CN205528048U - Minimum discharge wet -type electric precipitation waste water concentrate processing system - Google Patents
Minimum discharge wet -type electric precipitation waste water concentrate processing system Download PDFInfo
- Publication number
- CN205528048U CN205528048U CN201620100769.5U CN201620100769U CN205528048U CN 205528048 U CN205528048 U CN 205528048U CN 201620100769 U CN201620100769 U CN 201620100769U CN 205528048 U CN205528048 U CN 205528048U
- Authority
- CN
- China
- Prior art keywords
- waste water
- desulfurization
- desulfurization wastewater
- wet
- pump
- 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
Abstract
The utility model relates to a minimum discharge wet -type electric precipitation waste water concentrate processing system, including wet electric efficient clarifier, sludge pump and desulfurization wastewater disposal basin, the waste water concentrate of wet electric efficient clarifier lower part is connected to the desulfurization wastewater disposal basin through the sludge pump, wet electric efficient clarifier upper portion overflow is connected to the water inlet of defroster water tank, the delivery port of defroster water tank is connected to the defroster on desulfurization absorption tower through the defroster water pump, the gypsum excavating pump on desulfurization absorption tower is connected to the desulfurization wastewater disposal basin through desulfurization waste water whirl station, the desulfurization wastewater disposal basin connects gradually three headers of desulfurization waste water and desulfurization waste water clarifier. The beneficial effects of the utility model are that: 1, stability is good, and the security is high, 2, prevent that desulfurization absorption tower liquid level is too high, 3, process flow is simple, and the investment is with low costs with the fortune dimension.
Description
Technical field
This utility model patent relates to Waste water concentrating liquid treating system, particularly relates to a kind of minimum discharge wet-esp Waste water concentrating liquid treating system.
Background technology
At present, for meeting tightened up environmental requirement, many coal-burning power plants implement minimum discharge improvement project, set up Wet-type electric dust removal system (the wettest electricity).Wet electricity needs a large amount of flushing waters, after this partial flushing water washes away pole plate, flows out from ash bucket, and part recycles, and part is outer to be lined up as wet electricity waste water.Wet electricity waste water is delivered to wet electricity high-efficiency clarifier by draining pump and is recycled.Top clear water after clarification by tube overflow to mist eliminator flushing water tank, and through mist eliminator flushing water pump deliver to desulfuration absorbing tower for absorption tower demisting device clean, bottom clarification concentrated solution deliver to desulfuration absorbing tower stock tank for absorption tower moisturizing through sludge pump.Bottom clarification concentrated solution contains more fine dust particles, if for absorption tower moisturizing, certainly will impact the reaction of desulfurizing agent in absorption tower, easily blocks filter cloth simultaneously, increases the burden of vacuum belt machine, affect desulphurization system safe operation.Meanwhile, desulfuration absorbing tower water balance, to desulfuration absorbing tower, was caused HD by the extra waste water that increases.
Utility model content
The purpose of this utility model is to overcome prior art not enough, it is provided that a kind of rational in infrastructure, reduces the Waste water concentrating liquid impact on desulphurization system of wet electricity, it is ensured that the wet electricity Waste water concentrating liquid treating system of system safety operation.
For achieving the above object, this utility model have employed techniques below scheme:
Minimum discharge wet-esp Waste water concentrating liquid treating system, including wet electricity high-efficiency clarifier, sludge pump and desulfurization wastewater pond, the Waste water concentrating liquid of wet electricity high-efficiency clarifier bottom is connected to desulfurization wastewater pond by sludge pump, the high-efficiency clarifier top overflow of wet electricity is connected to the water inlet of demister water tank, the outlet of demister water tank is connected to the demister of desulfuration absorbing tower by demister water pump, the Gypsum Fibrosum excavationg pump of desulfuration absorbing tower is connected to desulfurization wastewater pond by desulfurization wastewater rotational flow station, and desulfurization wastewater pond is sequentially connected with desulfurization wastewater three header and desulfurization wastewater defecator.
The beneficial effects of the utility model are:
1, good stability, safety is high: wet electricity Waste water concentrating liquid is fed directly to desulfurization wastewater treatment system, reduces the impact of the reaction of desulfurizing agent in absorption tower, prevents the fine particle blocking to filter cloth in concentrated solution simultaneously, reduce the burden of vacuum belt machine, improve the safety that system is run.
2, preventing desulfuration absorbing tower liquid level too high: after minimum discharge transformation, because of setting up low temp. electric dedusting, cigarette temperature drop is low causes absorption tower evaporation capacity minimizing, and absorption tower water liquid level easily causes too high and overflow.Wet electricity Waste water concentrating liquid is directly outer drains into desulfurization wastewater treatment system, reduces absorbing tower liquid-level excess pressure.
3, technological process is simple, and investment and O&M cost are low: this programme increase only sludge pump and the connecting line of desulfurization wastewater treatment system and related valve etc., and system process is simple.System capital equipment, material are conventional products, it is easy to buying, cost of investment is low.Pipeline is simple, this system can be included in desulphurization system unified management and safeguard, O&M cost is low.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation;
Description of reference numerals: wet electricity high-efficiency clarifier 1, sludge pump 2, desulfurization wastewater pond 3, desulfurization wastewater three header 4, desulfurization wastewater defecator 5, desulfuration absorbing tower 6, desulfurization wastewater rotational flow station 7, demister water tank 8, demister water pump 9.
Detailed description of the invention
Below in conjunction with embodiment, this utility model is described further.The explanation of following embodiment is only intended to help and understands this utility model.Should be understood that; for those skilled in the art; on the premise of without departing from this utility model principle, it is also possible to this utility model is carried out some improvement and modification, these improve and modification also falls in this utility model scope of the claims.
As shown in Figure 1, the minimum discharge wet-esp Waste water concentrating liquid treating system of the present embodiment, including wet electricity high-efficiency clarifier 1, sludge pump 2 and desulfurization wastewater pond 3, the Waste water concentrating liquid of wet electricity high-efficiency clarifier 1 bottom is connected to desulfurization wastewater pond 3 by sludge pump 2, the high-efficiency clarifier 1 top overflow of wet electricity is connected to the water inlet of demister water tank 8, the outlet of demister water tank 8 is connected to the demister of desulfuration absorbing tower 6 by demister water pump 9, the Gypsum Fibrosum excavationg pump of desulfuration absorbing tower 6 is connected to desulfurization wastewater pond 3 by desulfurization wastewater rotational flow station 7, desulfurization wastewater pond 3 is sequentially connected with desulfurization wastewater three header 4 and desulfurization wastewater defecator 5.
Wet electricity Waste water concentrating liquid treating system of the present utility model, the bottom Waste water concentrating liquid of wet electricity high-efficiency clarifier 1 delivers to desulfurization wastewater pond 3 by sludge pump 2, the waste water discharged with desulfuration absorbing tower 6 mixes, outer row is processed through desulfurization wastewater three header 4, desulfurization wastewater defecator 5, thus reduce the impact on desulphurization system of the Waste water concentrating liquid, it is ensured that system safety operation.
Claims (1)
1. a minimum discharge wet-esp Waste water concentrating liquid treating system, it is characterised in that: include wet electricity high-efficiency clarifier
(1), sludge pump (2) and desulfurization wastewater pond (3), the Waste water concentrating liquid of wet electricity high-efficiency clarifier (1) bottom passes through sludge pump
(2) being connected to desulfurization wastewater pond (3), high-efficiency clarifier (1) the top overflow of wet electricity is connected to the water inlet of demister water tank (8)
Mouthful, the outlet of demister water tank (8) is connected to the demister of desulfuration absorbing tower (6), desulfurization by demister water pump (9)
The Gypsum Fibrosum excavationg pump on absorption tower (6) is connected to desulfurization wastewater pond (3), desulfurization wastewater pond (3) by desulfurization wastewater rotational flow station (7)
It is sequentially connected with desulfurization wastewater three header (4) and desulfurization wastewater defecator (5).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620100769.5U CN205528048U (en) | 2016-02-01 | 2016-02-01 | Minimum discharge wet -type electric precipitation waste water concentrate processing system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620100769.5U CN205528048U (en) | 2016-02-01 | 2016-02-01 | Minimum discharge wet -type electric precipitation waste water concentrate processing system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205528048U true CN205528048U (en) | 2016-08-31 |
Family
ID=56775120
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620100769.5U Active CN205528048U (en) | 2016-02-01 | 2016-02-01 | Minimum discharge wet -type electric precipitation waste water concentrate processing system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205528048U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105540898A (en) * | 2016-02-01 | 2016-05-04 | 浙江天地环保工程有限公司 | Ultra-low drainage wet type electric dedusting wastewater concentrated liquid treatment system |
-
2016
- 2016-02-01 CN CN201620100769.5U patent/CN205528048U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105540898A (en) * | 2016-02-01 | 2016-05-04 | 浙江天地环保工程有限公司 | Ultra-low drainage wet type electric dedusting wastewater concentrated liquid treatment system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN207628209U (en) | A kind of desulfurization slurry Recovery Purifying utilizes system | |
CN105776706A (en) | Device and method for treating desulfurized waste water through flue multi-level evaporation | |
CN101816882A (en) | The lime method mine water is handled useless underflow as wet desulphurization absorbent | |
CN209567937U (en) | High saliferous desulfurizing waste water processing device | |
CN111320315A (en) | Desulfurization wastewater treatment system | |
CN202398279U (en) | Desulfuration equipment for boiler of power plant | |
CN104086011B (en) | Be applicable to the technique of zero discharge of viscose fibre industry acid station waste water | |
CN205528048U (en) | Minimum discharge wet -type electric precipitation waste water concentrate processing system | |
CN102049168A (en) | Equipment for flue gas desulfurization by use of industrial wastewater | |
CN202962208U (en) | High-temperature selenium-containing flue gas treatment device | |
CN102974188B (en) | Method for processing high temperature selenium-containing flue gas | |
CN102527219A (en) | Smoke gas wet method sulfur removal and dust removal integral treatment system | |
CN207877490U (en) | A kind of thermal power plant desulfurization wastewater zero-discharge treatment system | |
CN205803170U (en) | A kind of Waste Water Treatment in coal | |
CN206652332U (en) | A kind of cooperation-removal PM2.5 and mercuric wastewater zero discharge desulphurization system | |
CN208757290U (en) | The supply equipment of demister in desulphurization system, desulphurization system | |
CN211734054U (en) | Desulfurization waste water is used for high-efficient water treatment system that defroster washed | |
CN104118954B (en) | A kind of method and device utilizing Chemical Mixed Fertilizer off gas treatment waste water | |
CN208995263U (en) | A kind of processing unit of Desulphurization for Coal-fired Power Plant waste water reuse | |
CN209456210U (en) | One kind is for the personal reasonable reclaiming system of water of Boiler water Feeding System | |
CN203545862U (en) | Chemical phosphorus removal and precipitation separation device for sludge | |
CN108905587A (en) | The method of supplying water and supply equipment of demister in desulphurization system, desulphurization system | |
CN206463770U (en) | A kind of power plant desulfurization wastewater recovery and processing system | |
CN205892947U (en) | Coal water treatment electricity flocculation system | |
CN206138864U (en) | Coal mine sewage treatment device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder |
Address after: Hangzhou City, Zhejiang province 310012 Huaxing Road No. 99 (Hangzhou Neusoft business building) Patentee after: Zhejiang Tiandi Environmental Protection Technology Co., Ltd Address before: Hangzhou City, Zhejiang province 310012 Huaxing Road No. 99 (Hangzhou Neusoft business building) Patentee before: ZHEJIANG TIANDI ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
|
CP01 | Change in the name or title of a patent holder |