一研究所 Remains and offering incineration and post-treatment equipment
CN201988321U (en) * 2011-02-14 2011-09-28 民政部一零一研究所 Incinerating smoke cleaning processing device

Also Published As

Publication number Publication date
CN102120132A (en) 2011-07-13

Similar Documents

Publication Publication Date Title
CN102120132B (en) Purification treatment device for incineration flue gas
CN211513996U (en) Flue gas carbon dioxide trapping device of coal-fired power plant
CN102294171B (en) Flue gas purifying system
CN106178892A (en) Exhaust gas treating method and system are reclaimed in a kind of enamel-covered wire pyrolysis
CN105463153B (en) A kind of converter gas purification recovery system and method
CN108977211A (en) A kind of solid waste pyrolysis system that coupling high temperature pyrolysis gas are directly burnt
CN103255260A (en) Converter flue gas purifying and waste heat recovering system and bag-type dust removing technology
CN102151472B (en) Small-sized cremation flue gas purification device
CN109331557A (en) A kind of cement kiln bypass flue gas purifying method
CN201988321U (en) Incinerating smoke cleaning processing device
CN201997253U (en) Minitype purifying device for cremating flue gas
CN107726337B (en) A kind of smoke processing system of garbage disposal furnace
CN106178877A (en) A kind of coke oven flue waste gas purification waste heat recovery apparatus and technique
CN203764071U (en) Environment-friendly treatment and purification system for flue gas of cremation machines
CN205867863U (en) Flue gas purification treatment device
CN210945666U (en) Converter gas dry dedusting recovery system
CN202605926U (en) Smoke multilevel wet dust-removal decontamination device
CN103614509B (en) A kind of carbon steel converter dry cloth bag dedusting process of whole process recovery waste heat and device thereof
CN101270877B (en) Water-proof coiled material flue gas processing equipment
CN215388529U (en) Collecting and processing system for waste gas generated in hazardous waste treatment process
CN202803043U (en) Boiler smoke purifying device
CN203625414U (en) Dry cloth-bag dust removal device for carbon steel converter capable of recovering waste heat in whole process
CN203790798U (en) Purification treatment system for waste gas produced in production process of furfural
CN211274055U (en) Cremation machine tail gas treatment equipment
CN110465542B (en) Device and method for treating organic pollution solid waste by cascade thermal desorption

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant