CN205974125U - Desulfurization waste water zero release processing system - Google Patents
Desulfurization waste water zero release processing system Download PDFInfo
- Publication number
- CN205974125U CN205974125U CN201620467366.4U CN201620467366U CN205974125U CN 205974125 U CN205974125 U CN 205974125U CN 201620467366 U CN201620467366 U CN 201620467366U CN 205974125 U CN205974125 U CN 205974125U
- Authority
- CN
- China
- Prior art keywords
- coal
- desulfurization wastewater
- thermal power
- waste water
- 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.)
- Expired - Fee Related
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a desulfurization waste water zero release processing system for coal -fired thermal power field, its characterized in that: including desulfurization waste water baffle -box (1), desulfurization waste water baffle -box (1) is used for collecting the desulfurization waste water that coal -fired thermal power produced, and its exit end has connected gradually desulfurization waste water pump (2), has softened coagulation and clarification and has filtered integration treatment device (3), middle water tank (4), middle water pump (5), degree of depth softening installation (6), membrane concentration device (7), concentrating spent liquor pond (8), concentrated waste liquid pump (9), water distribution device (10), water distribution device (10) arrange in coal -fired thermal power's dust remover (11) and/or sediment storehouse (12) top of coal -fired thermal power. The utility model discloses waste control by waste's process systems is adopted in capital construction and operation cheap cost, with desulfurization waste water soften with the membrane concentration after for ash removal system and deslagging system absorb, realize the zero release of desulfurization waste water.
Description
Technical field
This utility model is related to Industrial Wastewater Treatment and resource circulation utilization technology, more particularly, to a kind of desulfurization wastewater zero-emission
Put processing system, for coal-fired field of thermal power.
Background technology
China's coal-electricity base resource concentrations, mainly concentrate Siklingelei, Erdos, Jin Bei, Jinzhong City, Jin Dong, Shan
North, Hami, accurate eastern, peaceful north-east area, and be in contrary distribution with water resource.Especially northern area water resource is more poor.
Shanxi, Gansu, the water resources quantity in Ningxia 3 province (autonomous region) only account for the 7.5% of northern water resources quantity, and natural resources of groundwater amount is only
Account for the 8.9% of northern natural resources of groundwater amount.This 3 provinces (autonomous region) and Shaanxi about, the Inner Mongol and Xinjiang are autonomous
Area, annual rainfall, how in below 500mm, also has some areas less than 250mm, the sunshine-duration is long in addition, and evaporation capacity is big, water resource
Very poor.Therefore, in northern area Development of Power Plant, being generated electricity using air cooling has significant conservation benefits.
In order to prevent natively very fragile ecological environment from deteriorating further it is necessary to waste water should be realized in air cooling power plant
Zero-emission.According to the Northwest 22 coal-burning power plant's engineering sounding example, the weight of current air cooling power-plant waste zero-emission
Point is the zero-emission of desulfurization wastewater.Desulfurization wastewater is processed using pretreatment-embrane method or electrodialysis concentration-evaporative crystallization technique,
Technically feasible, but economy is poor, and capital construction and operating cost are higher.
Utility model content
Technical problem to be solved in the utility model is, the capital construction existing for existing method for treating desulfurized wastewater and
The higher problem of operating cost, provides a kind of desulfurization wastewater zero-discharge treatment system, its capital construction and running cost low cost, comprehensive effect
Benefit is high.
In order to reach solution above-mentioned technical problem, this utility model employs the following technical solutions and is achieved.
A kind of desulfurization wastewater zero-discharge treatment system, for coal-fired field of thermal power it is characterised in that：Including desulfurization
Waste water baffle-box, described desulfurization wastewater baffle-box is used for collecting the desulfurization wastewater that coal-fired thermal power generation produces, and its port of export is successively
It is connected with desulfurization wastewater pump, soften coagulation clarification filtering integral processing meanss, intermediate water tank, middle water pump, depth softening dress
Put, film condensing device, concentrating spent liquor pond, thickened waste liquid pump, water-distributing device；Described water-distributing device is arranged in coal-fired firepower and sends out
The slag silo roof portion of the interior and/or coal-fired thermal power generation of the cleaner unit of electricity.
Preferably, described softening coagulation clarification filtering integral processing meanss be with Calx-soda soften medicine charging function,
The integrated treatment unit of coagulant medicine charging function, coagulation clarification function and ceramic filter function.
Preferably, described depth softening plant is Weak Acid Ion exchanger, strong acid ion exchanger or nanofiltration device.
When this utility model uses, desulfurization wastewater softens through softening coagulation clarification filtering integral processing meanss and depth
After device carries out sofening treatment, thoroughly eliminate the heavy metal in water and fouling tendency ion, after water outlet concentrates through film condensing device,
The water yield substantially reduces, and only designs the 1/3-1/5 of the water yield.Desulfurization wastewater after concentration is arranged in cleaner unit and/or slag storehouse
The water-distributing device at top sprays, and is respectively used to ash disposal system and slag removing system, and a part is entered ash disposal system by smoke evaporative, salinity
System, another part is mixed wet consumption by slag removing system evaporation.
The beneficial effects of the utility model are：
(1) adopt the technique of the treatment of wastes with processes of wastes against one another it is achieved that the zero-emission of desulfurization wastewater.
(2) desulfurization wastewater after softening avoids scaling in subsequent technique.
(3) the traditional desulfurization wastewater Zero-discharge treating process of ratio, capital construction and operating cost reduce 60-80%, economic benefit
Significantly.
Brief description
Fig. 1 is structural representation of the present utility model；
Wherein, 1- desulfurization wastewater baffle-box, 2- desulfurization wastewater pump, 3- softens coagulation clarification filtering integral processing meanss,
4- intermediate water tank, 5- middle water pump, 6- depth softening plant, 7- film condensing device, 8- waste liquid concentrates pond, 9- concentrating spent liquor
Pump, 10- water-distributing device, 12- cleaner unit, 13- slag storehouse.
Specific embodiment
As shown in figure 1, being a kind of preferred embodiment of desulfurization wastewater zero discharge treatment device of the present utility model, it is used for
Coal-fired field of thermal power, specifically includes desulfurization wastewater baffle-box (1), and described desulfurization wastewater baffle-box (1) is used for collecting fire coal
The desulfurization wastewater that thermal power generation produces, its port of export is connected with desulfurization wastewater pump (2) in turn, softens coagulation clarification filtering integral
Processing meanss (3), intermediate water tank (4), middle water pump (5), depth softening plant (6), film condensing device (7), concentrating spent liquor water
Pond (8), thickened waste liquid pump (9), water-distributing device (10).Wherein water-distributing device (10) is arranged in the cleaner unit of coal-fired thermal power generation
(11) slag storehouse (12) top with coal-fired thermal power generation in.
Wherein, from the desulfurization wastewater of the gypsum dehydration separator outlet exclusion of the desulphurization system of coal-fired thermal power generation, enter
Desulfurization wastewater baffle-box (1), after desulfurization wastewater pump (2) pressurization, enters and softens coagulation clarification filtering integral processing meanss
(3), after one-level sofening treatment, most heavy metal ion and hardness ions are removed.Soften coagulation clarification and filter one
Body processing meanss (3) water outlet enters intermediate water tank (4), after middle water pump (5) pressurization, enters depth softening plant (6) and enters
Row secondary softening is processed, and removes remaining heavy metal ion and residual harness.Wherein, depth softening plant (6) adopts ion to hand over
Change softening bed.
Ion exchange softening bed water outlet enters film condensing device (7) and is concentrated, and the waste water after concentration enters concentrating spent liquor
Pond (8), is concentrated waste drains pump (9) circulation and squeezes into water-distributing device (10).A small amount of desulfurization wastewater after concentration is through water-distributing device
(10) it is sprayed in cleaner unit (11) and slag storehouse (12) top, a part is entered ash disposal system, another portion by smoke evaporative, salinity
Divide and wet consumption is mixed by slag removing system evaporation.
This utility model is described further below taking the treatment for reuse of certain power plant desulfurization waste water as a example.
Certain power plant desulfurization waste water quality is as shown in table 1.
Desulfurization wastewater, about 14t/h, after softened coagulation clarification filtering integral processing meanss (3) one-level sofening treatment, greatly
Part hardness is removed, and residual harness is about 40mg/L, then carries out depth sofening treatment, hardness through depth softening plant (6)
It is about 0-1mg/L.Produce water and enter film condensing device (7), be further concentrated, the response rate controls about 80%, and the water yield is about 2-
3t/h.
This utility model is softened using depth and the desulfurization wastewater of membrance concentration is concentrated, and concentrates waste water and is used for ash disposal or removes
Slag system.Using the handling process of the treatment of wastes with processes of wastes against one another, capital construction and operating cost are cheap, and economical realizes desulfurization wastewater zero-emission.
Claims (3)
1. a kind of desulfurization wastewater zero-discharge treatment system, for coal-fired field of thermal power it is characterised in that：Including desulfurization wastewater
Baffle-box (1), described desulfurization wastewater baffle-box (1) is used for collecting the desulfurization wastewater that coal-fired thermal power generation produces, its port of export according to
Secondary be connected with desulfurization wastewater pump (2), soften coagulation clarification filtering integral processing meanss (3), intermediate water tank (4), middle water pump
(5), depth softening plant (6), film condensing device (7), concentrating spent liquor pond (8), thickened waste liquid pump (9), water-distributing device (10)；
Described water-distributing device (10) is arranged in the slag storehouse of the interior and/or coal-fired thermal power generation of cleaner unit (11) of coal-fired thermal power generation
(12) top.
2. desulfurization wastewater zero-discharge treatment system according to claim 1 it is characterised in that：Described softening coagulation clarification mistake
Filter integrated treatment unit (3) be with Calx-soda soften medicine charging function, coagulant medicine charging function, coagulation clarification function with
And the integrated treatment unit of ceramic filter function.
3. desulfurization wastewater zero-discharge treatment system according to claim 1 it is characterised in that：Described depth softening plant
For Weak Acid Ion exchanger, strong acid ion exchanger or nanofiltration device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620467366.4U CN205974125U (en) | 2016-05-20 | 2016-05-20 | Desulfurization waste water zero release processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620467366.4U CN205974125U (en) | 2016-05-20 | 2016-05-20 | Desulfurization waste water zero release processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205974125U true CN205974125U (en) | 2017-02-22 |
Family
ID=58019655
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620467366.4U Expired - Fee Related CN205974125U (en) | 2016-05-20 | 2016-05-20 | Desulfurization waste water zero release processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205974125U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11855324B1 (en) | 2022-11-15 | 2023-12-26 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell with heat pump |
| US12040517B2 (en) | 2022-11-15 | 2024-07-16 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell and methods of use thereof |
-
2016
- 2016-05-20 CN CN201620467366.4U patent/CN205974125U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11563229B1 (en) | 2022-05-09 | 2023-01-24 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11611099B1 (en) | 2022-05-09 | 2023-03-21 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11699803B1 (en) | 2022-05-09 | 2023-07-11 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US12107308B2 (en) | 2022-05-09 | 2024-10-01 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11855324B1 (en) | 2022-11-15 | 2023-12-26 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell with heat pump |
| US12040517B2 (en) | 2022-11-15 | 2024-07-16 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell and methods of use thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205974125U (en) | Desulfurization waste water zero release processing system | |
| CN208414114U (en) | A kind of desulfurization wastewater zero-discharge treatment system | |
| WO2017133514A1 (en) | Treatment apparatus and method for softening desulfurization wastewater | |
| CN206069429U (en) | A kind of concentration tower of desulfurization wastewater decrement concentration | |
| CN105174584A (en) | Zero discharging processing device of desulfurization waste water | |
| CN101417826A (en) | Method and system for processing desulphurization waste water | |
| CN107857321B (en) | Process for zero discharge treatment of wastewater of thermal power plant | |
| CN206940653U (en) | Desulphurization for Coal-fired Power Plant waste water zero discharge device | |
| CN102010082B (en) | Treatment method for recycling waste dilute sulfuric acid | |
| CN211497236U (en) | Novel processing system of thermal power factory desulfurization waste water | |
| CN111423046A (en) | Power plant desulfurization wastewater advanced treatment and resource utilization system and method | |
| CN100376472C (en) | Method for utilizing low-concentration waste sulfuric acid through multi-effect concentration and flash evaporation | |
| CN206204082U (en) | Wet desulphurization wastewater zero discharge and resource recovering system | |
| CN210786877U (en) | Flue gas waste heat evaporation crystallization zero discharge system | |
| CN205635216U (en) | Concentrated processing apparatus of desulfurization waste water | |
| CN216236502U (en) | Landfill leachate treatment system | |
| CN212403826U (en) | Desulfurization waste water advanced treatment of power plant and utilization system | |
| CN206457365U (en) | Flue gas desulfurization waste-water is classified dual treatment system | |
| CN209974511U (en) | Desulfurization water zero release comprehensive utilization device | |
| CN109850996A (en) | A kind of processing method of power plant desulfurization wastewater | |
| CN204958640U (en) | Desulfurization waste water zero release processing apparatus | |
| CN211445352U (en) | Coal fired power plant desulfurization waste water resourceful treatment system | |
| CN207537295U (en) | A kind of high-salt wastewater treatment process system | |
| CN210559894U (en) | Zero release and resource utilization system of whole factory of power plant waste water | |
| CN110436713A (en) | A kind of processing method of rotary kiln deacidifying flue gas waste liquid |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170222 Termination date: 20180520 |