CN107543194A - Deep condensation dust removal mist residual neat recovering system - Google Patents
Deep condensation dust removal mist residual neat recovering system Download PDFInfo
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- CN107543194A CN107543194A CN201710974771.4A CN201710974771A CN107543194A CN 107543194 A CN107543194 A CN 107543194A CN 201710974771 A CN201710974771 A CN 201710974771A CN 107543194 A CN107543194 A CN 107543194A
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- water
- heat exchanger
- dust removal
- residual neat
- neat recovering
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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Abstract
The invention provides a kind of deep condensation dust removal mist residual neat recovering system, including boiler, desulfurizing tower and condensing heat exchanger, boiler connects with desulfurizing tower, desulfurizing tower is connected by flue with deep condensation formula heat exchanger, cigarette vapour is provided with flue and enters porthole, condensing heat exchanger is connected by mixing liquid drain pipe with desulfurizing tower, and cigarette vapour liquid packing is provided with mixing liquid drain pipe.The beneficial effects of the invention are as follows：White smoke more than 90% can be eliminated using deep condensation technology；Trickle gel is greatly reduced, converts fume amount≤5mg/Nm3.Wet electric cleaner can be replaced, investment is reduced, saves substantial amounts of electric energy；Waste heat recovery can be carried out, energy-saving effect is notable；The condensed water in cigarette vapour is reclaimed, reduces rate of water make-up；Condensing heat exchanger and First air heater are bypass arrangement, small on original production process influence, and securely and reliably, flexibility is big；Recirculated water and condensing water conduit system laying reduced investment, floor space be few, construction is simple.
Description
Technical field
The invention belongs to industrial technical field, more particularly to a kind of deep condensation dust removal mist residual neat recovering system.
Background technology
Coal-fired plant flue gas is discharged into air through chimney, forms white steam, plume.Most of flue gas desulfurization in China uses
Wet desulfurizing process, especially limestone-gypsum method technique.This technique can make cigarette temperature be reduced to 50 DEG C or so, and these are low
Have enough to eat and wear and wet flue gas, directly enter atmospheric environment through chimney, condense into fine droplet to the cold, produce " white plume ", be commonly called as " big
White cigarette ", " Bai Long ".
Although simple white plume does not influence directly on environmental quality, surrounding resident can be lived and cause to be stranded
Disturb.Environmental Protection Agency also often by similar complaint, therefore many enterprises for being equipped with wet flue gas desulfurizer, eliminating " in vain
One of important content that color plume " is transformed as minimum discharge.State Power Environmental Protection Research Institute has investigated national thermal power plant 95,
It is related to 235 units, in 122 chimneys of all investigations, there are 107 wet plume occur, account for 88%.95 power plant have 17
Power plant is complained by nearby residents, and only 2 local governments of power plant claim.
During wet desulphurization, desulfurization slurry contacts with high-temperature flue gas, one side moisture evaporation, and increase flue gas is containing wet
Amount, on the other hand, flue-gas temperature reduce, and the ability that flue gas carries vapor reduces.After flue gas reaches saturation state, portion can be carried
Divide droplet.The saturation wet flue gas for carrying droplet is discharged into air after demister removes partial drop, due to environment temperature
It is lower than flue-gas temperature, hydrogenesis droplet, the white plume of formation in saturation wet flue gas.Environment temperature is lower, ambient humidity
Bigger, white plume is longer.
" white plume " is easily formed using the coal unit chimney breast of wet desulfurizing process in the prior art, directly added
Although hot method can eliminate " white plume ", the operation energy consumption of unit can be increased.
Therefore, this area needs a kind of new deep condensation dust removal mist residual neat recovering system to solve the above problems.
The content of the invention
In order to solve the above-mentioned technical problem, the invention provides a kind of deep condensation dust removal mist residual neat recovering system, including：
Boiler, desulfurizing tower and condensing heat exchanger, the boiler connect with the desulfurizing tower, and the desulfurizing tower passes through flue and the depth
Condensing heat exchanger connection is spent, being provided with cigarette vapour on the flue enters porthole, and the condensing heat exchanger is dredged by mixing liquid
Water pipe is connected with the desulfurizing tower, and cigarette vapour liquid packing is provided with the mixing liquid drain pipe, and the flue is straight by cigarette vapour
Open gate connects with chimney, and the condensing heat exchanger goes out porthole by cigarette vapour and connected with chimney；More than the deep condensation dust removal mist
Heat recovery system also includes：Primary air intake pipe, First air lead directly to door, First air shutter, First air and go out air door and First air
Heater, the primary air intake pipe are connected by the First air shutter with the First air heater, the First air
Blast pipe leads directly to door by the First air and connected with the boiler, and the First air heater goes out air door by the First air
Being connected with the boiler, the condensing heat exchanger is connected by recirculated water return pipe with the First air heater, and described one
Secondary wind heater is connected by recirculated water feed pipe with the condensing heat exchanger, and circulation is provided with the recirculated water feed pipe
Water pump.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, more than the deep condensation dust removal mist
Heat recovery system also includes：Industry water main pipe, industry water intake gate, industry water go out water valve and industry water leads directly to door, the condensation
Formula heat exchanger goes out water valve with the industry water and connected, and the industry water goes out water valve and connected with the straight-through door of the industry water, the work
Industry water leads directly to door and connected with the industry water intake gate, and the industry water intake gate connects with the condensing heat exchanger, described
The water side of industry water main pipe is connected to the industry water and led directly to after door and the industry water intake gate.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, more than the deep condensation dust removal mist
Heat recovery system also includes：Condensation water heater, condensate pump and condenser, the condensation water heater connect with the boiler
Logical, the condensation water heater is connected by the condensate pump with the condenser, and the condenser is connected to the industry
Water goes out water valve and the industry water is led directly to after door.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, more than the deep condensation dust removal mist
Heat recovery system also includes：Steam turbine, the steam turbine connect with the condensation water heater, and the steam turbine with it is described
Condenser connects.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, more than the deep condensation dust removal mist
Heat recovery system also includes：Generator, the generator connect with the steam turbine, and the generator and the condensing
Heat exchanger connects.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, the condensing heat exchanger includes
Cool side and condensation side.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, the flue and the cooling side
Connection.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, the recirculated water feed pipe and institute
Recirculated water return pipe is stated to connect with the cooling side.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, the industry water intake gate and institute
State industry water and go out water valve and connected with the condensation side.
In the optimal technical scheme of above-mentioned deep condensation dust removal mist residual neat recovering system, the cigarette vapour go out porthole with it is described
Condensation side connects.
The beneficial effects of the invention are as follows：
1st, white smoke more than 90% can be eliminated using deep condensation technology.
2nd, trickle gel can be substantially reduced while white smoke is eliminated, converts fume amount≤5mg/Nm3.
3rd, wet electric cleaner can be replaced, investment is reduced, saves substantial amounts of electric energy.
4th, waste heat recovery can be carried out during deep condensation, energy-saving effect is notable.
5th, the condensed water in cigarette vapour is reclaimed, reduces rate of water make-up.
6th, condensing heat exchanger and First air heater are bypass arrangement, small on original production process influence, securely and reliably,
Flexibility is big.
7th, recirculated water and condensing water conduit system laying reduced investment, floor space be few, construction is simple.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
There is the required accompanying drawing used in technology description to be briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, can be with
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is the structural representation of the deep condensation dust removal mist residual neat recovering system of the present invention；
In figure：1st, boiler；2nd, desulfurizing tower；3rd, flue；4th, cigarette vapour enters porthole；5th, condensing heat exchanger；6th, recirculated water water outlet
Room；7th, upper tank dividing plate；8th, industry water intake chamber；9th, cigarette vapour leads directly to door；10th, chimney；11st, cigarette vapour goes out porthole；12nd, condensing heat-exchange
Pipe；13rd, cigarette vapour dividing plate；14th, cigarette vapour cooling heat exchanger tube；15th, industry water water-supplying chamber；16th, recirculated water intake chamber；17th, cigarette carbonated drink is sealed
Device；18th, mixing liquid drain pipe；19th, generator；20th, steam turbine；21st, industry water intake gate；22nd, industry water goes out water valve；23、
Industry water leads directly to door；24th, industry water main pipe；25th, condenser；26th, condensate pump；27th, condensation water heater；28th, First air is straight
Open gate；29th, primary air intake pipe；30th, First air shutter；31st, First air heater；32nd, First air goes out air door；33rd, circulate
Water pump；34th, recirculated water feed pipe；35th, recirculated water return pipe.
Embodiment
To make the object, technical solutions and advantages of the present invention clearer, technical scheme will be carried out below
Detailed description.Obviously, described embodiment is only part of the embodiment of the present invention, rather than whole embodiments.Base
Embodiment in the present invention, those of ordinary skill in the art are resulting on the premise of creative work is not made to be owned
Other embodiment, belong to the scope that the present invention is protected.
It should be noted that in the description of the invention, term " " center ", " on ", " under ", "left", "right", " vertical ",
The direction of instruction such as " level ", " interior ", " outer " or the term of position relationship are to be based on direction shown in the drawings or position relationship, this
Description is intended merely to facilitate, rather than instruction or hint described device or element there must be specific orientation, with specific
Azimuth configuration and operation, therefore be not considered as limiting the invention.In addition, term " first ", " second ", " the 3rd " are only used
In description purpose, and it is not intended that instruction or hint relative importance.
In addition it is also necessary to explanation, in the description of the invention, unless otherwise clearly defined and limited, term " peace
Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or integratedly
Connection；Can be mechanical connection or electrical connection；Can be joined directly together, can also be indirectly connected by intermediary,
It can be the connection of two element internals.To those skilled in the art, it can understand that above-mentioned term exists as the case may be
Concrete meaning in the present invention.
As shown in figure 1, the invention provides a kind of deep condensation dust removal mist residual neat recovering system, including：Boiler 1, desulfurization
Tower 2 and condensing heat exchanger 5, the boiler 1 connect with the desulfurizing tower 2, and the desulfurizing tower 2 passes through flue 3 and the depth
Condensing heat exchanger 5 is connected, and cigarette vapour is provided with the flue 3 and enters porthole 4, the condensing heat exchanger 5 passes through mixing liquid
Drain pipe 18 is connected with the desulfurizing tower 2, and cigarette vapour liquid packing 17, the flue 3 are provided with the mixing liquid drain pipe 18
Door 9 is led directly to by cigarette vapour to connect with chimney 10, the condensing heat exchanger 5 goes out porthole 11 by cigarette vapour and connected with chimney 10；Institute
Stating deep condensation dust removal mist residual neat recovering system also includes：Primary air intake pipe 29, First air lead directly to door 28, First air shutter
30th, First air goes out air door 32 and First air heater 31, the primary air intake pipe 29 by the First air shutter 30 with
The First air heater 31 connects, and the primary air intake pipe 29 leads directly to door 28 by the First air and connected with the boiler 1
Logical, the First air heater 31 goes out air door 32 by the First air and connected with the boiler 1, the condensing heat exchanger 5
Pass through recirculated water return pipe.35 are connected with the First air heater 31, and the First air heater 31 is supplied water by recirculated water
Pipe 34 is connected with the condensing heat exchanger 5, and water circulating pump 33 is provided with the recirculated water feed pipe 34.
Preferably, the deep condensation dust removal mist residual neat recovering system also includes：Industry water main pipe 24, industry water intake gate
21st, industry water goes out water valve 22 and industry water leads directly to door 23, and the condensing heat exchanger 5 goes out water valve 22 with the industry water and connected,
The industry water goes out water valve 22 and connected with the straight-through door 23 of the industry water, and the industry water leads directly to door 23 and intake with the industry water
Door 21 connects, and the industry water intake gate 21 connects with the condensing heat exchanger 5, and the water side of the industry water main pipe 24 connects
The industry water is connected on to lead directly to after door 23 and the industry water intake gate 21.
Preferably, the deep condensation dust removal mist residual neat recovering system also includes：Condensation water heater 27, condensate pump 26
With condenser 25, the condensation water heater 27 connects with the boiler 1, and the condensation water heater 27 passes through the condensate
Pump 26 connects with the condenser 25, and the condenser 25 is connected to the industry water and goes out water valve 22 and the straight-through door of the industry water
After 23.
Preferably, the deep condensation dust removal mist residual neat recovering system also includes：Steam turbine 20, the steam turbine 20 and institute
State condensation water heater 27 to connect, and the steam turbine 20 connects with the condenser 25.
Preferably, the deep condensation dust removal mist residual neat recovering system also includes：Generator 19, the generator 19 and institute
State steam turbine 20 to connect, and the generator 19 connects with the condensing heat exchanger 5.
Preferably, the condensing heat exchanger 5 includes cooling side and condensation side, wherein, the left side of condensing heat exchanger 5 is
Cool side, and right side is condensation side.
Preferably, the flue 3 connects with the cooling side.
Preferably, the recirculated water feed pipe 34 and the recirculated water return pipe.35 connect with the cooling side.
Preferably, the industry water intake gate 21 and the industry water go out water valve 22 and connected with the condensation side.
Preferably, the cigarette vapour goes out porthole 11 and connected with the condensation side.
The present invention is divided the carbonated drink in cigarette vapour using condensing heat-exchange technology according to hydrodynamics, thermodynamics, heat transfer principle
The cohesion of son group, increase, depart from, landing, under the water vapour in cigarette vapour and the gel of carrying are separated before smoke stack emission
Come, primary structure is made up of two parts：
Deep condensation formula heat exchanger section, mainly gone out by deep condensation formula heat exchanger 5, recirculated water intake chamber 16, recirculated water
Hydroecium 6, upper tank dividing plate 7, lower header dividing plate 36, industry water enter room 8, water-supplying chamber 15, deep condensation heat exchanger tube 12, cigarette vapour dividing plate
13rd, flue gas cool-down heat exchanger tube 14, cigarette vapour enter porthole 4, cigarette vapour goes out porthole 11, cigarette vapour leads directly to door 9, flue gas liquid packing 17, mixed liquor
Body drain pipe 18, industry water intake gate 12, industry water go out water valve 22, industry water leads directly to door 23, circulating water inlet 34, recirculated water
The grade of outlet pipe 35 forms.
First air heater section, main once wind heater 31, First air shutter 30, First air go out air door 32,
First air leads directly to the composition such as door 28, water circulating pump 33, circulating water inlet 35, circulating water outlet pipe 34.
The operation principle of the present invention is as follows：
1st, temperature is that the cigarette vapour after 50 DEG C or so desulfurization enters porthole 4 into the heat exchange of deep condensation formula by flue 3 by cigarette vapour
The cooling side of device 5, cooling side of the cigarette vapour in housing 37 are carried out countercurrently efficient by heat exchanger tube 14 with the recirculated water in heat exchanger tube
Heat exchange, the cigarette vapour after preliminary cooling enter deep condensation side under the water conservancy diversion of dividing plate 13, enter to advance with the industry water of lower temperature
The heat exchange of one step, deep condensation into liquid, during deep condensation saturated steam with the gel and PM2.5 that carry and with
Under molecule be condensed into mixing liquid together, desulfurizing tower bottom is drained into by 17 blended liquid hydrophobic pipe 18 of cigarette vapour liquid packing
In the storage stock tank in portion；Clean flue gas after deep condensation is discharged into air through chimney 10.
2nd, recirculated water beaten through water circulating pump 33 to the recirculated water intake chamber 16 of deep condensation heat exchanger, by heat exchanger tube 14 with
Cigarette vapour outside heat exchanger tube carries out adverse current high efficient heat exchanging, makes the reduction of cigarette stripping temperature, circulating water temperature rise, then by water-supplying chamber 6, follow
Ring water return pipe 35, which enters, heats cold wind in First air heater 31, after a cold wind absorption cycle hydro-thermal amount, circulating water temperature
Reduce and carry out heat exchange absorption heat rise temperature through the driving depth condensing heat exchanger 5 of water circulating pump 23 again, circulated with this past
It is multiple, complete heat absorption, the waste heat recovery process of heat release；First air is heated.
3rd, entered by industry water main pipe 24 through industry water intake gate 21 in the deep condensation side intake chamber 8 of condensing heat exchanger 5,
Heat exchange is further carried out through deep condensation heat exchanger tube 12 and cigarette vapour again, the industry water of lower temperature steams the saturation water in cigarette vapour
For the gel such as vapour and PM2.5 fine particles deep condensation into mixing liquid, industry water absorbs thermal temperature rise again through industry
Water water-supplying chamber 15, industry water go out water valve 22 and enter condenser 25 by condensate main pipe 24.
The foregoing is only a specific embodiment of the invention, but protection scope of the present invention is not limited thereto, any
Those familiar with the art the invention discloses technical scope in, change or replacement can be readily occurred in, should all be contained
Cover within protection scope of the present invention.Therefore, protection scope of the present invention should be based on the protection scope of the described claims.
Claims (10)
- A kind of 1. deep condensation dust removal mist residual neat recovering system, it is characterised in that the deep condensation dust removal mist waste heat recovery system System includes：Boiler, desulfurizing tower and condensing heat exchanger, the boiler connect with the desulfurizing tower, and the desulfurizing tower passes through flue Connected with the deep condensation formula heat exchanger, cigarette vapour is provided with the flue and enters porthole, the condensing heat exchanger passes through mixed Close liquid hydrophobic pipe to connect with the desulfurizing tower, cigarette vapour liquid packing is provided with the mixing liquid drain pipe, the flue leads to Cross the straight-through door of cigarette vapour to connect with chimney, the condensing heat exchanger goes out porthole by cigarette vapour and connected with chimney；The deep condensation dust removal mist residual neat recovering system also includes：Primary air intake pipe, First air lead directly to door, First air air intake Door, First air go out air door and First air heater, the primary air intake pipe by the First air shutter with it is described once Wind heater connects, and the primary air intake pipe leads directly to door by the First air and connected with the boiler, and the First air adds Hot device goes out air door by the First air and connected with the boiler, the condensing heat exchanger by recirculated water return pipe with it is described First air heater is connected, and the First air heater is connected by recirculated water feed pipe with the condensing heat exchanger, described Water circulating pump is provided with recirculated water feed pipe.
- 2. deep condensation dust removal mist residual neat recovering system according to claim 1, it is characterised in that the deep condensation removes Cloud residual neat recovering system also includes：Industry water main pipe, industry water intake gate, industry water go out water valve and industry water leads directly to door, institute To state condensing heat exchanger and go out water valve with the industry water and connect, the industry water, which goes out water valve and leads directly to door with the industry water, to be connected, The industry water leads directly to door and connected with the industry water intake gate, and the industry water intake gate connects with the condensing heat exchanger Logical, the water side of the industry water main pipe is connected to the industry water and led directly to after door and the industry water intake gate.
- 3. deep condensation dust removal mist residual neat recovering system according to claim 2, it is characterised in that the deep condensation removes Cloud residual neat recovering system also includes：Condensation water heater, condensate pump and condenser, the condensation water heater and the pot Stove is connected, and the condensation water heater is connected by the condensate pump with the condenser, and the condenser is connected to described Industry water goes out water valve and the industry water is led directly to after door.
- 4. deep condensation dust removal mist residual neat recovering system according to claim 3, it is characterised in that the deep condensation removes Cloud residual neat recovering system also includes：Steam turbine, the steam turbine connect with the condensation water heater, and the steam turbine Connected with the condenser.
- 5. deep condensation dust removal mist residual neat recovering system according to claim 4, it is characterised in that the deep condensation removes Cloud residual neat recovering system also includes：Generator, the generator connect with the steam turbine, and the generator with it is described Condensing heat exchanger connects.
- 6. deep condensation dust removal mist residual neat recovering system according to claim 5, it is characterised in that the condensing heat exchange Device includes cooling side and condensation side.
- 7. deep condensation dust removal mist residual neat recovering system according to claim 6, it is characterised in that the flue with it is described Cool side connection.
- 8. deep condensation dust removal mist residual neat recovering system according to claim 7, it is characterised in that the recirculated water supplies water Pipe and the recirculated water return pipe connect with the cooling side.
- 9. deep condensation dust removal mist residual neat recovering system according to claim 8, it is characterised in that the industry water water inlet Door and the industry water go out water valve and connected with the condensation side.
- 10. deep condensation dust removal mist residual neat recovering system according to claim 9, it is characterised in that the cigarette vapour goes out vapour Door connects with the condensation side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710974771.4A CN107543194B (en) | 2017-10-19 | 2017-10-19 | Deep condensation dust removal mist residual neat recovering system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710974771.4A CN107543194B (en) | 2017-10-19 | 2017-10-19 | Deep condensation dust removal mist residual neat recovering system |
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| Publication Number | Publication Date |
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| CN107543194A true CN107543194A (en) | 2018-01-05 |
| CN107543194B CN107543194B (en) | 2018-06-22 |
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ID=60968166
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| Application Number | Title | Priority Date | Filing Date |
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| CN201710974771.4A Active CN107543194B (en) | 2017-10-19 | 2017-10-19 | Deep condensation dust removal mist residual neat recovering system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111389171A (en) * | 2020-04-26 | 2020-07-10 | 中国电力工程顾问集团西北电力设计院有限公司 | White smoke plume elimination and water recycling system and process for thermal power plant |
| CN113804013A (en) * | 2021-10-15 | 2021-12-17 | 西安热工研究院有限公司 | A recovery system that continuously discharges fluid into a surface condenser |
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| EP2431579A2 (en) * | 2010-09-21 | 2012-03-21 | Hitachi Ltd. | Multipurpose thermal power plant system |
| JP2013204972A (en) * | 2012-03-29 | 2013-10-07 | Hitachi Zosen Corp | Waste treatment facility |
| CN103528044A (en) * | 2013-09-28 | 2014-01-22 | 昆山市周市溴化锂溶液厂 | Heat recovery system of smoke exhaust gas desulfurization device |
| CN203489246U (en) * | 2013-06-13 | 2014-03-19 | 烟台龙源电力技术股份有限公司 | Boiler smoke waste-heat application system |
| CN206478668U (en) * | 2017-01-24 | 2017-09-08 | 中国电力工程顾问集团华北电力设计院有限公司 | Eliminate the device of the white plume of chimney |
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2017
- 2017-10-19 CN CN201710974771.4A patent/CN107543194B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2431579A2 (en) * | 2010-09-21 | 2012-03-21 | Hitachi Ltd. | Multipurpose thermal power plant system |
| JP2013204972A (en) * | 2012-03-29 | 2013-10-07 | Hitachi Zosen Corp | Waste treatment facility |
| CN203489246U (en) * | 2013-06-13 | 2014-03-19 | 烟台龙源电力技术股份有限公司 | Boiler smoke waste-heat application system |
| CN103528044A (en) * | 2013-09-28 | 2014-01-22 | 昆山市周市溴化锂溶液厂 | Heat recovery system of smoke exhaust gas desulfurization device |
| CN206478668U (en) * | 2017-01-24 | 2017-09-08 | 中国电力工程顾问集团华北电力设计院有限公司 | Eliminate the device of the white plume of chimney |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111389171A (en) * | 2020-04-26 | 2020-07-10 | 中国电力工程顾问集团西北电力设计院有限公司 | White smoke plume elimination and water recycling system and process for thermal power plant |
| CN113804013A (en) * | 2021-10-15 | 2021-12-17 | 西安热工研究院有限公司 | A recovery system that continuously discharges fluid into a surface condenser |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107543194B (en) | 2018-06-22 |
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