CN107697967A - A kind of Desulphurization for Coal-fired Power Plant wastewater zero discharge system and method - Google Patents
A kind of Desulphurization for Coal-fired Power Plant wastewater zero discharge system and method Download PDFInfo
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- CN107697967A CN107697967A CN201710942060.9A CN201710942060A CN107697967A CN 107697967 A CN107697967 A CN 107697967A CN 201710942060 A CN201710942060 A CN 201710942060A CN 107697967 A CN107697967 A CN 107697967A
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- desulphurization
- power plant
- spray drying
- coal
- drying tower
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/10—Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
- C02F1/12—Spray evaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/501—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
- B01D53/505—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound in a spray drying process
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents
Abstract
The invention discloses a kind of Desulphurization for Coal-fired Power Plant zero emission method of wastewater, after caused waste water after wet desulphurization is simply pre-processed by three header technologies, adds a small amount of Ca (OH)2Pass through the rotary atomizer of spray drying tower after slurries are well mixed, the mist drop for being atomized into 10 ~ 60mm of average grain diameter is sprayed into drying tower, the high-temperature flue gas of boiler is used as thermal source before by the use of air preheater, waste water is evaporated in spray drying tower, moisture enters in flue gas, salt in waste water is collected after drying, reach the purpose of desulfurization wastewater zero-emission, present invention is primarily intended to be evaporated the waste water directly discharged after original desulfurization, collect, waste water treatment is added after desulfurization, small-sized pre- dust-removing process, really realize zero-emission, quality of fly ash after electric cleaner dedusting is high, it is easy to recycle；And cost is low, efficiency high, it is easy to promote.
Description
Technical field
The present invention relates to Desulphurization for Coal-fired Power Plant field of waste water treatment, and in particular to one kind is applied to Desulphurization for Coal-fired Power Plant waste water
Zero discharging system and method.
Background technology
Coal-burning power plant is the rich and influential family of China's industrial water, and its water consumption and displacement are very huge, about 40% in industrial water
For coal-burning power plant, the annual discharge capacity in coal-burning power plant accounts for the 10% of national industrial enterprise's discharge capacity.Coal-burning power plant is given up in China
The research of water harnessing is started late, but with environmental protection relevant law and supervises more and more stricter, coal-burning power plant's waste water " zero-emission
Put " it is mentioned more and more.
Promulgate within 2006《Waste Water From Fire Power Plant Treatment design technical regulation》Explicitly point out, the desulfurization wastewater of thermal power plant
Treatment facility will be separately provided, and paid the utmost attention to treatment for reuse, do not set floss hole, it is necessary to realize waste water zero emission.In April, 2015
Issue《Water pollution action plan》Pointing out, country will strengthen the management of all kinds of water pollutions, control pollutant emission comprehensively,
Desulphurization for Coal-fired Power Plant waste water causes industry to be paid close attention to because of complicated component, containing heavy metal.What in November, 2016 put into effect《Control pollutant
Discharge permit embodiment》Even more take the lead in pointing out to thermoelectricity, paper industry enterprise core hair pollutant discharging license.Same month, State Council
Issue《" 13 " ecological environmental protection is planned》, it is indicated that pollutant should be greatly reduced in the highly water intensive industry such as electric power, papermaking, printing and dyeing
Intensity is discharged, reaches advanced norm standard.On January 11st, 2017, Chinese Ministry of Environmental Protection prints and distributes again《Thermal power plant's pollution prevention technique political affairs
Plan》.
In recent years the environmental protection policy of the intensive issue of government department shows that the Party Central Committee, State Council pay much attention to ecological environmental protection
Work, pressure of the thermal power plant as water consumption rich and influential family in terms of Water Resources Restriction with discharge limitation suddenly rise, accelerate to implement
Depth is economized on water and effluent sewage " zero-emission " turns into inevitable choice.With the continuous progress of green technology and the leather of environmental protection concept
Newly, some coal-burning power plants being on the forefront start to be laid out in advance, made rational planning for, and do not stint and substantial contribution is put into environmental protection.But i.e.
Just in this way, the domestic coal-burning power plant for really realizing waste water zero emission is still very few at present.
Study carefully its cause, on the one hand, due to the difficulty in treatment of coal-burning power plant's waste water zero emission --- desulfurization waste water quality has
Have turbidity is big, hardness is high, content of beary metal is high, chloride ion content superelevation, easy fouling, it is perishable the features such as, intractability is big；Separately
On the one hand, the existing desulfurization wastewater Treatment process generally used, the performance in reliability, economy are unsatisfactory on the market.Example
Though such as three header technology techniques of most of power plants' uses are simple before this, investment cost is relatively low, full factory's waste water " zero can not be met
The environmental requirement of discharge ".
Currently, domestic thermal power plant desulfurization wastewater " zero-emission " technology is summed up still in research and development and Preliminary Applications stage
Mainly there are two process routes：One is the process route for being realized in a manner of water process " zero-emission ", i.e. " pretreatment softening+film
Concentrate decrement+evaporative crystallization " technology.The technology is more ripe, stable, has part successful operation case and not to power plant
Generating production has any impact, but its investment and operating cost are too high, and more solid waste is also easy to produce in processing procedure, this
Containing toxic components such as chlorion, sulfate radicals in a little solid waste, separating treatment again is also needed to before being recycled after reclaiming,
Increase cost, cause the unmanned recovery of the solid waste after present coal-burning power plant's exhaust-gas treatment, reduce the performance of enterprises；Another is
The process route of " zero-emission " is realized in a manner of fume afterheat, i.e. " pretreatment+flue spray drying " technology.Its advantage is investment
It is relatively low with operating cost, but technology also unshaped, waste water evaporation is incomplete, easily causes corrosion and dust stratification to block to flue, at present
Impacted there has been no successful operation case and to power plants generating electricity production.
The content of the invention
To solve the above problems, the invention discloses a kind of Desulphurization for Coal-fired Power Plant wastewater zero discharge system and method, its work
Skill composition is simple, and engineering reliability is high, and once input and operating cost are relatively low, and the solid waste after processing is up to standard, carries
High economic benefit.
To reach above-mentioned purpose, the present invention provides a kind of Desulphurization for Coal-fired Power Plant zero emission method of wastewater, it is characterised in that：It is wet
After caused waste water is by three header technologies simply pretreatment after method desulfurization, a small amount of Ca (OH) is added2Lead to after slurries are well mixed
The rotary atomizer of spray drying tower is crossed, the mist drop for being atomized into 10 ~ 60mm of average grain diameter is sprayed into drying tower, utilizes air preheater
The high-temperature flue gas of preceding boiler（350 DEG C or so）As thermal source, waste water is evaporated in spray drying tower, moisture enters in flue gas,
Salt in waste water is collected after drying, and reaches the purpose of desulfurization wastewater zero-emission.
Preferably, the method suitable for Desulphurization for Coal-fired Power Plant wastewater zero discharge also includes step：Simultaneously from air preheater
Low-temperature flue gas in a part is drawn afterwards（120 DEG C or so）, it is laggard by introducing the mixing of high-temperature flue gas flue after Smoke-heating device
Enter spray drying tower.When power plant's operating load reduces, extraction flue gas has a great influence to power plant's coal consumption etc. directly before air preheater,
By being supplemented in high-temperature flue gas after low-temperature flue gas in being introduced into suitably heating, while the extraction of high-temperature flue gas is reduced, so as to reduce pair
The influence of boiler of power plant efficiency.
Preferably, the method suitable for Desulphurization for Coal-fired Power Plant wastewater zero discharge also includes step：In spray drying tower
With installing small-sized pre-duster device additional between power plant original electric cleaner, to collect the things such as the salt after spray drying in flue gas
Matter, the material of collection is delivered to waste residue disposal plant together with the material of spray drying tower bottom collection, collectively as dangerous waste list
Stay alone reason, the flyash after electric cleaner processing undopes harmful ion, can directly recycle, improve business economic effect
Benefit.
Preferably, before spray drying tower processing desulfurization wastewater, first with process water instead of using, after system is normal,
Desulfurization wastewater is cut again, before spray drying tower is stopped transport, also with technique water running for a period of time, cleans high speed atomisation device, while clearly
Sulphur waste pipe and pump etc. are eluted, avoids the corrosion of equipment.
Preferably, the desulfurization wastewater after pretreatment, adds a small amount of Ca (OH)2After slurries are quenched, pipeline is extremely
Waste water tank in desulfurization wastewater treatment system, then high-order feed box is delivered to, gravity flow enters spray drying tower, wherein Ca (OH)2
Concentration of slurry is 5% ~ 25%.
Preferably, to avoid corroding, the conveyance conduit that desulfurization wastewater flows through uses Glass Flake Substrate anti-corrosion, glass flake
2.0 ~ 3.5mm of thickness；In spray drying tower oncus anti-corrosion, using Glass Flake Substrate, additional glass-fiber-fabric strengthens, glass squama
Piece 1.5 ~ 3.0mm of thickness, 1 ~ 2 layer of glass-fiber-fabric, thickness is in 0.2 ~ 0.6mm.
Present invention also offers a kind of Desulphurization for Coal-fired Power Plant wastewater zero discharge system, boiler be sequentially connected Benitration reactor,
Air preheater, electric cleaner, wet desulphurization device, chimney；The delivery port of the wet desulphurization device passes through three header devices, waste water
Case, high-order feed box connection spray drying tower, waste water tank are connected with slurry tank, are provided between the Benitration reactor and air preheater
Branch pipe one connects spray drying tower, and branch pipe two is provided between air preheater and electric cleaner and connects spray drying tower, is set on branch pipe two
There is Smoke-heating device, pre-duster is provided between spray drying tower and electric cleaner, Solid state fermentation is provided with below pre-duster
Device.
Preferably, three header devices include neutralizing case, reaction chamber and flocculation tanks.
Preferably, spray drying tower upper end is disposed with nucleus equipment rotary atomizer.
Preferably, spray drying tower inlet and outlet flue sets inlet baffle and outlet damper, inlet baffle to use adjustment type
Structure is performed, the exhaust gas volumn of the system is entered according to spray drying system exhaust pass temperature adjustment, outlet damper is using switch
Type performs structure.
Preferably, the operating temperature of the spray drying tower is always more than acid dew-point temperature, tower body and flue etc. and cigarette
The material of gas medium contact uses ordinary carbon steel, and the atomizer contacted with desulfurization wastewater uses Hastelloy material.
Preferably, the straight-through end of the spray drying tower uses stainless steel, and cone, which gathers dust to hold, uses carbon steel, spray drying tower sheet
External wall is incubated using heat-preservation cotton rock.
Preferably, the high-order feed box Joining Technology water tank.
Preferably, blower fan is provided between the electric cleaner and wet desulphurization device.
Preferably, waste water delivery pump is provided between the waste water tank and high-order feed box.
Preferably, the Smoke-heating device is provided with control valve.
In summary, the system and method suitable for Desulphurization for Coal-fired Power Plant wastewater zero discharge of the invention can be realized following
Beneficial effect：
（1）The present invention can really realize desulfurization wastewater zero-emission, and waste water is evaporated by heat smoke and collected, cigarette after waste water evaporation
Moisture increases in gas, and particulate matter ratio resistance reduces in flue gas, carrying capacity increase, so as to improve power plant's original deduster dedusting effect
Rate；Supplement the moisture in flue gas indirectly simultaneously, reduce the water consumption and waste water yield of subsequent wet desulfurizer, realize benign
Circulation；
（2）The present invention takes middle low-temperature flue gas heat make-up thermal source, avoids the high warm flue gas before single extraction air preheater to pot
The influence of the efficiency of furnace, the normal production and operation of power plant are not influenceed, so as to be easier to be received by power plant；
（3）Present invention process flow is simple, relatively low using former flue gas heat energy consumption, compared with traditional " evaporative crystallization " technology, compared with
Its disposable input and operating cost can reduce by more than 50%, alleviate coal-burning power plant's operated pressure significantly, reduce social emission reduction into
This, economy is obvious；
（4）The present invention is separately provided small-sized pre-dedusting device after spray drying, to collect having in flue gas after spray drying
Evil salts substances, the dedusting pressure of former electric cleaner is reduced, avoids the influence to former electric cleaner quality of fly ash, improves power plant
Business income；
（5）By the lime white added in waste water, accelerate rate of drying, can be with the SO in cooperation-removal flue gas2、SO3, carry
High efficiency.
Brief description of the drawings
Fig. 1 is the structural representation of patent working of the present invention.
Reference numerals list：
1st, boiler, 2, Benitration reactor, 3, air preheater, 4, spray drying tower, 5, Smoke-heating device, 6, control valve, 7, pre-
Deduster, 8, Solid state fermentation device, 9, electric cleaner, 10, blower fan, 11, wet desulphurization device, 12, chimney, 13, three headers dress
Put, 14, waste water tank, 15, slurry tank；16th, waste water delivery pump；17th, high-order feed box, 18, technique water tank, 19, branch pipe one, 20,
Branch pipe two.
Embodiment
The present invention is described in further detail with reference to the accompanying drawings and examples, as shown in figure 1, its concrete technology is such as
Under：
（1）Desulfurization wastewater is pre-processed using three header devices 13, pre-processing the step of specifically including has：It is de- to neutralize regulation
The pH value of sulphur waste water obtains alkaline desulfurization wastewater；The compound in alkaline desulfurization wastewater is precipitated in solid form, and obtain
Layer clear liquid；Supernatant liquor is reacted with medicament, and make the suspension and sediment flocculation sediment generated after reaction；
（2）Waste water enters waste water tank 14 after desulfurization wastewater pretreatment, in Ca (OH) of the internal modulation concentration of slurry tank 15 5% ~ 25%2
Slurries, by Ca (OH)2Slurries are sufficiently mixed with desulfurization wastewater；
（3）Desulfurization wastewater after being sufficiently mixed is delivered to high-order feed box 17 again, and gravity flow enters spray drying tower 4, passes through spraying
The rotary atomizer of drying tower, the mist drop for being atomized into 10 ~ 60mm of average grain diameter is sprayed into drying tower, while introduces branch pipe 1
High-temperature flue gas as thermal source, waste water is evaporated in spray drying tower 4；
（4）Low-temperature flue gas in a part is drawn from branch pipe 2 20, by introducing branch pipe 1 after Smoke-heating device（High-temperature flue gas
Flue）Enter spray drying tower afterwards；When power plant's operating load reduces, flue gas is extracted directly before air preheater to power plant's coal consumption etc.
Have a great influence, by being supplemented in high-temperature flue gas after low-temperature flue gas in being introduced into suitably heating, while reduce the extraction of high-temperature flue gas, from
And reduce the influence to boiler of power plant efficiency；
（5）The spray-dried tower 4 of desulfurization wastewater enters the small-sized pre-duster 7 installed additional with flue gas after drying evaporation, dry to spraying
The harmful substances such as the salt after dry in flue gas are collected, the material of collection together with the material of the bottom collection of spray drying tower 4,
Waste residue disposal plant is delivered to, is individually handled collectively as dangerous waste；
（6）Flue gas returns to the impurity such as the front end of power plant's original electric cleaner 9, flyash and enters electric cleaner 9 after the collection of pre-duster 7
Collect again, so as to really reliablely and stablely realize desulfurization wastewater zero-emission.
Power plant comes out the flow for sending out waste gas primary abatement or denitration, dedusting, desulfurization, and present invention is primarily intended to will be original
The waste water directly discharged after desulfurization is evaporated, collected, and the present invention adds waste water treatment, small-sized pre- dedusting work after desulfurization
Sequence, zero-emission is really realized, the quality of fly ash after electric cleaner dedusting is high, is easy to recycle；And cost is low, efficiency
Height, it is easy to promote.
Technological means disclosed in the present invention program is not limited only to the technological means disclosed in above-mentioned embodiment, in addition to
Formed technical scheme is combined by above technical characteristic.
Claims (9)
- A kind of 1. Desulphurization for Coal-fired Power Plant zero emission method of wastewater, it is characterised in that：Caused waste water passes through three after wet desulphurization After box technology simply pretreatment, a small amount of Ca (OH) is added2Pass through the rotary atomizer of spray drying tower, mist after slurries are well mixed The mist drop for being melted into average grain diameter 10 ~ 60mm is sprayed into drying tower, by the use of air preheater before boiler high-temperature flue gas as thermal source, Waste water is evaporated in spray drying tower, moisture enters in flue gas, and the salt in waste water is collected after drying, and reaches desulfurization and gives up The purpose of water zero discharge.
- A kind of 2. Desulphurization for Coal-fired Power Plant zero emission method of wastewater according to claim 1, it is characterised in that：After air preheater Low-temperature flue gas in a part is drawn, by entering spray drying tower after the mixing of high-temperature flue gas flue is introduced after Smoke-heating device.
- A kind of 3. Desulphurization for Coal-fired Power Plant zero emission method of wastewater according to claim 1, it is characterised in that：It is being spray-dried Install small-sized pre-duster between tower and electric cleaner additional, to collect the materials such as the salt after spray drying in flue gas, collection Material is delivered to waste residue disposal plant together with the material of spray drying tower bottom collection, is individually handled collectively as dangerous waste.
- A kind of 4. Desulphurization for Coal-fired Power Plant zero emission method of wastewater according to claim 1, it is characterised in that：The Ca (OH)2 Concentration of slurry is 5% ~ 25%.
- A kind of 5. Desulphurization for Coal-fired Power Plant zero emission method of wastewater according to claim 1, it is characterised in that：Desulfurization wastewater stream The conveyance conduit of warp uses Glass Flake Substrate anti-corrosion, 2.0 ~ 3.5mm of glass flake thickness；Spray drying inner wall of tower uses glass Scale lining, additional glass-fiber-fabric enhancing, glass flake 1.5 ~ 3.0mm of thickness, 1 ~ 2 layer of glass-fiber-fabric, thickness is in 0.2 ~ 0.6mm.
- A kind of 6. Desulphurization for Coal-fired Power Plant wastewater zero discharge system, it is characterised in that：Including boiler, boiler is sequentially connected denitration reaction Device, air preheater, electric cleaner, wet desulphurization device, chimney；The delivery port of the wet desulphurization device by three header devices, Waste water tank, high-order feed box connection spray drying tower, waste water tank connects with slurry tank, between the Benitration reactor and air preheater Spray drying tower is connected provided with branch pipe one, branch pipe two is provided between air preheater and electric cleaner and connects spray drying tower, branch pipe two Smoke-heating device is provided with, pre-duster is provided between spray drying tower and electric cleaner, waste residue is provided with below pre-duster Processing unit.
- A kind of 7. Desulphurization for Coal-fired Power Plant wastewater zero discharge system according to claim 6, it is characterised in that：Spray drying tower Import and export flue and inlet baffle and outlet damper are set, inlet baffle performs structure using adjustment type, and outlet damper is using switch Type performs structure.
- A kind of 8. Desulphurization for Coal-fired Power Plant wastewater zero discharge system according to claim 6, it is characterised in that：The high position is given Hopper Joining Technology water tank.
- A kind of 9. Desulphurization for Coal-fired Power Plant wastewater zero discharge system according to claim 6, it is characterised in that：The flue gas adds Thermal is provided with control valve.
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108285188A (en) * | 2018-03-13 | 2018-07-17 | 南京常荣声学股份有限公司 | A kind of UTILIZATION OF VESIDUAL HEAT IN coordinated desulfurization wastewater zero discharge and the device and method for removing plume |
| CN109059027A (en) * | 2018-08-27 | 2018-12-21 | 山东电力工程咨询院有限公司 | A kind of high-temperature biomass gas is cooling and the system and method for UTILIZATION OF VESIDUAL HEAT IN |
| CN109110846A (en) * | 2018-08-22 | 2019-01-01 | 盛发环保科技（厦门）有限公司 | A kind of desulfurization wastewater flue gas concentration decrement and cement fixed system and technique |
| CN109607907A (en) * | 2018-10-17 | 2019-04-12 | 北京国电龙源环保工程有限公司 | A kind of desulfurization wastewater multi-heat source coupled processing system and processing method |
| CN109970130A (en) * | 2019-04-11 | 2019-07-05 | 北京国电龙源环保工程有限公司 | Wastewater zero discharge and desulfurization fume disappear white integrated treatment unit and processing method |
| CN110790335A (en) * | 2018-12-13 | 2020-02-14 | 北京国电龙源环保工程有限公司 | Wastewater zero discharge and desulfurization flue gas white elimination integrated treatment device and treatment method |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103420549A (en) * | 2013-07-26 | 2013-12-04 | 新汶矿业集团有限责任公司 | Harmless waste treatment method in coal chemical industry |
| CN105152254A (en) * | 2015-10-08 | 2015-12-16 | 河北省电力勘测设计研究院 | Flue gas desulfurization and wastewater treatment system for coal-fired power plant |
| CN106315915A (en) * | 2016-09-13 | 2017-01-11 | 上海电气电站环保工程有限公司 | Zero-emission and salt-separation desulphurization wastewater treatment system |
| CN106517628A (en) * | 2016-09-21 | 2017-03-22 | 上海发电设备成套设计研究院 | Desulfurization-wastewater zero discharging device for coal-fired power plant |
| CN107162084A (en) * | 2017-06-16 | 2017-09-15 | 浙江大学 | A kind of salt water treating system and its method with preposition heat exchanger and rear end deduster |
| CN207738568U (en) * | 2017-10-11 | 2018-08-17 | 江苏中建材环保研究院有限公司 | A kind of Desulphurization for Coal-fired Power Plant wastewater zero discharge system |
-
2017
- 2017-10-11 CN CN201710942060.9A patent/CN107697967A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103420549A (en) * | 2013-07-26 | 2013-12-04 | 新汶矿业集团有限责任公司 | Harmless waste treatment method in coal chemical industry |
| CN105152254A (en) * | 2015-10-08 | 2015-12-16 | 河北省电力勘测设计研究院 | Flue gas desulfurization and wastewater treatment system for coal-fired power plant |
| CN106315915A (en) * | 2016-09-13 | 2017-01-11 | 上海电气电站环保工程有限公司 | Zero-emission and salt-separation desulphurization wastewater treatment system |
| CN106517628A (en) * | 2016-09-21 | 2017-03-22 | 上海发电设备成套设计研究院 | Desulfurization-wastewater zero discharging device for coal-fired power plant |
| CN107162084A (en) * | 2017-06-16 | 2017-09-15 | 浙江大学 | A kind of salt water treating system and its method with preposition heat exchanger and rear end deduster |
| CN207738568U (en) * | 2017-10-11 | 2018-08-17 | 江苏中建材环保研究院有限公司 | A kind of Desulphurization for Coal-fired Power Plant wastewater zero discharge system |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108285188A (en) * | 2018-03-13 | 2018-07-17 | 南京常荣声学股份有限公司 | A kind of UTILIZATION OF VESIDUAL HEAT IN coordinated desulfurization wastewater zero discharge and the device and method for removing plume |
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