CN208732818U - A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system - Google Patents

A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system Download PDF

Info

Publication number
CN208732818U
CN208732818U CN201721901115.3U CN201721901115U CN208732818U CN 208732818 U CN208732818 U CN 208732818U CN 201721901115 U CN201721901115 U CN 201721901115U CN 208732818 U CN208732818 U CN 208732818U
Authority
CN
China
Prior art keywords
spray drying
clarifying basin
drying tower
waste water
electrodialysis
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201721901115.3U
Other languages
Chinese (zh)
Inventor
任丹丹
冯罗澍
童晓凡
张岚
陈颖
张卫灵
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.)
Energy Source In China Construction Group Zhejiang Province Power Design Institute Co Ltd
Original Assignee
Energy Source In China Construction Group Zhejiang Province Power Design Institute 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 Energy Source In China Construction Group Zhejiang Province Power Design Institute Co Ltd filed Critical Energy Source In China Construction Group Zhejiang Province Power Design Institute Co Ltd
Priority to CN201721901115.3U priority Critical patent/CN208732818U/en
Application granted granted Critical
Publication of CN208732818U publication Critical patent/CN208732818U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system, the processing system is mainly made of lime clarifying basin, sodium carbonate clarifying basin, electrodialysis system, reverse osmosis unit and spray drying tower, pass through the electrodialysis system behind the Dual alkali softening sewage pretreatment device that lime clarifying basin, sodium carbonate clarifying basin are constituted, spray drying tower is connected by waste water pump behind electrodialysis system, the top gas outlet of spray drying tower connects fume afterheat exchanger, after a deduster, desulfurizing tower is connected through air-introduced machine;Its processing method is: after lime clarifying basin and the clarification tank depth pretreatment of sodium carbonate clarifying basin two-stage, again after electrodialysis system concentration, waste water enters spray drying tower through waste water pump, enter smoke gas afterheat heat exchanger after the atomization of high-speed rotating atomizer is fine drop group and flue gas carries out sufficient heat exchange, using fume afterheat wink-dry desulfurization wastewater, the discharge outlet discharge from spray drying tower bottom such as most of solid matter of generation is evaporated.

Description

A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system
Technical field
The utility model relates to a kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment systems, belong at power-plant waste Manage technical field.
Background technique
China is the country of a drought and water shortage, and water resource is relatively deficient.The shortage of water resource have become restriction country and The serious problems of local economic development.Only Comprehensive utilizes the effective way for being only solution water shortage and blowdown environmental pollution Diameter.With water resource growing tension and environmental requirement it is increasingly stringent, coal-burning power plant it is water-saving subtract it is dirty imperative.Country is right The environment that thermal power plant generates influences requirement, and more stringent requirements are proposed: " realizing full factory waste water zero discharge ".Coal-burning power plant is useless Water recycling substantially after full factory's water affairs management, by finally can not reuse to other systems industrial wastewater be used as desulfurization use Water, so desulfurization wastewater processing is the key that full factory's zero-emission.The desulfurization wastewater zero-emission of coal-burning power plant can be maximum Wastewater disposition is reduced, there is good environmental benefit and social benefit.
The coal-burning power plant of desulfurizing fly ash is completed mainly using lime stone-gypsum wet flue gas desulfurizing technique at present. Lime stone-gypsum wet sulfur removal technology generallys use lime stone as desulfurization absorbent, will mix after limestone crushing with water, It is levigate to become powdery, absorption slurries are made.It absorbs slurries and is sent to desulfurizing tower as loop slurry, loop slurry is by nozzle from upper And lower spray, it is contacted with the flue gas adverse current flowed from bottom to top, the sulfur dioxide in flue gas is rapidly absorbed into slurry pool and lime Stone, air oxidation, which react, generates gypsum, and sulfur dioxide is removed, and gypsum is transported through dehydration.
Desulphurization circulating slurries cause chlorine ion concentration continuous due to constantly absorbing the chloride in flue gas and lime stone Increase, increasing for concentration can bring many adverse effects, such as inhibit the dissolution of lime stone, reduce the pH value of slurries, influence The assimilation effect of sulfur dioxide, makes CaSO4It is easy to fouling, and accelerates the corrosion etc. of metal material.In addition, chlorine ion concentration is excessively high Also it will affect the quality of desulfurizing byproduct gypsum.For the normal operation for guaranteeing desulphurization system, should generally control in absorption tower chlorine from Sub- content is lower than 20000mg/L.In addition, dust also can constantly accumulate in loop slurry, desulphurization system as chloride ion Fine dust carried in flue gas dust, the inert substance in lime stone, dormant small gypsum crystal and Impurity etc. in process water.For the purity and the normal physicochemical properties of system slurry for guaranteeing commercial gypsum, need to system Interior fine dust concentration is controlled.
Therefore, in order to guarantee the normal operation of desulphurization system and the quality of desulfurizing byproduct gypsum, it is necessary to discharge a certain amount of Desulfurization wastewater.The waste water of desulphurization system discharge is generally from lower unit: overflow water, the waste-water vortex of gypsum hydrocyclone Overflow water, filtrate of vacuum belt filter of device etc..Desulfurization wastewater is generally weakly acidic, coal-burning power plant's wet desulphurization waste water Typical water quality see the table below.
Coal-burning power plant's wet desulphurization waste water typical case's water quality
Project Unit Data Project Unit Data
pH 4.0-6.0 Fe2+ mg/L ≤30
SS mg/L 20000-50000 Al3+ mg/L ≤50
F- mg/L 20-40 Mn2+ mg/L ≤30
Cl- mg/L 1000-20000 Cr2+ mg/L ≤5
SO4 2- mg/L 2000-5000 Ni2+ mg/L ≤2
SO3 2- mg/L 0-200 Zn2+ mg/L 5-25
S2O6 2- mg/L 500-1000 Cd2+ mg/L 0.5-25
NO3- mg/L 100-200 Cu2+ mg/L 5-23
Ca2+ mg/L 500-5000 Pb2+ mg/L 3-15
Mg2+ mg/L 500-5000 Hg2+ mg/L 0.2-5
COD(Cr) mg/L ≤200 V mg/L ≤2
Remarks: desulfurization wastewater water, water quality are by the water quality impact of coal quality and desulphurization system process water, substantially a factory One water, water quality, water quality and water are unstable, and the above is only typical datas.
For the water quality characteristics of desulfurization wastewater, desulfurization wastewater conventional treatment is generally using neutralization, flocculation, precipitating and mistake at present The treatment process such as filter, according to desulfurization waste water quality feature, power industry has formulated that " thermal power plant's lime stone-gypsum wet desulfurization is useless Water Water Quality Control Indexes " (DL/T 997-2006), the index define desulfurization wastewater treatment system outlet monitoring project and dirt Contaminating object highest allows concentration of emission, becomes and instructs the processed conventionally main criteria of power plant desulfurization wastewater.It is conventional pretreated de- Sulphur waste water discharge of major pollutant index should meet: pH:6~9;Ss suspended solid≤70mg/L;COD(Cr)≤150mg/L;Sulfuric acid Radical ion≤3000mg/L.In addition to this, desulfurization wastewater salt content (TDS) is generally 25,000~35,000mg/L, wherein chlorine Ion > 10000mg/L, calcium+magnesium ion > 3000mg/L and according to coal quality fluctuate it is larger.
We are illustrated with Zhejiang Desulphurization for Coal-fired Power Plant waste water system.
2x300MW generator set desulfurization waste water actual amount of water in Zhejiang coal-burning power plant is about 15m3/ h, field measurement water sample water quality It is as follows:
Since the wastewater zero discharge project to have put into operation at present is seen, project cost height and operating cost height are two most outstanding Problem, this just needs to find more preferably method for treating desulfurized wastewater from improving heat utilization ratio and reducing the angle of cost.
Summary of the invention
The purpose of the utility model is to overcome the shortcomings of the prior art, and provide one kind and combine film concentration and side Road flue spray drying technology, is able to achieve wastewater zero discharge, and the coal-burning power plant for having reached reduction investment and operating cost purpose is de- Sulphur Wastewater zero-discharge treatment system and method.
The purpose of this utility model is completed by following technical solution, a kind of Desulphurization for Coal-fired Power Plant wastewater zero discharge Processing system, it is mainly by lime clarifying basin, sodium carbonate clarifying basin, electrodialysis system, reverse osmosis unit and spray drying tower group At by Dual alkali sofening treatment dress behind the waste gas pre-treating device that the lime clarifying basin, sodium carbonate clarifying basin are constituted It sets and connects the electrodialysis system, spray drying tower is connected by waste water pump behind the electrodialysis system, it is described spraying dry The top gas outlet connection fume afterheat exchanger of dry tower connects desulfurizing tower through air-introduced machine after a deduster.
As preferred: the bottom of the spray drying tower passes through storehouse pump one Solid state fermentation system of connection;The electric osmose Also connect reverse osmosis unit all the way on analysis system, and the Dual alkali sofening treatment device described by reverse osmosis unit connection, in institute It states and also mating before electrodialysis system an electrodialysis feed pump is installed;A waste water tank is connected to behind the electrodialysis system, The wastewater outlet of the waste water tank first connects a high-order feed box, the high position feed box being sprayed described in connection by a waste water pump Drying tower.
It is a kind of to carry out Desulphurization for Coal-fired Power Plant wastewater zero discharge using the Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system Processing method, this method are then the electrodialysis after lime clarifying basin and the clarification tank depth pretreatment of sodium carbonate clarifying basin two-stage After system concentration, waste water enters spray drying tower through waste water pump, after the atomization of high-speed rotating atomizer is fine drop group Sufficient heat exchange is carried out into smoke gas afterheat heat exchanger and flue gas, using fume afterheat wink-dry desulfurization wastewater, evaporation is produced The discharge outlet discharge from spray drying tower bottom such as raw most of solid matter;Tail gas after spray-dried tower is dry returns The import of electric precipitator enters desulfurizing tower after air-introduced machine.
The utility model is using lime clarifying basin → sodium carbonate clarifying basin → electrodialysis → bypass flue spray drying work The advantages of skill route, the program are as follows: technique of the electrodialysis as enriching stage, investment and operating cost all relatively economicals;It examines Consider and Waste water concentrating to about 20% is used into high-temperature flue gas desiccation again, operating cost can be reduced;Bypass flue process system heat benefit High with rate, heat loss is small.
Detailed description of the invention
Fig. 1 is the flow diagram of desulfurization wastewater zero-discharge treatment system described in the utility model.
Specific embodiment
Detailed introduction is done to the utility model below in conjunction with attached drawing: shown in Fig. 1, a kind of combustion described in the utility model Coal-fired plant's desulfurization wastewater zero-discharge treatment system, it is mainly by lime clarifying basin, sodium carbonate clarifying basin, electrodialysis system 4, reverse osmosis Saturating device 5 and spray drying tower 9 form, the waste gas pre-treating device 1 that the lime clarifying basin, sodium carbonate clarifying basin are constituted The electrodialysis system 4 is connected by Dual alkali sofening treatment device 2 below, passes through waste water behind the electrodialysis system 4 7 connection spray drying tower 9 of pump, the top gas outlet of the spray drying tower 9 connects fume afterheat exchanger 12, removes by one After dirt device 13, desulfurizing tower 15 is connected through air-introduced machine 14, exhaust gas after processing is discharged through chimney 16.
As shown in the figure, the bottom of the spray drying tower 9 passes through 10 one Solid state fermentation system 11 of connection of storehouse pump;Described Also connect reverse osmosis unit 5 all the way on electrodialysis system 4, and connects the Dual alkali sofening treatment by reverse osmosis unit 5 and fill 2 are set, it is also mating before the electrodialysis system 4 that an electrodialysis feed pump 3 is installed;Connect behind the electrodialysis system 4 There is a waste water tank 6, the wastewater outlet of the waste water tank 6 first connects a high-order feed box 8, the high position feed box 8 by a waste water pump 7 Reconnect the spray drying tower 9.
It is a kind of to carry out Desulphurization for Coal-fired Power Plant wastewater zero discharge using the Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system Processing method, which is: after lime clarifying basin and the clarification tank depth pretreatment of sodium carbonate clarifying basin two-stage, then electricity After electrodialysis system concentration, waste water enters spray drying tower through waste water pump, is fine drop by the atomization of high-speed rotating atomizer Enter smoke gas afterheat heat exchanger after group and flue gas carries out sufficient heat exchange, using fume afterheat wink-dry desulfurization wastewater, steams Send out the discharge outlet discharge from spray drying tower bottom such as most of solid matter generated;Tail gas after spray-dried tower is dry The import for returning to electric precipitator enters desulfurizing tower after air-introduced machine.
Embodiment: a kind of Desulphurization for Coal-fired Power Plant wastewater treatment method, it mainly by lime clarifying basin, sodium carbonate clarifying basin, Electrodialysis system, counter-infiltration system and spray drying tower composition.Waste water raw water water 15t/h, after depth pretreatment system, It produces water and squeezes into electrodialysis system through filtering pump, and lime clarifying basin spoil disposal is sent through dehydration to grey factory or as fixed-end forces; Sodium carbonate clarifying basin spoil disposal sends FGD lime stock tank back to and does slurries.Select electrodialysis by Waste water concentrating to 3t/h, two units are respectively set The spray drying tower of a set of 3t/h, the using and the reserved.By taking 30MW unit as an example, the total flue gas of bypass flue gas Zhan needed for dry 3t waste water Ratio about 3.5% is measured, it is smaller to be calculated influence to air preheater.Waste water enters drying tower through waste water pump after electrodialysis concentration, passes through High-speed rotating atomizer atomization is crossed to carry out sufficient heat exchange with flue gas after fine drop group, is done using fume afterheat moment Dry desulfurization wastewater evaporates the discharge outlet discharge from spray drying tower bottom such as most of solid matter of generation;It is spray-dried Tail gas after tower is dry returns to electric precipitation import.The water outlet of electrodialysis fresh water side returns to depth pretreatment system reuse.This technique cigarette The object that is evaporated after the dry waste water of gas is finally mixed into flyash.
Desulfurization wastewater is after pretreatment, at the two-stage coagulation clarification softening by lime clarifying basin and sodium carbonate clarifying basin Science and engineering skill removes solid suspension, heavy metal and Ca in water removal to greatest extent2+、Mg2+、SO4 2-、F-, the foulings factor such as silicon, Electrodialysis plant is squeezed by pump after filtering.Strong brine after electrodialysis is concentrated enters bypass flue spraying system, fresh water Side waste water is retracted into depth pretreatment system by reverse osmosis concentrated.Bypass flue is to export to draw hot fume from denitration by spraying, warp Bypass flue is sent to spray drying tower;Desulfurization wastewater enters drying tower by the road, is thin by the atomization of high-speed rotating atomizer Sufficient heat exchange, which is carried out, with flue gas after droplet group evaporates the big portion of generation using fume afterheat wink-dry desulfurization wastewater Divide the discharge outlet discharge from spray drying tower bottom such as solid matter;Tail gas after spray-dried tower is dry return electric precipitation into Mouthful.The object that is evaporated after flue gas drying waste water is finally mixed into flyash.

Claims (2)

1. a kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system, it is mainly by lime clarifying basin, sodium carbonate clarifying basin, electric osmose Analysis system, reverse osmosis unit and spray drying tower composition, it is characterised in that the lime clarifying basin, sodium carbonate clarifying basin are constituted Dual alkali softening sewage pretreatment device behind pass through the electrodialysis system, pass through waste water behind the electrodialysis system Pump connection spray drying tower, the top gas outlet of the spray drying tower connect fume afterheat exchanger, are passing through a deduster Afterwards, desulfurizing tower is connected through air-introduced machine.
2. Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system according to claim 1, it is characterised in that described spraying dry The bottom of dry tower passes through storehouse pump one Solid state fermentation system of connection;Also connect reverse osmosis dress all the way on the electrodialysis system It sets, and the Dual alkali sofening treatment device described by reverse osmosis unit connection, it is also mating before the electrodialysis system to be equipped with One electrodialysis feed pump;A waste water tank is connected to behind the electrodialysis system, the wastewater outlet of the waste water tank is useless by one Water pump first connects a high-order feed box, which reconnects the spray drying tower.
CN201721901115.3U 2017-12-29 2017-12-29 A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system Active CN208732818U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721901115.3U CN208732818U (en) 2017-12-29 2017-12-29 A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721901115.3U CN208732818U (en) 2017-12-29 2017-12-29 A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system

Publications (1)

Publication Number Publication Date
CN208732818U true CN208732818U (en) 2019-04-12

Family

ID=66022841

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721901115.3U Active CN208732818U (en) 2017-12-29 2017-12-29 A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system

Country Status (1)

Country Link
CN (1) CN208732818U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107892427A (en) * 2017-12-29 2018-04-10 中国能源建设集团浙江省电力设计院有限公司 A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system and method
CN111437701A (en) * 2020-05-08 2020-07-24 浙江浙能技术研究院有限公司 System and method for balancing and treating materials in slurry of limestone wet desulphurization absorption tower

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107892427A (en) * 2017-12-29 2018-04-10 中国能源建设集团浙江省电力设计院有限公司 A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system and method
CN111437701A (en) * 2020-05-08 2020-07-24 浙江浙能技术研究院有限公司 System and method for balancing and treating materials in slurry of limestone wet desulphurization absorption tower

Similar Documents

Publication Publication Date Title
CN107892427A (en) A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system and method
CN104355473B (en) A kind of method using electrodialytic technique to carry out power plant desulfurization waste water desalination zero discharge treatment
CN105817134A (en) Chemical process wet-method desulphurization technology
CN109647164B (en) Zero-emission wastewater desulfurization process and device
CN107129094A (en) The Zero discharging system of desulfurization wastewater is evaporated based on multi-heat source
CN105481157A (en) Method for zero emission treatment of desulfurization waste water based on flue gas waste heat evaporation
CN105254101A (en) Desulfurization waste water zero-discharging treatment technology for coal-fired power plants
CN104085934B (en) A kind of method of heat-engine plant desulfurized waste water high-efficiency spray evaporation nucleation
CN105967420A (en) Synergistic gas-liquid-solid pollutant treatment system based on power plant wastewater zero-discharge technology
CN109384332A (en) A kind of method of coal burning flue gas desulfurization wastewater treatment
CN104129824A (en) Method for heat-engine plant desulfurization wastewater comprehensive treatment and dust particle emission reduction
CN101347706A (en) Flue gas desulfurization technique using dual alkali method with acetylene sludge as recycling agent
CN208732818U (en) A kind of Desulphurization for Coal-fired Power Plant Wastewater zero-discharge treatment system
CN205556349U (en) Novel zero release of desulfurization waste water is handled device
CN106517628A (en) Desulfurization-wastewater zero discharging device for coal-fired power plant
CN109399855A (en) A kind of zero emission treatment of desulfured waste water
CN107176742A (en) A kind of desulfurization wastewater rotational flow dust-removing method
CN208857076U (en) A kind of desulfurization wastewater treatment system
CN105621775A (en) Novel desulfurated wastewater zero-emission treatment device and method
CN110756027B (en) Promote low-cost desulfurization waste water zero discharge system of gypsum quality
CN107899383B (en) Mixed desulfurizer prepared from red mud and seawater and flue gas desulfurization method thereof
CN206751583U (en) Desulfurization wastewater Zero discharging system based on ion selectivity electrodialytic technique
CN215506351U (en) Desulfurization absorbent purifies regeneration system
CN112973403A (en) Method for desulfurizing white mud
CN211339161U (en) Treatment device for realizing zero discharge of desulfurization wastewater by bypass evaporation process

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant