CN108031271A - A kind of flue gas desulfurization device - Google Patents

A kind of flue gas desulfurization device Download PDF

Info

Publication number
CN108031271A
CN108031271A CN201810050317.4A CN201810050317A CN108031271A CN 108031271 A CN108031271 A CN 108031271A CN 201810050317 A CN201810050317 A CN 201810050317A CN 108031271 A CN108031271 A CN 108031271A
Authority
CN
China
Prior art keywords
heat exchanger
cooling water
desulfurizing tower
slurries
slurry
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
CN201810050317.4A
Other languages
Chinese (zh)
Inventor
李爱云
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 Xing Sheng Technology Co Ltd
Original Assignee
Beijing Xing Sheng 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 Xing Sheng Technology Co Ltd filed Critical Beijing Xing Sheng Technology Co Ltd
Priority to CN201810050317.4A priority Critical patent/CN108031271A/en
Publication of CN108031271A publication Critical patent/CN108031271A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/80Semi-solid phase processes, i.e. by using slurries
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases
    • 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
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Treating Waste Gases (AREA)

Abstract

The present invention provides a kind of flue gas desulfurization device, belong to technical field of waste gas treatment, including desulfurizing tower, slurry pool and First Heat Exchanger, the side wall of desulfurizing tower is equipped with gas inlet, the top of desulfurizing tower is equipped with exhanst gas outlet, desulfurizing tower is internally provided with spray equipment, slurry pool is arranged at the inner bottom surface of desulfurizing tower, First Heat Exchanger has slurry inlet, serum outlet, cooling water inlet and cooling water outlet, the slurry inlet of First Heat Exchanger is connected with slurry pool by the first slurries pipeline, the serum outlet of First Heat Exchanger is connected with spray equipment by the second slurries pipeline, on first slurries pipeline or the second slurries pipeline is pumped equipped with slurries, cooling water inlet pipe is equipped with cooling water inlet, cooling water outlet pipe is equipped with cooling water outlet.Its is simple in structure, First Heat Exchanger can to desulfurization slurry carry out cooling treatment, ensure from desulfurizing tower outflow flue-gas temperature and humidity it is relatively low, reduce exhanst gas outlet emit white cigarette phenomenon occur, substantially increase desulfurization, efficiency of dust collection.

Description

A kind of flue gas desulfurization device
Technical field
The present invention relates to technical field of waste gas treatment, in particular to a kind of flue gas desulfurization device.
Background technology
In conventional wet lay flue gas desulfurization technique, it will usually which multiple spray equipments and supporting slurries are set in desulfurizing tower Pump, slurries pump power driving under, desulfurization slurry via desulfurization slurry pond-pipeline-slurries pump-pipeline-spray equipment nozzle Sprayed, after desulfurization slurry carries out washing desulphurization dedusting to flue gas, return to slurry pool and continue cycling through use.Meanwhile desulfurization is starched Liquid heat absorption flue gas heat partial moisture is evaporated and mixed with flue gas, and flue gas cool-down simultaneously becomes saturated flue gas into saturation state, satisfies Carry dust, gypsum, droplet, vapor etc. at the same time with flue gas and flow out desulfurization after the processing of further demisting into desulfurizing tower top Tower.Since the saturated flue gas humidity for flowing out desulfurizing tower is larger, the condensables such as certain soluble salt, sulfate, organic matter are carried Grain thing, it will certain pollution is caused to atmospheric environment;It can also cause serious chimney " white cigarette " phenomenon at the same time.
The content of the invention
The purpose of embodiment of the present invention is to provide a kind of flue gas desulfurization device, its is simple in structure, easy to use, can It is preferable to improve the above problem.
What embodiments of the present invention were realized in:
Embodiments of the present invention provide a kind of flue gas desulfurization device, including desulfurizing tower, slurry pool and First Heat Exchanger, The side wall of the desulfurizing tower is equipped with gas inlet, and the top of the desulfurizing tower is equipped with exhanst gas outlet, and the inside of the desulfurizing tower is set There is spray equipment, for the spray equipment between the gas inlet and the exhanst gas outlet, the slurry pool is arranged at institute State the inner bottom surface of desulfurizing tower, the First Heat Exchanger is located at the outside of the desulfurizing tower, the First Heat Exchanger have slurries into Mouth, serum outlet, cooling water inlet and cooling water outlet, the slurry inlet of the First Heat Exchanger and the slurry pool pass through the One slurries pipeline connects, and the serum outlet of the First Heat Exchanger is connected with the spray equipment by the second slurries pipeline, institute State on the first slurries pipeline or the second slurries pipeline is pumped equipped with slurries, be equipped with and be used for described at the cooling water inlet The cooling water inlet pipe of cooling water is conveyed in First Heat Exchanger, the cooling for being used for discharging cooling water is equipped with the cooling water outlet Water outlet pipe.
Alternatively, the second heat exchanger is additionally provided with the cooling water outlet pipe.
Alternatively, second heat exchanger is heat pump or Boiler Air Heater's.
Alternatively, the First Heat Exchanger is shell-and-tube heat exchanger, plate heat exchanger or band-tube type heat exchanger.
Alternatively, the First Heat Exchanger is shell-and-tube heat exchanger, the first slurries pipeline and second slurry pipe Tube side of the road respectively with the shell-and-tube heat exchanger connects, the cooling water inlet pipe and the cooling water outlet pipe respectively with institute State the shell side connection of shell-and-tube heat exchanger.
Alternatively, the quantity of the spray equipment is multiple, vertical side of multiple spray equipments along the desulfurizing tower To interval setting.
Embodiments of the present invention provide another flue gas desulfurization device, including desulfurizing tower, slurry pool, slurries recycling dress Put and First Heat Exchanger, the side wall of the desulfurizing tower are equipped with gas inlet, the top of the desulfurizing tower is equipped with exhanst gas outlet, described Desulfurizing tower is internally provided with spray equipment, and the spray equipment is described between the gas inlet and the exhanst gas outlet Slurry pool is arranged at the outside of the desulfurizing tower, and the slurries retracting device is arranged at the inside of the desulfurizing tower and positioned at described The lower section of spray equipment, the slurries retracting device are connected with the slurry pool by pipeline, and the First Heat Exchanger is located at institute The outside of desulfurizing tower is stated, the First Heat Exchanger has slurry inlet, serum outlet, cooling water inlet and cooling water outlet, institute The slurry inlet for stating First Heat Exchanger is connected with the slurry pool by the first slurries pipeline, and the slurries of the First Heat Exchanger go out Mouth is connected with the spray equipment by the second slurries pipeline, is set on the first slurries pipeline or on the second slurries pipeline There is slurries pump, cooling water inlet pipe is equipped with the cooling water inlet, cooling water outlet pipe is equipped with the cooling water outlet.
Alternatively, the second heat exchanger is additionally provided with the cooling water outlet pipe.
Alternatively, second heat exchanger is heat pump or Boiler Air Heater's.
Alternatively, the First Heat Exchanger is shell-and-tube heat exchanger, the first slurries pipeline and second slurry pipe Tube side of the road respectively with the shell-and-tube heat exchanger connects, the cooling water inlet pipe and the cooling water outlet pipe respectively with institute State the shell side connection of shell-and-tube heat exchanger.
Embodiments of the present invention have the advantages that:
The flue gas desulfurization device that embodiment of the present invention provides, its is simple in structure, easy to use, and desulfurizing tower can be to flue gas Desulfurization and dedusting processing is carried out, First Heat Exchanger can carry out cooling treatment to desulfurization slurry, ensure the flue gas from desulfurizing tower outflow Temperature is relatively low, reduces the phenomenon generation that exhanst gas outlet emits white cigarette, substantially increases desulfurization, dedusting, demisting efficiency;Second heat exchanger Heat in cooling water can be recycled, substantially increase the utilization rate of thermal energy.
Brief description of the drawings
, below will be to required use in embodiment in order to illustrate more clearly of the technical solution of embodiment of the present invention Attached drawing be briefly described, it will be appreciated that the following drawings illustrate only the certain embodiments of the present invention, therefore should not be seen Work is the restriction to scope, for those of ordinary skill in the art, without creative efforts, can be with Other relevant attached drawings are obtained according to these attached drawings.
Fig. 1 is the structure diagram of the flue gas desulfurization device of embodiment of the present invention one;
Fig. 2 is the structure diagram of the flue gas desulfurization device of embodiment of the present invention two.
Icon:10- desulfurizing towers;101- gas inlets;102- exhanst gas outlets;11- slurry pools;12- First Heat Exchangers;121- Slurry inlet;122- serum outlets;123- cooling water inlets;124- cooling water outlets;125- the first slurries pipelines;126- second Slurries pipeline;127- slurries pump;128- cooling water inlet pipes;129- cooling water outlet pipes;13- spray equipments;14- second exchanges heat Device;20- slurries retracting devices.
Embodiment
To make the purpose, technical scheme and advantage of embodiment of the present invention clearer, implement below in conjunction with the present invention Attached drawing in mode, is clearly and completely described the technical solution in embodiment of the present invention, it is clear that described reality The mode of applying is a part of embodiment of the present invention, rather than whole embodiments.Usually it is described and illustrated herein in the accompanying drawings The component of embodiment of the present invention can arrange and design with a variety of configurations.
Therefore, the detailed description of the embodiments of the present invention to providing in the accompanying drawings is not intended to limit requirement guarantor below The scope of the present invention of shield, but it is merely representative of the selected embodiment of the present invention.Based on the embodiment in the present invention, ability The every other embodiment that domain those of ordinary skill is obtained without creative efforts, belongs to the present invention The scope of protection.
It should be noted that in the case where there is no conflict, the feature in embodiment and embodiment in the present invention can To be mutually combined.
It should be noted that:Similar label and letter represents similar terms in following attached drawing, therefore, once a certain Xiang Yi It is defined, then it further need not be defined and explained in subsequent attached drawing in a attached drawing.
In the description of the present invention, it is necessary to explanation, term " on ", " under ", " vertical ", " level ", " interior ", " outer " etc. The orientation or position relationship of instruction are usual based on orientation shown in the drawings or position relationship, or during invention product use The orientation or position relationship put, or the orientation that usually understands of those skilled in the art or position relationship, or the hair Bright product using when the orientation usually put or position relationship, be for only for ease of the description present invention and simplify description, rather than Indicate or imply that signified device or element there must be specific orientation, with specific azimuth configuration and operation, therefore cannot It is interpreted as limitation of the present invention.In addition, term " first ", " second " etc. are only used for distinguishing description, and it is not intended that instruction Or imply relative importance.
In the description of the present invention, it is also necessary to explanation, unless otherwise clearly defined and limited, term " setting ", " installation ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or one Connect body;Can mechanically connect or be electrically connected;It can be directly connected, can also be indirect by intermediary It is connected, can is the connection inside two elements.For the ordinary skill in the art, on being understood with concrete condition State the concrete meaning of term in the present invention.
Embodiment 1
Refering to what is shown in Fig. 1, embodiment of the present invention one provides flue gas desulfurization device, including desulfurizing tower 10, slurry pool 11 With First Heat Exchanger 12.
Desulfurizing tower 10 is used to carry out desulfurization process to flue gas.The side wall of desulfurizing tower 10 is equipped with gas inlet 101, pending Flue gas can be passed through in desulfurizing tower 10 from gas inlet 101;The top of desulfurizing tower 10 is equipped with exhanst gas outlet 102, and flue gas can be from Exhanst gas outlet 102 is discharged into outside desulfurizing tower 10.Certainly, exhanst gas outlet 102 can also be arranged on the side wall of desulfurizing tower 10 by At position closely at the top of it.
Slurry pool 11 is used to contain desulfurization slurry, and slurry pool 11 is arranged on the inner bottom surface of desulfurizing tower 10, slurry pool 11 it is upper Level height position is held to be less than the level height position of gas inlet 101.
Desulfurizing tower 10 is internally provided with spray equipment 13, and spray equipment 13 is arranged on gas inlet 101 and exhanst gas outlet 102 Between.
First Heat Exchanger 12 is located at the outside of desulfurizing tower 10, and First Heat Exchanger 12 has slurry inlet 121, serum outlet 122nd, cooling water inlet 123 and cooling water outlet 124.
The slurry inlet 121 of First Heat Exchanger 12 is connected with slurry pool 11 by the first slurries pipeline 125, First Heat Exchanger 12 serum outlet 122 is connected with spray equipment 13 by the second slurries pipeline 126, and the first slurries pipeline 125 is equipped with slurries Pump 127, certainly, slurries pump 127 can also be arranged on the second slurries pipeline 126.Slurries pump 127 can be by slurry pool 11 Desulfurization slurry is extracted out and is transported to spray equipment 13, is then sprayed from spray equipment 13, and such flue gas is flowed to from gas inlet 101 It can be contacted during exhanst gas outlet 102 with desulfurization slurry, under the action of desulfurization slurry, sulfide and dust quilt in flue gas Remove, meanwhile, the heat in flue gas can also be desulfurized slurries absorption, and partial moisture is evaporated and is mixed with flue gas, and flue gas is wet Degree increase, so that the flue-gas temperature of outflow desulfurizing tower 10 reduces.
The cooling water inlet pipe for being used for that cooling water to be conveyed into the First Heat Exchanger 12 is equipped with cooling water inlet 123 128, one end of the remote First Heat Exchanger 12 of cooling water inlet pipe 128 is used to connect with water source, is equipped with cooling water outlet 124 For discharging the cooling water outlet pipe 129 of cooling water.Cooling water is passed through First Heat Exchanger 12 from cooling water inlet pipe 128, from cold But water outlet pipe 129 flows out.During desulfurization slurry flows through First Heat Exchanger 12, the heat in desulfurization slurry can transmit To cooling water, so as to play the role of cooling to desulfurization slurry, and then flue gas is cooled down by desulfurization slurry, flue gas Humidity reduce, greatly reduce exhanst gas outlet 102 outflow white cigarette amount, while also so that outflow flue gas in carry droplet, The condensable such as soluble salt, sulfuric acid mist and organic matter particle is reduced.
It should be noted that First Heat Exchanger 12 can use shell-and-tube heat exchanger, the first slurries pipeline 125 and the second slurry Liquid pipe road 126 is connected with the tube side of shell-and-tube heat exchanger respectively, cooling water inlet pipe 128 and cooling water outlet pipe 129 respectively with The shell side connection of shell-and-tube heat exchanger.Certainly, First Heat Exchanger 12 can also use plate heat exchanger, band-tube type heat exchanger or its The heat exchanger of his form.
Contain certain heat, if be directly discharged in environment, meeting in the cooling water excluded from cooling water outlet pipe 129 Hot loss of energy is caused, in order to reasonably recycle the thermal energy in cooling water, can be set on cooling water outlet pipe 129 Put the second heat exchanger 14.
Second heat exchanger 14 can use heat pump, and heat pump can extract the thermal energy in cooling water and improve the product of thermal energy Matter, being then delivered to thermal energy needs the place for using thermal energy.
Second heat exchanger 14 can also use Boiler Air Heater's, and Boiler Air Heater's can extract the thermal energy in cooling water Come and be used for heating boiler air-supply.
It should be noted that in order to improve the desulfurization and dedusting effect of flue gas desulfurization device, can be set in desulfurizing tower 10 Multiple spray equipments 13, multiple spray equipments 13 along desulfurizing tower 10 vertical direction be arranged at intervals, this makes it possible to flue gas into The multiple desulfurization and dedusting processing of row.Correspondingly, the quantity and the number of spray equipment 13 of quantity and the slurries pump 127 of First Heat Exchanger 12 Measure identical and correspond.
Embodiment 2
Refering to what is shown in Fig. 2, embodiment of the present invention two provides a kind of flue gas desulfurization device, including desulfurizing tower 10, slurries Pond 11, slurries retracting device 20 and First Heat Exchanger 12.
Present embodiment and embodiment one are used difference lies in the outside that slurry pool 11 is arranged on to desulfurizing tower 10 Slurries retracting device 20 recycles the slurries sprayed from spray equipment 13, structure, operation principle and the generation of remaining part Technique effect it is identical with the component in embodiment one, may be referred to the corresponding contents in embodiment one, do not do herein superfluous State.
Refering to what is shown in Fig. 2, slurry pool 11 is arranged on the outside of desulfurizing tower 10, slurries retracting device 20 is arranged on desulfurizing tower 10 Inside and positioned at the lower section of spray equipment 13, slurries retracting device 20 connected with slurry pool 11 by pipeline, and slurries recycling fills Putting 20 can will be recycled from the slurries that spray equipment 13 sprays and be delivered in slurry pool 11.
The foregoing is merely the preferred embodiment of the present invention, is not intended to limit the invention, for this area For technical staff, the invention may be variously modified and varied.Within the spirit and principles of the invention, that is made is any Modification, equivalent substitution, improvement etc., should all be included in the protection scope of the present invention.

Claims (10)

  1. A kind of 1. flue gas desulfurization device, it is characterised in that including desulfurizing tower, slurry pool and First Heat Exchanger, the desulfurizing tower Side wall is equipped with gas inlet, and the top of the desulfurizing tower is equipped with exhanst gas outlet, and the desulfurizing tower is internally provided with spray equipment, institute Spray equipment is stated between the gas inlet and the exhanst gas outlet, the slurry pool is arranged at the interior bottom of the desulfurizing tower Face, the First Heat Exchanger are located at the outside of the desulfurizing tower, and the First Heat Exchanger has slurry inlet, serum outlet, cold But water inlet and cooling water outlet, the slurry inlet of the First Heat Exchanger are connected with the slurry pool by the first slurries pipeline Logical, the serum outlet of the First Heat Exchanger is connected with the spray equipment by the second slurries pipeline, first slurry pipe On road or the second slurries pipeline is pumped equipped with slurries, is equipped with and is used for into the First Heat Exchanger at the cooling water inlet The cooling water inlet pipe of cooling water is conveyed, the cooling water outlet pipe for being used for discharging cooling water is equipped with the cooling water outlet.
  2. 2. flue gas desulfurization device according to claim 1, it is characterised in that be additionally provided with second on the cooling water outlet pipe Heat exchanger.
  3. 3. flue gas desulfurization device according to claim 2, it is characterised in that second heat exchanger warms up for heat pump or boiler Wind device.
  4. 4. flue gas desulfurization device according to claim 1, it is characterised in that the First Heat Exchanger is pipe shell type heat exchange Device, plate heat exchanger or band-tube type heat exchanger.
  5. 5. flue gas desulfurization device according to claim 4, it is characterised in that the First Heat Exchanger is pipe shell type heat exchange Device, the tube side of the first slurries pipeline and the second slurries pipeline respectively with the shell-and-tube heat exchanger connects, described cold But the shell side of water water inlet pipe and the cooling water outlet pipe respectively with the shell-and-tube heat exchanger connects.
  6. 6. flue gas desulfurization device according to claim 1, it is characterised in that the quantity of the spray equipment is more to be multiple A spray equipment is arranged at intervals along the vertical direction of the desulfurizing tower.
  7. A kind of 7. flue gas desulfurization device, it is characterised in that including desulfurizing tower, slurry pool, slurries retracting device and First Heat Exchanger, The side wall of the desulfurizing tower is equipped with gas inlet, and the top of the desulfurizing tower is equipped with exhanst gas outlet, and the inside of the desulfurizing tower is set There is spray equipment, for the spray equipment between the gas inlet and the exhanst gas outlet, the slurry pool is arranged at institute The outside of desulfurizing tower is stated, the slurries retracting device is arranged at the inside of the desulfurizing tower and under the spray equipment Side, the slurries retracting device are connected with the slurry pool by pipeline, and the First Heat Exchanger is located at the outer of the desulfurizing tower Portion, the First Heat Exchanger have slurry inlet, serum outlet, cooling water inlet and cooling water outlet, the First Heat Exchanger Slurry inlet connected with the slurry pool by the first slurries pipeline, the serum outlet of the First Heat Exchanger and the spray Device is connected by the second slurries pipeline, and on the first slurries pipeline or the second slurries pipeline is pumped equipped with slurries, institute State and cooling water inlet pipe is equipped with cooling water inlet, cooling water outlet pipe is equipped with the cooling water outlet.
  8. 8. flue gas desulfurization device according to claim 7, it is characterised in that be additionally provided with second on the cooling water outlet pipe Heat exchanger.
  9. 9. flue gas desulfurization device according to claim 8, it is characterised in that second heat exchanger warms up for heat pump or boiler Wind device.
  10. 10. flue gas desulfurization device according to claim 7, it is characterised in that the First Heat Exchanger is pipe shell type heat exchange Device, the tube side of the first slurries pipeline and the second slurries pipeline respectively with the shell-and-tube heat exchanger connects, described cold But the shell side of water water inlet pipe and the cooling water outlet pipe respectively with the shell-and-tube heat exchanger connects.
CN201810050317.4A 2018-01-18 2018-01-18 A kind of flue gas desulfurization device Pending CN108031271A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810050317.4A CN108031271A (en) 2018-01-18 2018-01-18 A kind of flue gas desulfurization device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810050317.4A CN108031271A (en) 2018-01-18 2018-01-18 A kind of flue gas desulfurization device

Publications (1)

Publication Number Publication Date
CN108031271A true CN108031271A (en) 2018-05-15

Family

ID=62096403

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810050317.4A Pending CN108031271A (en) 2018-01-18 2018-01-18 A kind of flue gas desulfurization device

Country Status (1)

Country Link
CN (1) CN108031271A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109331639A (en) * 2018-11-30 2019-02-15 北京兴晟科技有限公司 A kind of flue gas desulfurization device with slurries filtering function
CN109364733A (en) * 2018-12-07 2019-02-22 山东金太阳设备制造有限公司 A kind of board-like slurries cooler
CN109381989A (en) * 2018-11-05 2019-02-26 华电电力科学研究院有限公司 The system and its working method of Multi-stage cooling cooperation-removal multiple pollutant in a kind of tower
CN110152460A (en) * 2019-06-14 2019-08-23 杭州蕴泽环境科技有限公司 It is a kind of to utilize the water-saving eliminating white smoke device and method of chimney sleeve

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN203886407U (en) * 2014-06-19 2014-10-22 南京凯盛开能环保能源有限公司 Flue gas purification and deep afterheat recycling integrated device
CN205019944U (en) * 2015-10-12 2016-02-10 李爱云 Flue gas desulfurization device
CN205850576U (en) * 2016-08-03 2017-01-04 天津华赛尔传热设备有限公司 A kind of flue gas desulfurization process system
CN107185329A (en) * 2017-07-24 2017-09-22 北京国电龙源环保工程有限公司 A kind of high-effective dust-removing and device for reclaiming moisture
CN207871901U (en) * 2018-01-18 2018-09-18 北京兴晟科技有限公司 A kind of flue gas desulfurization device

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN203886407U (en) * 2014-06-19 2014-10-22 南京凯盛开能环保能源有限公司 Flue gas purification and deep afterheat recycling integrated device
CN205019944U (en) * 2015-10-12 2016-02-10 李爱云 Flue gas desulfurization device
CN205850576U (en) * 2016-08-03 2017-01-04 天津华赛尔传热设备有限公司 A kind of flue gas desulfurization process system
CN107185329A (en) * 2017-07-24 2017-09-22 北京国电龙源环保工程有限公司 A kind of high-effective dust-removing and device for reclaiming moisture
CN207871901U (en) * 2018-01-18 2018-09-18 北京兴晟科技有限公司 A kind of flue gas desulfurization device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109381989A (en) * 2018-11-05 2019-02-26 华电电力科学研究院有限公司 The system and its working method of Multi-stage cooling cooperation-removal multiple pollutant in a kind of tower
CN109331639A (en) * 2018-11-30 2019-02-15 北京兴晟科技有限公司 A kind of flue gas desulfurization device with slurries filtering function
CN109364733A (en) * 2018-12-07 2019-02-22 山东金太阳设备制造有限公司 A kind of board-like slurries cooler
CN110152460A (en) * 2019-06-14 2019-08-23 杭州蕴泽环境科技有限公司 It is a kind of to utilize the water-saving eliminating white smoke device and method of chimney sleeve
CN110152460B (en) * 2019-06-14 2024-04-09 杭州蕴泽环境科技有限公司 Water-saving white smoke eliminating device and method by using chimney sleeve

Similar Documents

Publication Publication Date Title
CN108031271A (en) A kind of flue gas desulfurization device
CN206121503U (en) Liquid cooling of wet desulphurization tower entoplasm is high -efficient flue gas processing system but
CN205379793U (en) Smoke desulfurizing dust collector
CN108465368A (en) Desulfurization and dedusting disappears white device for deep cleaning
CN207641242U (en) A kind of wet flue gas flue heat exchange eliminating white smoke and condensate water recovery device
CN108970370A (en) It is a kind of low cost flue gas device for deep cleaning and its purification receive water eliminating white smoke technique
CN108554157A (en) A kind of single column washing Wet fume sweetening dust remover of no stock tank secondary cycle
CN107519757A (en) A kind of unpowered cooling cigarette tower apparatus of wet flue gas
CN106861354A (en) A kind of condensation method water saving wet desulfurizer
CN207478303U (en) A kind of system for eliminating the coloured plume of industrial smoke
CN109107328A (en) It solves desulfurization fume and takes off white method and desulphurization system
CN208927905U (en) A kind of low cost flue gas device for deep cleaning
CN109432969A (en) A kind of three-circulation desulphurization disappears white integrated apparatus
CN207871901U (en) A kind of flue gas desulfurization device
CN107684817A (en) A kind of flue gas desulfurization process system
CN206897161U (en) A kind of flue gas waste heat recovery system and a kind of high-efficiency desulfurization Tower System
CN211367032U (en) Steam wet type self-condensation device for desulfurization wastewater zero-discharge system
CN208742284U (en) A kind of single column washing Wet fume sweetening dust remover of no stock tank secondary cycle
CN208049672U (en) Plume takes off white system
CN207871875U (en) A kind of desulfurating dust removing device for flue gas
CN207042170U (en) Condensation method water saving wet desulfurizer
CN103463965B (en) A kind of low-temperature circulating fluid bed flue gas desulfurization cleaner
CN108579316A (en) A kind of flue gas for wet desulfuration tower disappears white plumage governing system
CN210773529U (en) Spray tower, exhaust system and boiler system
CN108671737A (en) Flue gas processing device and wet desulfurization system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination