CN203976588U - Integrated small painting wastewater is processed complete process structure - Google Patents
Integrated small painting wastewater is processed complete process structure Download PDFInfo
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- CN203976588U CN203976588U CN201420384637.0U CN201420384637U CN203976588U CN 203976588 U CN203976588 U CN 203976588U CN 201420384637 U CN201420384637 U CN 201420384637U CN 203976588 U CN203976588 U CN 203976588U
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Integrated small painting wastewater is processed complete process structure, it relates to technical field of sewage, grid is connected with equalizing tank, equalizing tank is connected with air supporting settling tank, air supporting settling tank is adjusted pond with PH and is connected, PH adjusts pond and is connected with electrolyzer, electrolyzer is connected with intermediate pool, intermediate pool is connected with UASB anaerobic reation pool, UASB anaerobic reation pool is connected with Aerobic Pond by pipeline, Aerobic Pond is connected with coagulation basin by pipeline, coagulation basin is connected with flocculation basin by pipeline, flocculation basin is connected with settling tank by pipeline, settling tank is connected with clean water basin by pipeline, clean water basin are connected with filtering system by pipeline, sludge thickener is connected with pressure filter by pipeline, sludge thickener is connected with equalizing tank by pipeline.It adopts all steel structure, and rational deployment, makes full use of space, has easy construction, simple to operate, and building is compact attractive in appearance.
Description
Technical field:
The utility model relates to technical field of sewage, is specifically related to integrated small painting wastewater and processes complete process structure.
Background technology:
The existing little water yield (being less than 200m3/d) painting wastewater is processed engineering and is substantially continued to use traditional technology and related facility equipment, and technique is advanced not, and facility is too huge, utilization ratio is low, and equipment overflows, and directly causes the wasting of resources and enterprise cost to increase.And wastewater treatment efficiency is difficult for stablely, integral layout is subject to larger restriction to such an extent as to the architectural effect that is difficult to reach attractive in appearance etc.
Utility model content:
The purpose of this utility model is to provide integrated small painting wastewater and processes complete process structure, and it adopts all steel structure, and rational deployment, makes full use of space, has easy construction, simple to operate, and building is compact attractive in appearance.
In order to solve the existing problem of background technology, the utility model is by the following technical solutions: it comprises grid, equalizing tank, air supporting settling tank, PH adjusts pond, electrolyzer, intermediate pool, UASB anaerobic reation pool, Aerobic Pond, coagulation basin, flocculation basin, settling tank, clean water basin, filtering system, sludge thickener, pressure filter, grid is connected with equalizing tank by pipeline, equalizing tank is connected with air supporting settling tank by pipeline, air supporting settling tank is adjusted pond by pipeline with PH and is connected, PH adjusts pond and is connected with electrolyzer by pipeline, electrolyzer is connected with intermediate pool by pipeline, intermediate pool is connected with UASB anaerobic reation pool by pipeline, UASB anaerobic reation pool is connected with Aerobic Pond by pipeline, Aerobic Pond is connected with coagulation basin by pipeline, coagulation basin is connected with flocculation basin by pipeline, and flocculation basin is connected with settling tank by pipeline, and settling tank is connected with clean water basin by pipeline, clean water basin are connected with filtering system by pipeline, described air supporting settling tank, UASB anaerobic reation pool is connected with sludge thickener by pipeline with settling tank, and sludge thickener is connected with pressure filter by pipeline, and sludge thickener is connected with equalizing tank by pipeline.
Total of the present utility model adopts joist steel, square steel and channel-section steel setting support, firmly sturdy; Each system adopts all steel plate system to build, rational deployment, and seamless connection, space utilization maximizes; Be aided with stainless steel tube and pvc pipe, saved anticorrosion input; Surface of steel plate adopts angle steel reinforced, material-saving attractive in appearance; Between steel material, adopt full weld mode, inside and outsidely all weld, prevent from leaking; Pipeline tapping place that connects each system is used sealing material sealing.
Principle of work of the present utility model:
One, waste water is removed suspended substance through grid and is entered equalizing tank, after stopping aeration, smoke by submersible pump, one segment pipe mixing tank is set in submersible pump pipeline, waste water reacts with the PAC coagulating agent of access at this, after entering air flotation pool reaction zone, react with PAM flocculation agent again, simultaneously in pond, separate scum silica frost and mud by aeration, scum silica frost is scraped to deslagging weir and is entered Residue extraction pipeline by air flotation pool top slag scraper, mud by pond at the bottom of shore pipe take away.
Two, water body flows to clear water in the process of the air supporting settling tank the other end and comes together in body middle part, pond, enters and adjusts pond from air flotation pool opposite side middle part water shoot.Waste water passes through acid, alkali medicament regulating water quality pH value in adjustment pond, flowing to fully reaction in intermediate pool process, by the submersible pump suction bypass channel in intermediate pool.
Three, bypass channel bottom even distribution pore, connects water distributor water distribution uniformity at the bottom of UASB anaerobic reation pool.Waste water fully contacts digestion with the anerobe in active sludge in UASB anaerobic reation pool, removes the organism in waste water, mud-water separation in uphill process, and sludge settling, unnecessary mud is taken away by pool bottom sludge pipe; Clear water overflows into surrounding effluent weir, flows into Aerobic Pond bottom by water pipe.
Four, in Aerobic Pond, be covered with filler, aeration at the bottom of pond, allows active sludge carry out aerobic repiration, further organic substance decomposing is become to inorganics.Waste water to Aerobic Pond the other end top, flows into PAC reaction tank and coagulating agent contact reacts by water surface posticum by filler stream, and then at the bottom of pond, water hole enters PAM reaction tank and flocculation agent contact reacts.
Five, the waste water of confection flows into settling tank bottom, is covered with inclined tube and assists sludge settling in pond.Mud, by pond bottom pipeline suction sludge sump, overflows into effluent weir by the clear water of inclined tube and flows into clean water basin.Now in clean water basin, water quality is up to standard, meets emission standard or reuse condition.
Six, scum silica frost and mud in air supporting settling tank, the whole suction sludge sumps of mud in UASB anaerobic reation pool and settling tank, further, after sedimentation, press mud machine by the pipeline suction at the bottom of sludge sump, are filtered dry mud, and filtrate is back to equalizing tank, and mud cake outward transport is processed.
The utlity model has following beneficial effect:
1, design technology is more advanced, scientific and reasonable;
2, system operates steadily, and water outlet continues up to standard;
3, building cost is cheap, and difficulty of construction is little, and building materials utilization ratio is high;
4, stainless steel integral structure, compact attractive in appearance, save anticorrosion expense;
5, whole project occupation of land area is little, and space availability ratio is high, and manual operation is easy.
Brief description of the drawings:
Fig. 1 is structural representation of the present utility model.
Embodiment:
Referring to Fig. 1, this embodiment is by the following technical solutions: it comprises grid 1, equalizing tank 2, air supporting settling tank 3, PH adjusts pond 4, electrolyzer 5, intermediate pool 6, UASB anaerobic reation pool 7, Aerobic Pond 8, coagulation basin 9, flocculation basin 10, settling tank 11, clean water basin 12, filtering system 13, sludge thickener 14, pressure filter 15, grid 1 is connected with equalizing tank 2 by pipeline, equalizing tank 2 is connected with air supporting settling tank 3 by pipeline, air supporting settling tank 3 is adjusted pond 4 by pipeline with PH and is connected, PH adjusts pond 4 and is connected with electrolyzer 5 by pipeline, electrolyzer 5 is connected with intermediate pool 6 by pipeline, intermediate pool 6 is connected with UASB anaerobic reation pool 7 by pipeline, UASB anaerobic reation pool 7 is connected with Aerobic Pond 8 by pipeline, Aerobic Pond 8 is connected with coagulation basin 9 by pipeline, coagulation basin 9 is connected with flocculation basin 10 by pipeline, and flocculation basin 10 is connected with settling tank 11 by pipeline, and settling tank 11 is connected with clean water basin 12 by pipeline, clean water basin 12 are connected with filtering system 13 by pipeline, described air supporting settling tank 3, UASB anaerobic reation pool 7 is connected by concentrated 14 ponds of pipeline and mud with settling tank 11, and sludge thickener 14 is connected with pressure filter 15 by pipeline, and sludge thickener 14 is connected with equalizing tank 2 by pipeline.
The principle of work of this embodiment is as follows:
One, waste water is removed suspended substance through grid 1 and is entered equalizing tank 2, after stopping aeration, smoke by submersible pump, one segment pipe mixing tank is set in submersible pump pipeline, waste water reacts with the PAC coagulating agent of access at this, after entering air supporting settling tank 3 reaction zones, react with PAM flocculation agent again, simultaneously in pond, separate scum silica frost and mud by aeration, scum silica frost is scraped to deslagging weir and is entered Residue extraction pipeline by air flotation pool top slag scraper, mud by pond at the bottom of shore pipe take away.
Two, water body flows to clear water in the process of the air flotation pool the other end and comes together in body middle part, pond, enters and adjusts pond from air flotation pool opposite side middle part water shoot.Waste water is adjusted in pond 4 by acid, alkali medicament regulating water quality pH value, flowing to fully reaction in intermediate pool 6 processes, by the submersible pump suction bypass channel in intermediate pool 6 at PH.
Three, bypass channel bottom even distribution pore, connects water distributor at 7 end of UASB anaerobic reation pool water distribution uniformity.Waste water fully contacts digestion with the anerobe in active sludge in UASB anaerobic reation pool 7, removes the organism in waste water, mud-water separation in uphill process, and sludge settling, unnecessary mud is taken away by pool bottom sludge pipe; Clear water overflows into surrounding effluent weir, flows into Aerobic Pond bottom by water pipe.
Four, in Aerobic Pond 8, be covered with filler, aeration at the bottom of pond, allows active sludge carry out aerobic repiration, further organic substance decomposing is become to inorganics.Waste water to Aerobic Pond the other end top, flows into PAC reaction tank and coagulating agent contact reacts by water surface posticum by filler stream, and then at the bottom of pond, water hole enters PAM reaction tank and flocculation agent contact reacts.
Five, the waste water of confection flows into settling tank bottom, is covered with inclined tube and assists sludge settling in pond.Mud, by pond bottom pipeline suction sludge sump, overflows into effluent weir by the clear water of inclined tube and flows into clean water basin.Now in clean water basin, water quality is up to standard, meets emission standard or reuse condition.
Six, scum silica frost and mud in air supporting settling tank 3, the whole suction sludge sumps of mud in UASB anaerobic reation pool 7 and settling tank 11, further, after sedimentation, press mud machine by the pipeline suction at the bottom of sludge sump, are filtered dry mud, and filtrate is back to equalizing tank, and mud cake outward transport is processed.
This embodiment has following beneficial effect: it adopts all steel structure, and rational deployment, makes full use of space, has easy construction, simple to operate, and building is compact attractive in appearance.
Claims (1)
1. integrated small painting wastewater is processed complete process structure, it is characterized in that it comprises grid (1), equalizing tank (2), air supporting settling tank (3), PH adjusts pond (4), electrolyzer (5), intermediate pool (6), UASB anaerobic reation pool (7), Aerobic Pond (8), coagulation basin (9), flocculation basin (10), settling tank (11), clean water basin (12), filtering system (13), sludge thickener (14), pressure filter (15), grid (1) is connected with equalizing tank (2) by pipeline, equalizing tank (2) is connected with air supporting settling tank (3) by pipeline, air supporting settling tank (3) is adjusted pond (4) by pipeline with PH and is connected, PH adjusts pond (4) and is connected with electrolyzer (5) by pipeline, electrolyzer (5) is connected with intermediate pool (6) by pipeline, intermediate pool (6) is connected with UASB anaerobic reation pool (7) by pipeline, UASB anaerobic reation pool (7) is connected with Aerobic Pond (8) by pipeline, Aerobic Pond (8) is connected with coagulation basin (9) by pipeline, coagulation basin (9) is connected with flocculation basin (10) by pipeline, flocculation basin (10) is connected with settling tank (11) by pipeline, settling tank (11) is connected with clean water basin (12) by pipeline, clean water basin (12) are connected with filtering system (13) by pipeline, described air supporting settling tank (3), UASB anaerobic reation pool (7) is connected by concentrated (14) pond of pipeline and mud with settling tank (11), sludge thickener (14) is connected with pressure filter (15) by pipeline, sludge thickener (14) is connected with equalizing tank (2) by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420384637.0U CN203976588U (en) | 2014-07-09 | 2014-07-09 | Integrated small painting wastewater is processed complete process structure |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420384637.0U CN203976588U (en) | 2014-07-09 | 2014-07-09 | Integrated small painting wastewater is processed complete process structure |
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| Publication Number | Publication Date |
|---|---|
| CN203976588U true CN203976588U (en) | 2014-12-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420384637.0U Expired - Fee Related CN203976588U (en) | 2014-07-09 | 2014-07-09 | Integrated small painting wastewater is processed complete process structure |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106145554A (en) * | 2016-08-30 | 2016-11-23 | 宜兴市中发水处理环保设备有限公司 | A kind of processing system being applied to high-concentration garbage percolate |
-
2014
- 2014-07-09 CN CN201420384637.0U patent/CN203976588U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106145554A (en) * | 2016-08-30 | 2016-11-23 | 宜兴市中发水处理环保设备有限公司 | A kind of processing system being applied to high-concentration garbage percolate |
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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: 20141203 Termination date: 20200709 |