CN102716656A - Smoke washing device - Google Patents

Smoke washing device Download PDF

Info

Publication number
CN102716656A
CN102716656A CN2012102259064A CN201210225906A CN102716656A CN 102716656 A CN102716656 A CN 102716656A CN 2012102259064 A CN2012102259064 A CN 2012102259064A CN 201210225906 A CN201210225906 A CN 201210225906A CN 102716656 A CN102716656 A CN 102716656A
Authority
CN
China
Prior art keywords
cleaning solution
smoke
washing device
flue
adverse current
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
CN2012102259064A
Other languages
Chinese (zh)
Inventor
张旭辉
卢红波
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.)
Beijing Dongzhan Kebo Technology Co., Ltd.
Original Assignee
BEIJING DONGXU HONGYE TECHNOLOGY 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 BEIJING DONGXU HONGYE TECHNOLOGY Co Ltd filed Critical BEIJING DONGXU HONGYE TECHNOLOGY Co Ltd
Priority to CN2012102259064A priority Critical patent/CN102716656A/en
Publication of CN102716656A publication Critical patent/CN102716656A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Treating Waste Gases (AREA)

Abstract

The invention relates to a smoke washing device. A washing tower of the smoke washing device comprises a cooling adsorption washing area and an adverse current adsorption washing area. When smoke passes through the cooling adsorption washing area, partial pollutant such as smoke dust in the smoke can be removed, volume flow rate of the smoke is reduced simultaneously, and sectional area of the adverse current adsorption washing area is favorably reduced. In the adverse current adsorption washing area, the smoke dust in the smoke can be absorbed through sufficient contact between the smoke dust and a liquid film, and simultaneously pollutant such as sulfur dioxide can be sufficiently reacted. By means of the smoke washing device, high-efficient smoke dedusting desulfuration is achieved. In addition, washed smoke and heated air are mixed and then discharged out, smoke humidity is reduced, and rime fog at an air outlet of the smoke washing device is avoided. The smoke washing device is small in size, light in weight and applicable to flue gas treatment of a host machine and a boiler of an offshore platform or a traveling ship, and meets miniaturization requirements of on-land fume treatment equipment.

Description

A kind of flue washing device
Technical field
The present invention relates to a kind of flue gas desulfurization and dedusting technology, relate in particular to a kind of flue washing device.
Background technology
At present, the flue gas that domestic and international offshore platform facility (for example main frame and boiler) is produced is basically still directly to airborne release, and the problem of smoke pollution is effectively solved always.Based on offshore platform and the limitation of navigating ship on space and environment; Such as climatic factors such as floor space, weight capacity, security, device height restriction and typhoon waves etc., offshore platform and navigating ship have higher requirement to flue washing device.Therefore, need a kind of requirement that can satisfy offshore platform and navigating ship, the device of smoke treatment expeditiously.
Summary of the invention
To above-mentioned technical problem, the present invention has designed and developed a kind of flue washing device.
The object of the present invention is to provide a kind of flue washing device.Scrubbing tower of the present invention comprises cooling absorption scrubbing section and adverse current absorption scrubbing section.Flue gas gets into cooling absorption scrubbing section; At first the cleaning solution with the ejection of the first cleaning solution spray equipment contacts, then at the first corrugated plate packing layer and the abundant haptoreaction of cleaning solution, said process; Can partly remove the pollutants such as flue dust in the flue gas on the one hand; Can reduce flue-gas temperature significantly on the other hand, reduce the volume flow of flue gas, help to reduce the sectional area of adverse current absorption scrubbing section.In adverse current absorption scrubbing section,, then on the second corrugated plate packing layer, can form liquid film because the second cleaning solution spray equipment is arranged on the top of the second corrugated plate packing layer.When flue gas moves upward, at first get into the second corrugated plate packing layer, collide back and forth at the second corrugated plate packing laminar surface, fully contact with liquid film.Through said process, the flue dust in the flue gas is adsorbed, and pollutants such as while sulfur dioxide have also obtained abundant reaction.Utilize flue washing device of the present invention, realized high efficiency flue-gas dust-removing and desulfurization.Simultaneously, the volume of flue washing device of the present invention is little, in light weight, is applicable to the main frame of offshore platform or navigating ship, the flue gas processing of boiler, also satisfies the miniaturization demand of land fume treatment auxiliary.
Technical scheme of the present invention is:
A kind of flue washing device comprises scrubbing tower, is provided with cooling absorption scrubbing section and adverse current absorption scrubbing section in the said scrubbing tower; Wherein, Said cooling absorption scrubbing section has the first cleaning solution spray equipment and the first corrugated plate packing layer, and the said first cleaning solution spray equipment is positioned at the top of the said first corrugated plate packing layer, and the said first cleaning solution spray equipment comprises the two row's nozzles that laterally arrange; Said two row's nozzles upwards and downwards spray cleaning solution respectively
Said adverse current absorption scrubbing section has the second cleaning solution spray equipment and the second corrugated plate packing layer; And the said second cleaning solution spray equipment is positioned at the top of the said second corrugated plate packing layer; The said second cleaning solution spray equipment comprises row's nozzle, and said row's nozzle sprays cleaning solution downwards
Said scrubbing tower has two communicate with each other vertical section; Said cooling absorption scrubbing section and said adverse current absorption scrubbing section lay respectively at said two vertical sections; Said adverse current absorption scrubbing section is arranged on the path of flue gas rising; Said cooling absorption scrubbing section is arranged on the path of flue gas decline, and said adverse current absorption scrubbing section is positioned at the downstream of said cooling absorption scrubbing section.
Preferably, in the described flue washing device, said scrubbing tower also comprise in order to the heat exchanger tube flue gas heat-shift, its inner bubbling air, said heat exchanger tube is positioned at the upper reaches of said cooling absorption scrubbing section.
Preferably, in the described flue washing device, said scrubbing tower also comprises the gas outlet, and said gas outlet is connected with said heat exchanger tube, discharges so that flue gas mixes the back with the air of said heat exchanger tube.
Preferably, in the described flue washing device, said heat exchanger tube is connected with blower fan.
Preferably, in the described flue washing device, said scrubbing tower also comprises demister, and said demister is positioned at the downstream of said adverse current absorption scrubbing section.
Preferably, described flue washing device also comprises:
The cleaning solution EGR; Said cleaning solution EGR comprises cleaning solution storage pool and the detergent circulator that is communicated with said cleaning solution storage pool; Said cleaning solution storage pool is communicated with said scrubbing tower, and is communicated with the said first cleaning solution spray equipment and the second cleaning solution spray equipment through detergent circulator.
Preferably, in the described flue washing device, the bottom of said scrubbing tower is provided with the cleaning solution outlet, and said cleaning solution storage pool is communicated with said cleaning solution outlet.
The scrubbing tower of flue washing device of the present invention comprises cooling absorption scrubbing section and adverse current absorption scrubbing section; Flue gas gets into cooling absorption scrubbing section; At first the cleaning solution with the ejection of the first cleaning solution spray equipment contacts, then at the first corrugated plate packing layer and the abundant haptoreaction of cleaning solution, said process; Can partly remove the pollutants such as flue dust in the flue gas on the one hand; Can reduce flue-gas temperature significantly on the other hand, reduce the volume flow of flue gas, help to reduce the sectional area of adverse current absorption scrubbing section.In adverse current absorption scrubbing section,, then on the second corrugated plate packing layer, can form liquid film because the second cleaning solution spray equipment is arranged on the top of the second corrugated plate packing layer.When flue gas moves upward, at first get into the second corrugated plate packing layer, collide back and forth at the second corrugated plate packing laminar surface, fully contact with liquid film.Through said process, the flue dust in the flue gas is adsorbed, and pollutants such as while sulfur dioxide have also obtained abundant reaction.Utilize flue washing device of the present invention, realized high efficiency flue-gas dust-removing and desulfurization.
In addition, utilize the flue gas heating air, heated air is directed into the position of gas outlet through heat transfer zone; Yet through the flue gas of washing and discharge again after heated air mixes; Can improve the discharge temperature of flue gas, reduce smoke moisture, prevent that white mist from appearring in the place, gas outlet of flue washing device.
The volume of flue washing device of the present invention is little, in light weight, is applicable to the main frame of offshore platform or navigating ship, the flue gas processing of boiler, also satisfies the miniaturization demand of land fume treatment auxiliary.
Description of drawings
Fig. 1 is the structural representation of flue washing device of the present invention.
The specific embodiment
As shown in Figure 1; The present invention provides a kind of flue washing device, comprises scrubbing tower, is provided with cooling absorption scrubbing section 2 and adverse current absorption scrubbing section 10 in the said scrubbing tower; Wherein, Said cooling absorption scrubbing section has the first cleaning solution spray equipment 3 and the first corrugated plate packing layer 5, and the said first cleaning solution spray equipment 3 is positioned at the top of the said first corrugated plate packing layer 5, and the said first cleaning solution spray equipment comprises the two row's nozzles that laterally arrange; Said two row's nozzles upwards and downwards spray cleaning solution respectively; Said adverse current absorption scrubbing section has the second cleaning solution spray equipment 11 and the second corrugated plate packing layer 6, and the said second cleaning solution spray equipment 11 is positioned at the top of the said second corrugated plate packing layer 6, and the said second cleaning solution spray equipment comprises that one arranges nozzle; Said row's nozzle sprays cleaning solution downwards; Said scrubbing tower has two communicate with each other vertical section, and said cooling absorption scrubbing section 2 and said adverse current absorption scrubbing section 10 lay respectively at said two vertical sections, and said adverse current absorption scrubbing section is arranged on the path that flue gas rises; Said cooling absorption scrubbing section is arranged on the path of flue gas decline, and said adverse current absorption scrubbing section is positioned at the downstream of said cooling absorption scrubbing section.
In the described flue washing device, said scrubbing tower also comprise in order to the heat exchanger tube 15 flue gas heat-shift, its inner bubbling air, said heat exchanger tube is positioned at the upper reaches of said cooling absorption scrubbing section 2.
In the described flue washing device, said scrubbing tower also comprises gas outlet 13, and said gas outlet 13 is connected with said heat exchanger tube 15, discharges so that flue gas mixes the back with the air of said heat exchanger tube.
In the described flue washing device, said heat exchanger tube 15 is connected with blower fan 16.
In the described flue washing device, said scrubbing tower also comprises demister 12, and said demister 2 is positioned at the downstream of said adverse current absorption scrubbing section 10.
Described flue washing device; Also comprise: the cleaning solution EGR; Said cleaning solution EGR comprises cleaning solution storage pool 8 and the detergent circulator 9 that is communicated with said cleaning solution storage pool 8; Said cleaning solution storage pool 8 is communicated with said scrubbing tower, and is communicated with the said first cleaning solution spray equipment 3 and the second cleaning solution spray equipment 11 through detergent circulator 9.
In the described flue washing device, the bottom of said scrubbing tower is provided with cleaning solution outlet 7, and said cleaning solution storage pool 8 is communicated with said cleaning solution outlet 7.
Former flue gas 17 gets into cooling absorption scrubbing section 2 through after former smoke inlet pipe 1 and heat exchanger tube 15 heat exchange; Vaporific cleaning solution with 3 ejections of the first cleaning solution spray equipment contacts earlier; Flue gas and cleaning solution get into the first corrugated plate packing layer simultaneously; Collide back and forth at the first corrugated plate packing laminar surface, make flue gas fully contact mixing with cleaning solution.In this course, flue-gas temperature declines to a great extent, and according to equation of gaseous state, the volume flow of flue gas also declines to a great extent thereupon.Under the certain condition of flue gas flow rate, the flue gas volume flow declines to a great extent, for the sectional area that reduces adverse current absorption scrubbing section 10 provides condition.
At adverse current absorption scrubbing section 10, the cleaning solution under the second cleaning solution spray equipment, 11 sprays of top forms liquid film at the second corrugated plate packing laminar surface.After flue gas gets into the second corrugated plate packing layer, collide back and forth at the second corrugated plate packing laminar surface, fully contact with liquid film, flue dust is adsorbed, and pollutants such as sulfur dioxide have also obtained abundant reaction.
The corrugated plate packing layer has very high specific surface; Flue gas can collide with the corrugated plating surface through the corrugated plate packing layer time back and forth; The liquid film on corrugated plating surface can fully capture the solid particle in the flue gas; Guaranteed that also pollutants such as sulfur dioxide and cleaning solution have the sufficient reaction time, thereby reached desulfurization dust-removing efficiency efficiently.Utilize the surface characteristic of corrugated plating, for desulfurization and denitration medium provide desirable reaction bed.Among the present invention, the first corrugated plate packing layer that is positioned at cooling absorption scrubbing section is a rough undulation plate packing layer, and the second corrugated plate packing layer that is positioned at adverse current absorption scrubbing section is an insertion waves plate packing layer.
Flue gas rises through the second corrugated plate packing layer continued, and with reverse contact of cleaning solution under the second cleaning solution spray equipment, 11 sprays of top, pollutants such as flue dust that is left in the flue gas and sulfur dioxide further are adsorbed reaction.
Through demister 12, the drop that carries in the flue gas is tackled.Heat exchanger tube is connected through pipeline 14 with the gas outlet of scrubbing tower; The air that will pass through heat exchange feeds the gas outlet, makes that can mix the back with hot-air through the flue gas that washs discharges, and has improved the temperature of flue gas; Reduced the humidity of flue gas, prevented that white mist from appearring in the place, gas outlet of flue washing device.
Cleaning solution can be allocated according to the composition of flue gas.Cleaning solution is discharged through the cleaning solution outlet of wash tower bottoms, gets in the cleaning solution storage pool.In the cleaning solution storage pool, sediment is separated, and additional cleaning solution, to satisfy the circulation demand of cleaning solution.
Above-mentioned each embodiment only is used to explain the present invention; The structure of each parts and connected mode all can change to some extent; On the basis of technical scheme of the present invention; All improvement and equivalents of the connection and the structure of individual component being carried out according to the principle of the invention all should not got rid of outside protection scope of the present invention.

Claims (7)

1. a flue washing device comprises scrubbing tower, it is characterized in that; Be provided with cooling absorption scrubbing section and adverse current absorption scrubbing section in the said scrubbing tower, wherein, said cooling absorption scrubbing section has the first cleaning solution spray equipment and the first corrugated plate packing layer; The said first cleaning solution spray equipment is positioned at the top of the said first corrugated plate packing layer; The said first cleaning solution spray equipment comprises the two row's nozzles that laterally arrange, and said two row's nozzles make progress respectively and downward ejection cleaning solution
Said adverse current absorption scrubbing section has the second cleaning solution spray equipment and the second corrugated plate packing layer; And the said second cleaning solution spray equipment is positioned at the top of the said second corrugated plate packing layer; The said second cleaning solution spray equipment comprises row's nozzle, and said row's nozzle sprays cleaning solution downwards
Said scrubbing tower has two communicate with each other vertical section; Said cooling absorption scrubbing section and said adverse current absorption scrubbing section lay respectively at said two vertical sections; Said adverse current absorption scrubbing section is arranged on the path of flue gas rising; Said cooling absorption scrubbing section is arranged on the path of flue gas decline, and said adverse current absorption scrubbing section is positioned at the downstream of said cooling absorption scrubbing section.
2. flue washing device as claimed in claim 1 is characterized in that, said scrubbing tower also comprise in order to the heat exchanger tube flue gas heat-shift, its inner bubbling air, said heat exchanger tube is positioned at the upper reaches of said cooling absorption scrubbing section.
3. flue washing device as claimed in claim 2 is characterized in that said scrubbing tower also comprises the gas outlet, and said gas outlet is connected with said heat exchanger tube, discharges so that flue gas mixes the back with the air of said heat exchanger tube.
4. like claim 2 or 3 described flue washing devices, it is characterized in that said heat exchanger tube is connected with blower fan.
5. flue washing device as claimed in claim 1 is characterized in that said scrubbing tower also comprises demister, and said demister is positioned at the downstream of said adverse current absorption scrubbing section.
6. flue washing device as claimed in claim 1 is characterized in that, also comprises:
The cleaning solution EGR; Said cleaning solution EGR comprises cleaning solution storage pool and the detergent circulator that is communicated with said cleaning solution storage pool; Said cleaning solution storage pool is communicated with said scrubbing tower, and is communicated with the said first cleaning solution spray equipment and the second cleaning solution spray equipment through detergent circulator.
7. flue washing device as claimed in claim 6 is characterized in that the bottom of said scrubbing tower is provided with the cleaning solution outlet, and said cleaning solution storage pool is communicated with said cleaning solution outlet.
CN2012102259064A 2012-03-23 2012-06-29 Smoke washing device Pending CN102716656A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012102259064A CN102716656A (en) 2012-03-23 2012-06-29 Smoke washing device

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN201210080967.6 2012-03-23
CN201210080967 2012-03-23
CN2012102259064A CN102716656A (en) 2012-03-23 2012-06-29 Smoke washing device

Publications (1)

Publication Number Publication Date
CN102716656A true CN102716656A (en) 2012-10-10

Family

ID=46942601

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012102259064A Pending CN102716656A (en) 2012-03-23 2012-06-29 Smoke washing device

Country Status (1)

Country Link
CN (1) CN102716656A (en)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103071362A (en) * 2013-01-29 2013-05-01 梅州环保设备有限公司 Dedusting and desulfuration integrated device for smoke and application of integrated device
CN103316553A (en) * 2013-07-05 2013-09-25 江苏博际喷雾***有限公司 Efficient wet-type variable flow fog-spraying sprinkling dust-removing purification device
CN105477981A (en) * 2016-01-20 2016-04-13 南通亚泰工程技术有限公司 Energy-saving marine desulfurizer
CN106474891A (en) * 2016-12-08 2017-03-08 上海酒店设备工程成套南翔厂有限公司 Flue gas washing purifier
CN106669374A (en) * 2017-03-15 2017-05-17 云南驰宏锌锗股份有限公司 Treatment equipment for temperature-rise flue gas containing dust, oil and sulfur dioxide for zinc smelting and roasting furnace
CN106943822A (en) * 2017-04-27 2017-07-14 天津普洛仙科技有限公司 A kind of high dustiness smoke duster of high temperature
CN107029523A (en) * 2017-06-14 2017-08-11 湘潭大学 Foam scrubber
CN107042033A (en) * 2017-03-28 2017-08-15 鲍守明 Efficient boiler dust-removal and desulfurizing denitrification apparatus
JP2018501954A (en) * 2015-01-23 2018-01-25 ベイジン ボーユアン ヘンシェン ハイ−テクノロジー カンパニー リミテッド Exhaust gas dust removal method and dust removal agent
CN107648960A (en) * 2017-10-25 2018-02-02 安徽华创环保设备科技有限公司 A kind of rinsing type emission-control equipment
CN107764104A (en) * 2017-10-27 2018-03-06 山东佩森环保科技股份有限公司 A kind of new type heat exchanger of scrubbing tower
CN108392970A (en) * 2018-05-08 2018-08-14 威海普益船舶环保科技有限公司 Exhaust gas scrubber and sea transport ship
CN108939888A (en) * 2018-08-21 2018-12-07 北京鼎翰科技有限公司 A kind of burning station-service high-temp waste gas desulfurization purifier
CN109141065A (en) * 2017-06-15 2019-01-04 广州新致晟环保科技有限公司 Tail gas clean-up and heat recovery system and method for Treatment of Sludge
CN109133572A (en) * 2017-06-15 2019-01-04 广州新致晟环保科技有限公司 The purification of exhaust gas for sludge drying and heat recovery system and method
CN112642281A (en) * 2020-12-28 2021-04-13 宜宾海翔化工有限责任公司 Cooling washing dust removal system and method for hydrogen sulfide acid production

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001029741A (en) * 1999-07-27 2001-02-06 Ishikawajima Harima Heavy Ind Co Ltd Water supply replenishing method for wet flue gas treating installation and device therefor
CN200995120Y (en) * 2006-12-04 2007-12-26 无锡利保科技发展有限公司 Smoke desulfurizing absorbing tower by integrated glass fiber reinforced plastic ammonia method
CN201249100Y (en) * 2008-07-16 2009-06-03 上海迪浩环保科技有限公司 Rotary spray thionizer
CN201357048Y (en) * 2009-02-16 2009-12-09 周松玉 Packed absorption tower capable of absorbing clockwise and counter-clockwise
WO2011142405A1 (en) * 2010-05-13 2011-11-17 戸田工業株式会社 Wet-type flue-gas desulfurization device using three-way spray nozzle
CN202506308U (en) * 2012-03-23 2012-10-31 北京东旭宏业科技有限公司 Smoke washing device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001029741A (en) * 1999-07-27 2001-02-06 Ishikawajima Harima Heavy Ind Co Ltd Water supply replenishing method for wet flue gas treating installation and device therefor
CN200995120Y (en) * 2006-12-04 2007-12-26 无锡利保科技发展有限公司 Smoke desulfurizing absorbing tower by integrated glass fiber reinforced plastic ammonia method
CN201249100Y (en) * 2008-07-16 2009-06-03 上海迪浩环保科技有限公司 Rotary spray thionizer
CN201357048Y (en) * 2009-02-16 2009-12-09 周松玉 Packed absorption tower capable of absorbing clockwise and counter-clockwise
WO2011142405A1 (en) * 2010-05-13 2011-11-17 戸田工業株式会社 Wet-type flue-gas desulfurization device using three-way spray nozzle
CN202506308U (en) * 2012-03-23 2012-10-31 北京东旭宏业科技有限公司 Smoke washing device

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103071362A (en) * 2013-01-29 2013-05-01 梅州环保设备有限公司 Dedusting and desulfuration integrated device for smoke and application of integrated device
CN103071362B (en) * 2013-01-29 2015-07-22 梅州环保设备有限公司 Dedusting and desulfuration integrated device for smoke and application of integrated device
CN103316553A (en) * 2013-07-05 2013-09-25 江苏博际喷雾***有限公司 Efficient wet-type variable flow fog-spraying sprinkling dust-removing purification device
JP2018501954A (en) * 2015-01-23 2018-01-25 ベイジン ボーユアン ヘンシェン ハイ−テクノロジー カンパニー リミテッド Exhaust gas dust removal method and dust removal agent
US10744452B2 (en) 2015-01-23 2020-08-18 Beijing Boyuan Hengsheng High-Technology Co., Ltd. Method for waste gas dedusting and dedusting agent
CN105477981A (en) * 2016-01-20 2016-04-13 南通亚泰工程技术有限公司 Energy-saving marine desulfurizer
CN106474891A (en) * 2016-12-08 2017-03-08 上海酒店设备工程成套南翔厂有限公司 Flue gas washing purifier
CN106669374A (en) * 2017-03-15 2017-05-17 云南驰宏锌锗股份有限公司 Treatment equipment for temperature-rise flue gas containing dust, oil and sulfur dioxide for zinc smelting and roasting furnace
CN107042033A (en) * 2017-03-28 2017-08-15 鲍守明 Efficient boiler dust-removal and desulfurizing denitrification apparatus
CN106943822A (en) * 2017-04-27 2017-07-14 天津普洛仙科技有限公司 A kind of high dustiness smoke duster of high temperature
CN106943822B (en) * 2017-04-27 2019-12-13 宁波双能环保科技有限公司 High-temperature high-dust-content flue gas dust remover
CN107029523A (en) * 2017-06-14 2017-08-11 湘潭大学 Foam scrubber
CN109133572A (en) * 2017-06-15 2019-01-04 广州新致晟环保科技有限公司 The purification of exhaust gas for sludge drying and heat recovery system and method
CN109141065A (en) * 2017-06-15 2019-01-04 广州新致晟环保科技有限公司 Tail gas clean-up and heat recovery system and method for Treatment of Sludge
CN109133572B (en) * 2017-06-15 2024-06-04 广州正晟科技有限公司 Purification and heat recovery system and method for sludge drying waste gas
CN109141065B (en) * 2017-06-15 2024-06-07 广州正晟科技有限公司 Tail gas purification and heat recovery system and method for sludge treatment
CN107648960A (en) * 2017-10-25 2018-02-02 安徽华创环保设备科技有限公司 A kind of rinsing type emission-control equipment
CN107764104A (en) * 2017-10-27 2018-03-06 山东佩森环保科技股份有限公司 A kind of new type heat exchanger of scrubbing tower
CN108392970A (en) * 2018-05-08 2018-08-14 威海普益船舶环保科技有限公司 Exhaust gas scrubber and sea transport ship
CN108939888A (en) * 2018-08-21 2018-12-07 北京鼎翰科技有限公司 A kind of burning station-service high-temp waste gas desulfurization purifier
CN108939888B (en) * 2018-08-21 2021-09-21 淄博鹏达环保科技有限公司 High-temperature waste gas desulfurization and purification device for incineration plant
CN112642281A (en) * 2020-12-28 2021-04-13 宜宾海翔化工有限责任公司 Cooling washing dust removal system and method for hydrogen sulfide acid production

Similar Documents

Publication Publication Date Title
CN102716656A (en) Smoke washing device
US9700837B2 (en) Wet scrubber nozzle system and method of use for cleaning a process gas
US9468885B2 (en) Method and apparatus for wet desulfurization spray towers
CN205379793U (en) Smoke desulfurizing dust collector
KR101698999B1 (en) Ship flue gas scrubbing apparatus and method
JP5631985B2 (en) Improved gas cleaning apparatus and method
CN110567290B (en) Unsaturated high-humidity tail gas white smoke eliminating device and method
CN101301574B (en) Multistage flue gas desulfurization spray tower
US8968450B1 (en) Wet scrubber design
CN106139866A (en) A kind of employing adverse current opposite-flushing type turbulence washing tower waste gas treatment process and device thereof
CN103100284A (en) Flue gas dedusting circulating purifying device
CN104324597A (en) Combined flue gas cleaning system and flue gas cleaning method thereof
JP2012528707A (en) Cleaning tower and associated flue gas cleaning equipment
CN202506308U (en) Smoke washing device
CN1899675A (en) Reverse flow type seawater desulfurizing and absorption tower
CN105233657A (en) Flue gas desulphurization and dedusting advanced treatment technology and apparatus thereof
CN105999916A (en) Air purifier
CN201073590Y (en) Absorbing tower with flue gas desulfurization
CN206924616U (en) A kind of flue gas desulfurization dehumidifying set treatment device
CN107101218B (en) The compact flue gas depth waste-heat recovery device of low-resistance
CN203123741U (en) Fume dedusting circulation purification device
CN101721901A (en) Flue gas desulfurization and denitration purifying device in chimney of horizontal flue
CN115040962A (en) Carbon dioxide absorption system
CN210131526U (en) Wet flue gas desulfurization, denitration and white control integrated device
CN208878182U (en) A kind of exhaust treatment system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
ASS Succession or assignment of patent right

Owner name: BEIJING DONGZHAN KEBO TECHNOLOGY CO., LTD.

Free format text: FORMER OWNER: BEIJING DONGXU HONGYE TECHNOLOGY CO., LTD.

Effective date: 20130617

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 100082 HAIDIAN, BEIJING TO: 100095 HAIDIAN, BEIJING

TA01 Transfer of patent application right

Effective date of registration: 20130617

Address after: 100095, Beijing Haidian District Su Tuo silk two factory East Cottage

Applicant after: Beijing Dongzhan Kebo Technology Co., Ltd.

Address before: 9 Anning, Zhuang Xisan, Haidian District, and No. 1, building 6, unit 100082, 202, Beijing

Applicant before: Beijing Dongxu Hongye Technology Co., Ltd.

C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20121010