CN206799333U - A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system - Google Patents
A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system Download PDFInfo
- Publication number
- CN206799333U CN206799333U CN201720605647.6U CN201720605647U CN206799333U CN 206799333 U CN206799333 U CN 206799333U CN 201720605647 U CN201720605647 U CN 201720605647U CN 206799333 U CN206799333 U CN 206799333U
- Authority
- CN
- China
- Prior art keywords
- water inlet
- delivery port
- sedimentation basins
- medicine
- water
- 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
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system, the system includes regulating reservoir, #1 sedimentation basins, reaction tank, #2 sedimentation basins, aerated precipitation tank, intermediate pool, electrolysis system, filtration system, clear water reserviors, nanofiltration system, nanofiltration water producing tank, #1 coagulant medicine systems, #1 flocculation aid medicine systems, gypsum dehydration system, gypsum return-flow system, #1 sodium hydroxide medicine systems, #2 coagulant medicine systems, #2 flocculation aid medicine systems, magnesium hydroxide return-flow system, desulphurization absorption tower system, aerating system, #2 sodium hydroxide medicine systems, acid adding system, filter backwash system, reducing agent medicine system, Tthe utility model system can reduce the operating cost of high-salt wastewater processing, realize heat-engine plant desulfurized waste water reclaiming.
Description
Technical field
The present invention relates to a kind of heat-engine plant desulfurized Waste Water Treatment and method, and in particular to a kind of Desulphurization for Coal-fired Power Plant gives up
Recycling of water resource system.
Background technology
《Water prevention and cure of pollution action plan》It is required that electricity power enterprise carries out waste water advanced treatment recovery, many local environmental protection policies
Efflux wastewater salt content is limited, and new power plant construction environmental impact assessment reply is intended to factory waste water zero discharge of demanding perfection.Desulfurization wastewater salt content is high,
Direct reuse is unable in factory, is the difficult point that coal-burning power plant's wastewater zero discharge is administered.
In the area of limitation power plant efflux wastewater salt content, desulfurization wastewater qualified discharge or zero-emission are realized, is both needed to pair
Desulfurization wastewater carries out film desalination.Because environmental protection policy requires more and more higher to power plant's water saving, part power plant is by Wastewater Form Circulating Cooling Water
With sewage reuse to desulphurization system, content of organics in desulfurization wastewater is caused to raise.And in the power plant desulfurization wastewater of part
Ammonia nitrogen concentration more and more higher, this mainly due to, one, power plant is using the reuse of precision processing regenerative wastewater as desulphurization system process water；Two,
To meet the ultra-clean emission request of flue gas, the denitration of part power plant sprays into excess ammonia, causes ammonia largely to be escaped to desulfuration absorbing tower.
At present, desulfurization wastewater conventional treatment process is " three headers-depositing reservoir-softening-film concentration-evaporative crystallization ", the work
Following defect be present in skill：Desulfurization wastewater organic matter is easily dirty to block up film, causes film desalination system can not stable operation；Ammonia influences evaporation
Crystallization, increase evaporative crystallization cost, and reduce crystallization purity salt, crystal salt can not recycle.
The content of the invention
It is an object of the invention to overcome above-mentioned prior art shortcoming, there is provided a kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system
System, the system can reduce the operating cost of high-salt wastewater processing, realize heat-engine plant desulfurized waste water reclaiming.
To reach above-mentioned purpose, the present invention adopts the following technical scheme that：
A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system, mainly including pliable cell, electrolysis cells and film upgrading unit；
The pliable cell, which includes regulating reservoir 1, #1 sedimentation basins 2, reaction tank 3, #2 sedimentation basins 4, aerated precipitation tank 5, #1, to be mixed
Solidifying agent medicine system 12, #1 flocculation aids medicine system 13, #1 sodium hydroxides medicine system 16, #2 coagulant medicine system 17, #2
Flocculation aid medicine system 18, gypsum dehydration system 14, gypsum return-flow system 15, magnesium hydroxide return-flow system 19, #2 sodium hydroxides
Medicine system 22, desulphurization absorption tower system 20, aerating system 21；
Wherein desulfurization wastewater is connected with the water inlet of regulating reservoir 1, and the delivery port of regulating reservoir 1 is connected with the water inlet of #1 sedimentation basins 2, #1
The delivery port of sedimentation basin 2 is connected with the water inlet of reaction tank 3, and the outlet of reaction tank 3 is connected with the water inlet of #2 sedimentation basins 4, and #2 sedimentation basins 4 go out
The mouth of a river is connected with the water inlet of aerated precipitation tank 5, and the delivery port of aerated precipitation tank 5 is connected with follow-up electrolysis cells；
#1 coagulant medicine system 12 is connected with the coagulant dosing mouth of regulating reservoir 1, #1 flocculation aids medicine system 13 and regulation
The flocculation aid dosing mouth of pond 1 is connected；The mud discharging mouth of #1 sedimentation basins 2 is connected with gypsum dehydration system 14；#1 sodium hydroxides medicine system 16
It is connected with the sodium hydroxide dosing mouth of reaction tank 3, #2 coagulant medicine system 17 is connected with the coagulant dosing mouth of reaction tank 3, and #2 is helped
Solidifying agent medicine system 18 is connected with the flocculation aid dosing mouth of reaction tank 3, is sold outside the bottom spoil disposal of #2 sedimentation basins 4, the water outlet of aerated precipitation tank 5
Mouth is connected with the water inlet of regulating reservoir 1；#2 sodium hydroxides medicine system 22 is connected with the sodium hydroxide dosing mouth of aerated precipitation tank 5, exposes
Gas system 21 is connected with the bottom aeration tube of aerated precipitation tank 5, and the mud discharging mouth of aerated precipitation tank 5 is connected with desulphurization absorption tower system 20；
The bottom mud discharging mouth of #1 sedimentation basins 2 is connected with the water inlet of gypsum return-flow system 15, the delivery port of gypsum return-flow system 15 with
The water inlet of regulating reservoir 1 is connected, and the bottom mud discharging mouth of #2 sedimentation basins 4 is connected with the water inlet of magnesium hydroxide return-flow system 19, magnesium hydroxide
The delivery port of return-flow system 19 is connected with the water inlet of reaction tank 3；
The electrolysis cells include intermediate pool 6, electrolysis system 7 and acid adding system 23；
Wherein the delivery port of aerated precipitation tank 5 of pliable cell is connected with the water inlet of intermediate pool 6, the delivery port of intermediate pool 6
It is connected with the water inlet of electrolysis system 7, the delivery port of electrolysis system 7 is connected with film upgrading unit, and acid adding system 23 adds with intermediate pool 6
Sour mouth is connected；
It is anti-that the film upgrading unit includes filtration system 8, clear water reserviors 9, nanofiltration system 10, nanofiltration water producing tank 11, filter
Wash system 24, reducing agent medicine system 25；
Wherein the electrolysis system 7 of electrolysis cells is connected with the water inlet of filtration system 8, the delivery port and clear water of filtration system 8
The water inlet of pond 9 is connected, and the delivery port of clear water reserviors 9 is connected with the water inlet of nanofiltration system 10, and nanofiltration system 10 produces the mouth of a river and nanofiltration production water
The water inlet of case 11 is connected, and the concentrated water spout of nanofiltration system 10 is connected with the water inlet of pliable cell regulating reservoir 1；The delivery port of clear water reserviors 9 and mistake
The water inlet of filter backwashing system 24 is connected, and the delivery port of filter backwash system 24 is connected with the backwash water inlet of filtration system 8, filtering
The backwash water out of system 8 is connected with pliable cell #1 sedimentation basins 2；Reducing agent medicine system 25 and the water inlet phase of nanofiltration system 10
Even.
The method of work of described Desulphurization for Coal-fired Power Plant waste water reclaiming system：
Desulfurization wastewater after coal-burning power plant conventional " three headers-clarifier " processing is in sub-saturated in alkalescence, calcium sulfate
State, mixed in regulating reservoir 1 with film upgrading unit nanofiltration concentrated water, a large amount of SO are contained in nanofiltration concentrated water4 2-, therefore, regulating reservoir 1
In calcium sulfate be in hypersaturated state, crystallization separates out, and through the separation of solid and liquid of #1 sedimentation basins 2, the bottom gypsum of #1 sedimentation basins 2 drains into electricity
The original gypsum dehydration system 14 of factory, the bottom gypsum part of #1 sedimentation basins 2 are back to regulating reservoir 1 and play a part of crystal seed, improve
The crystalline rate of calcium sulfate, remove part Ca2+, the flocculation Accelerated subsidence through coagulant, flocculation aid；
Reaction tank 3 adds sodium hydroxide, removes Mg in desulfurization wastewater2+, the high Mg (OH) of generation purity2, Mg (OH)2Make
To be sold outside refractory material；The bottom Mg (OH) of #2 sedimentation basins 42Part is back to reaction tank 3 and plays a part of crystal seed, improves Mg2+'s
Removal effect, the flocculation Accelerated subsidence through coagulant, flocculation aid, separation of solid and liquid is realized in #2 sedimentation basins；
Exposed under the alkaline environment of aerated precipitation tank 5 into appropriate CO2, the high CaCO of generation purity3, remove Ca2+, CaCO3As de-
Sulphur agent is mended and recycled to desulphurization absorption tower system 20, realizes recycling；
The water outlet of aerated precipitation tank 5 is in strong basicity, and the water part of aerated precipitation tank 5 is back to regulating reservoir 1, improves regulating reservoir
PH, the solubility product of calcium sulfate is reduced, improve Ca2+Removal effect, while improve pliable cell Ca total to desulfurization wastewater2+And Mg2+'s
Removal effect；
Pliable cell water outlet adds acid for adjusting pH, into electrolysis system 7, to remove organic matter and ammonia in desulfurization wastewater to acidity
Nitrogen；
After softened unit and electrolysis cells, leading ion is Na in desulfurization wastewater+、Cl-And SO4 2-, removed by filter
Suspension, after adding reducing agent, into nanofiltration system 10, using nanofiltration system 10 to SO4 2-High rejection realize a divalence from
Son separation, concentrated water is NaCl and NaSO4, pliable cell regulating reservoir 1 is back to, removes Ca2+, save softening medicament expense and use；Nanofiltration is produced
Water is high concentration NaCl solution, as industrial chemicals recycling.
The invention has the advantages that：
(1) nanofiltration NF concentrated water reuse is to softening single time regulating reservoir, and by exposing into appropriate carbon dioxide, removes Ca2+, reduce soft
The medicament expense for eliminating calcium is used.
(2) Ca can be respectively increased in gypsum backflow and magnesium hydroxide backflow2+And Mg2+Removal effect.
(3) electrolysis cells efficiently remove ammonia nitrogen and organic matter in desulfurization wastewater, improve film upgrading unit stability and chlorination
Sodium product quality.
(4) Ca is removed2+Caused gypsum removes the original gypsum dehydration system of power plant；CaCO3Desulphurization system is gone as desulfurizing agent,
Recycling；Except Mg2+Caused magnesium hydroxide is sold outside as chemical materials such as fire proofing materials；Whole system is without solid waste
Produce, and ensure that product quality purity caused by unit is high, realize Deep.
Brief description of the drawings
Fig. 1 is the structural representation of present system.
Wherein, 1 it is regulating reservoir, 2 be #1 sedimentation basins, 3 be reaction tank, 4 be #2 sedimentation basins, 5 be aerated precipitation tank, 6 is
Between pond, 7 be electrolysis system, 8 be filtration system, 9 be clear water reserviors, 10 be nanofiltration system, 11 be nanofiltration water producing tank, 12 be that #1 is mixed
Solidifying agent medicine system, 13 be #1 flocculation aids medicine system, 14 be gypsum dehydration system, 15 be gypsum return-flow system, 16 be #1
Sodium hydroxide medicine system, 17 be #2 coagulant medicine system, 18 be #2 flocculation aids medicine system, 19 be magnesium hydroxide backflow system
System, 20 be desulphurization absorption tower system, 21 be aerating system, 22 be #2 sodium hydroxides medicine system, 23 be acid adding system, 24 be
Filter backwashing system, 25 are reducing agent medicine system.
Embodiment
The present invention is described in further detail below in conjunction with the accompanying drawings：
As shown in figure 1, desulfurization wastewater is connected with the water inlet of regulating reservoir 1, the delivery port of regulating reservoir 1 and the water inlet of #1 sedimentation basins 2
It is connected, the delivery port of #1 sedimentation basins 2 is connected with the water inlet of reaction tank 3, and the outlet of reaction tank 3 is connected with the water inlet of #2 sedimentation basins 4, and #2 sinks
The delivery port of shallow lake pond 4 is connected with the water inlet of aerated precipitation tank 5, and the delivery port of aerated precipitation tank 5 is connected with the water inlet of intermediate pool 6, in
Between the delivery port of pond 6 be connected with the water inlet of electrolysis system 7, the delivery port of electrolysis system 7 is connected with the water inlet of filtration system 8, filtering
The delivery port of system 8 is connected with the water inlet of clear water reserviors 9, and the delivery port of clear water reserviors 9 is connected with the water inlet of nanofiltration system 10, nanofiltration system
The 10 production mouths of a river are connected with the water inlet of nanofiltration water producing tank 11, and the concentrated water spout of nanofiltration system 10 is connected with the water inlet of regulating reservoir 1.
#1 coagulant medicine system 12 is connected with the coagulant dosing mouth of regulating reservoir 1, #1 flocculation aids medicine system 13 and regulation
The flocculation aid dosing mouth of pond 1 is connected；The mud discharging mouth of #1 sedimentation basins 2 is connected with gypsum dehydration system 14.
#1 sodium hydroxides medicine system 16 is connected with the sodium hydroxide dosing mouth of reaction tank 3, #2 coagulant medicine system 17 with
The coagulant dosing mouth of reaction tank 3 is connected, and #2 flocculation aids medicine system 18 is connected with the flocculation aid dosing mouth of reaction tank 3, #2 sedimentation basins
Sold outside 4 bottom spoil disposals.#2 sodium hydroxides medicine system 22 is connected with the sodium hydroxide dosing mouth of aerated precipitation tank 5.
The bottom mud discharging mouth of #1 sedimentation basins 2 is connected with the water inlet of gypsum return-flow system 15, the delivery port of gypsum return-flow system 15 with
The water inlet of regulating reservoir 1 is connected.The bottom mud discharging mouth of #2 sedimentation basins 4 is connected with the water inlet of magnesium hydroxide return-flow system 19, magnesium hydroxide
The delivery port of return-flow system 19 is connected with the water inlet of reaction tank 3.
Aerating system 21 is connected with the bottom aeration tube of aerated precipitation tank 5, the mud discharging mouth of aerated precipitation tank 5 and desulfuration absorbing tower system
System 20 is connected.
Acid adding system 23 is connected with the acid-adding port of intermediate pool 6；The delivery port of clear water reserviors 9 and the water inlet of filter backwash system 24
It is connected, the delivery port of filter backwash system 24 is connected with the backwash water inlet of filtration system 8, the backwash water out of filtration system 8 and #1
Sedimentation basin 2 is connected；Reducing agent medicine system 25 is connected with the water inlet of nanofiltration system 10.
The method of work of Desulphurization for Coal-fired Power Plant waste water reclaiming system of the present invention is as follows：
Desulfurization wastewater after coal-burning power plant conventional " three headers-clarifier " processing is in alkaline (pH9.5~10.0), sulphur
Sour calcium is in sub-saturated state, is mixed in regulating reservoir 1 with the concentrated water concentrated water of nanofiltration system 10, in the concentrated water of nanofiltration system 10
Contain a large amount of SO4 2-, therefore, the calcium sulfate in regulating reservoir 1 is in hypersaturated state, and crystallization separates out, through the solid-liquid point of #1 sedimentation basins 2
From the bottom gypsum of #1 sedimentation basins 2 drains into the original gypsum dehydration system 14 of power plant, and the base section gypsum of #1 sedimentation basins 2 passes through stone
Cream return-flow system 15 is back to regulating reservoir 1 and plays a part of crystal seed, improves the crystalline rate of calcium sulfate, removes part Ca2+.#1 is mixed
Solidifying agent medicine system 12 and #1 flocculation aids medicine system 13 are connected with the dosing mouth of regulating reservoir 1, with the flocculation aid dosing of regulating reservoir 1
Mouth is connected, the flocculation Accelerated subsidence through coagulant, flocculation aid.
The delivery port of #1 sedimentation basins 2 is connected with the water inlet of reaction tank 3, and reactor 3 is added by #1 sodium hydroxides medicine system 16
Enter sodium hydroxide, remove Mg in desulfurization wastewater2+, the high Mg (OH) of generation purity2, Mg (OH)2Sold outside as refractory material etc..#2
The bottom Mg (OH) of sedimentation basin 42Part is back to reaction tank 3 by magnesium hydroxide return-flow system 19 and plays a part of crystal seed, improves
Mg2+Removal effect.#2 coagulant medicine system 17 and #2 flocculation aids medicine system 18 are connected with the dosing mouth of reaction tank 3, warp
The flocculation Accelerated subsidence of coagulant, flocculation aid, separation of solid and liquid is realized in #2 sedimentation basins 4.
The delivery port of #2 sedimentation basins 4 is connected with aerated precipitation tank 5, and aerated precipitation tank 5 passes through #2 sodium hydroxides medicine system 22
The pH that sodium hydroxide remains certain is added, aerating system 21 is exposed into appropriate CO2, the high CaCO of generation purity3, remove Ca2+。CaCO3
Desulfurizing agent can be used as to mend to recycle to desulfuration absorbing tower 20, realize recycling.
The water outlet of aerated precipitation tank 5 is in strong basicity, and the water part of aerated precipitation tank 5 is back to regulating reservoir 1, can improve regulating reservoir
PH, the solubility product of calcium sulfate is reduced, improve Ca2+Removal effect, while improve pliable cell Ca total to desulfurization wastewater2+And Mg2+'s
Removal effect.
The delivery port of aerated precipitation tank 5 is connected with the water inlet of intermediate pool 6, acid adding system 23 and the acid-adding port phase of intermediate pool 6
Even, pH to 4.0~6.0 is adjusted, into electrolysis system 7, removes organic matter and ammonia nitrogen in desulfurization wastewater.
After softened unit and electrolysis cells, leading ion is Na in desulfurization wastewater+、Cl-And SO4 2-, filtered system 8
Oil removal is removed, reducing agent medicine system 25 is connected with the water inlet of nanofiltration system 10, after adding reducing agent, into nanofiltration system
10, using nanofiltration system 10 to SO4 2-High rejection realize a divalent ion separate, the concentrated water of nanofiltration system 10 be NaCl and
NaSO4, pliable cell regulating reservoir 1 is back to, removes Ca2+, save softening medicament expense and use；It is high concentration NaCl that nanofiltration system 10, which produces water,
Solution, industrial chemicals recycling can be used as.
The delivery port of electrolysis system 7 is connected with the water inlet of filtration system 8, delivery port and the water inlet of clear water reserviors 9 of filtration system 8
It is connected, the delivery port of clear water reserviors 9 is connected with the water inlet of nanofiltration system 10.The delivery port of clear water reserviors 9 is intake with filter backwash system 24
Mouth is connected, and the delivery port of filter backwash system 24 is connected with the backwash water inlet of filtration system 8, the backwash water out of filtration system 8 and #
1 sedimentation basin 2 is connected, reuse after filter backwash Water Sproading.
The citing of the implementation steps described above for being only the present invention, it is noted that for the ordinary skill of the art
For personnel, without departing from the technical principles of the invention, some improvement and modification can also be made, these improve and become
Type also should be regarded as protection scope of the present invention.
Claims (1)
- A kind of 1. Desulphurization for Coal-fired Power Plant waste water reclaiming system, it is characterised in that：Concentrated including pliable cell, electrolysis cells and film Unit；The pliable cell includes regulating reservoir (1), #1 sedimentation basins (2), reaction tank (3), #2 sedimentation basins (4), aerated precipitation tank (5), #1 coagulant medicine system (12), #1 flocculation aids medicine system (13), #1 sodium hydroxides medicine system (16), #2 coagulant Medicine system (17), #2 flocculation aids medicine system (18), gypsum dehydration system (14), gypsum return-flow system (15), magnesium hydroxide Return-flow system (19), #2 sodium hydroxides medicine system (22), desulphurization absorption tower system (20), aerating system (21)；Wherein desulfurization wastewater is connected with regulating reservoir (1) water inlet, regulating reservoir (1) delivery port and #1 sedimentation basins (2) water inlet phase Even, #1 sedimentation basins (2) delivery port is connected with reaction tank (3) water inlet, reaction tank (3) outlet and #2 sedimentation basins (4) water inlet phase Even, #2 sedimentation basins (4) delivery port is connected with aerated precipitation tank (5) water inlet, and aerated precipitation tank (5) delivery port and follow-up electrolysis are single Member is connected；#1 coagulant medicine system (12) is connected with regulating reservoir (1) coagulant dosing mouth, and #1 flocculation aids medicine system (13) is with adjusting Section pond (1) flocculation aid dosing mouth is connected；#1 sedimentation basins (2) mud discharging mouth is connected with gypsum dehydration system (14)；#1 sodium hydroxides add Medicine system (16) is connected with reaction tank (3) sodium hydroxide dosing mouth, #2 coagulant medicine system (17) and reaction tank (3) coagulant Dosing mouth is connected, and #2 flocculation aids medicine system (18) is connected with reaction tank (3) flocculation aid dosing mouth, #2 sedimentation basins (4) bottom row Mud is sold outside, and aerated precipitation tank (5) delivery port is connected with regulating reservoir (1) water inlet；#2 sodium hydroxides medicine system (22) and aeration Sedimentation basin (5) sodium hydroxide dosing mouth is connected, and aerating system (21) is connected with aerated precipitation tank (5) bottom aeration tube, and aeration is heavy Shallow lake pond (5) mud discharging mouth is connected with desulphurization absorption tower system (20)；#1 sedimentation basins (2) bottom mud discharging mouth is connected with gypsum return-flow system (15) water inlet, gypsum return-flow system (15) delivery port It is connected with regulating reservoir (1) water inlet, #2 sedimentation basins (4) bottom mud discharging mouth is connected with magnesium hydroxide return-flow system (19) water inlet, Magnesium hydroxide return-flow system (19) delivery port is connected with reaction tank (3) water inlet；The electrolysis cells include intermediate pool (6), electrolysis system (7) and acid adding system (23)；Wherein aerated precipitation tank (5) delivery port of pliable cell is connected with intermediate pool (6) water inlet, intermediate pool (6) water outlet Mouth is connected with electrolysis system (7) water inlet, and electrolysis system (7) delivery port is connected with film upgrading unit, and acid adding system (23) is with Between pond (6) acid-adding port be connected；The film upgrading unit includes filtration system (8), clear water reserviors (9), nanofiltration system (10), nanofiltration water producing tank (11), filtering Device backwashing system (24), reducing agent medicine system (25)；Wherein the electrolysis system (7) of electrolysis cells is connected with filtration system (8) water inlet, the delivery port of filtration system (8) with it is clear Pond (9) water inlet is connected, and clear water reserviors (9) delivery port is connected with nanofiltration system (10) water inlet, nanofiltration system (10) the production mouth of a river It is connected with nanofiltration water producing tank (11) water inlet, nanofiltration system (10) concentrated water spout is connected with pliable cell regulating reservoir (1) water inlet；Clearly Pond (9) delivery port is connected with filter backwash system (24) water inlet, and filter backwash system (24) delivery port is with filtering System (8) backwash water inlet is connected, and filtration system (8) backwash water out is connected with pliable cell #1 sedimentation basins (2)；Reducing agent dosing System (25) is connected with nanofiltration system (10) water inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720605647.6U CN206799333U (en) | 2017-05-26 | 2017-05-26 | A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720605647.6U CN206799333U (en) | 2017-05-26 | 2017-05-26 | A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206799333U true CN206799333U (en) | 2017-12-26 |
Family
ID=60743096
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720605647.6U Active CN206799333U (en) | 2017-05-26 | 2017-05-26 | A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206799333U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105819608A (en) * | 2016-05-23 | 2016-08-03 | 西安西热水务环保有限公司 | Thermal power plant terminal waste water salt separating and crystallizing system |
| CN107055885A (en) * | 2017-05-26 | 2017-08-18 | 西安热工研究院有限公司 | A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system and method for work |
| CN109095732A (en) * | 2018-10-30 | 2018-12-28 | 华北电力大学（保定） | A kind of technique based on magnesium processes desulfurization wastewater high-purity magnesium hydroxide |
| CN109095731A (en) * | 2018-10-30 | 2018-12-28 | 华北电力大学（保定） | A kind of system based on magnesium processes desulfurization wastewater high-purity magnesium hydroxide |
| CN110078249A (en) * | 2018-01-25 | 2019-08-02 | 宝山钢铁股份有限公司 | Remove the deep treatment method and system of COD and total iron in power plant desulfurization wastewater |
-
2017
- 2017-05-26 CN CN201720605647.6U patent/CN206799333U/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105819608A (en) * | 2016-05-23 | 2016-08-03 | 西安西热水务环保有限公司 | Thermal power plant terminal waste water salt separating and crystallizing system |
| CN107055885A (en) * | 2017-05-26 | 2017-08-18 | 西安热工研究院有限公司 | A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system and method for work |
| CN107055885B (en) * | 2017-05-26 | 2023-04-25 | 西安热工研究院有限公司 | Desulfurization wastewater recycling system of coal-fired power plant and working method |
| CN110078249A (en) * | 2018-01-25 | 2019-08-02 | 宝山钢铁股份有限公司 | Remove the deep treatment method and system of COD and total iron in power plant desulfurization wastewater |
| CN110078249B (en) * | 2018-01-25 | 2022-03-18 | 宝山钢铁股份有限公司 | Advanced treatment method and system for removing COD (chemical oxygen demand) and total iron in desulfurization wastewater of power plant |
| CN109095732A (en) * | 2018-10-30 | 2018-12-28 | 华北电力大学（保定） | A kind of technique based on magnesium processes desulfurization wastewater high-purity magnesium hydroxide |
| CN109095731A (en) * | 2018-10-30 | 2018-12-28 | 华北电力大学（保定） | A kind of system based on magnesium processes desulfurization wastewater high-purity magnesium hydroxide |
| CN109095732B (en) * | 2018-10-30 | 2021-10-29 | 华北电力大学（保定） | Process for preparing high-purity magnesium hydroxide based on magnesium-method desulfurization wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206799333U (en) | A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system | |
| WO2017148229A1 (en) | Low-sludge-production desulfurization wastewater treatment apparatus and method | |
| WO2017133513A1 (en) | Treatment apparatus and method for softening desulfurization wastewater | |
| CN105060545B (en) | A kind of system and method for sofening treatment Desulphurization for Coal-fired Power Plant waste water | |
| CN105174580A (en) | Desulphurization waste-water zero discharge processing system and technology | |
| CN107055885A (en) | A kind of Desulphurization for Coal-fired Power Plant waste water reclaiming system and method for work | |
| CN105800846A (en) | Method used for reverse osmosis concentrated water treatment and zero discharge, and apparatus thereof | |
| CN108017213A (en) | A kind of high slat-containing wastewater recycling treatment system and technique | |
| CN106746059B (en) | Terminal high salt wastewater treatment system of economical coal fired power plant | |
| CN107176726A (en) | Desulphurization for Coal-fired Power Plant waste water integrates defluorination method | |
| CN105523666A (en) | Strengthened pretreatment system for high-salt-content industrial wastewater and production process of strengthened pretreatment system | |
| CN105984992A (en) | Paint wastewater treatment method | |
| CN109437480A (en) | A kind of viscose fiber wastewater treatment process | |
| CN105858981A (en) | Quality-divided reclamation treatment device and process for strong brine | |
| CN103011462B (en) | Device and method for treating waste residues of circulating make-up water by reutilizing lime softening method of power plant | |
| CN205442916U (en) | Contain salt effluent disposal system | |
| CN206666295U (en) | A kind of economical coal-burning power plant end high-salt wastewater processing system | |
| CN107445382B (en) | Coal industry waste water crystallization salt resourceful system | |
| CN105621775A (en) | Novel desulfurated wastewater zero-emission treatment device and method | |
| CN113264605A (en) | Desulfurization wastewater anti-scaling pretreatment method and system | |
| CN103304072B (en) | Recycling method of industrial waste water | |
| CN106830440A (en) | A kind of thermal power plant's high-salt wastewater dish tubular membrane concentrating and treating system and method | |
| CN207121501U (en) | A kind of hardness removing device suitable for the hard waste water of high magnesium | |
| CN206901925U (en) | The device of novel desulphurization wastewater treatment | |
| CN207537309U (en) | IGCC plant coal gasification and sulfur-bearing composite waste treatment for reuse Zero discharging system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant |