CN2892839Y - Light oil polluted water integrated processing apparatus - Google Patents
Light oil polluted water integrated processing apparatus Download PDFInfo
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- CN2892839Y CN2892839Y CN 200520113839 CN200520113839U CN2892839Y CN 2892839 Y CN2892839 Y CN 2892839Y CN 200520113839 CN200520113839 CN 200520113839 CN 200520113839 U CN200520113839 U CN 200520113839U CN 2892839 Y CN2892839 Y CN 2892839Y
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Abstract
The utility model relates to a light oil wastewater integrated water treatment device, which comprises a base. An inclined plate separator, a buffering water tank, a filter, a coalescence separator, an absorber and a control box are arranged in the base. A wastewater pump is connected with the water inlet of the inclined plate separator through a pipeline. The water discharging opening of the inclined plate separator is connected with the inlet of the buffering water tank through a pipeline pump. The floating oil opening of the inclined plate separator is communicated with a waste oil tank through the pipeline. The water discharging opening of the buffering water tank is connected with the inlet of said filter through a pipeline pump. The outlet of the filter is connected with the oil containing wastewater inlet of the coalescence separator through the pipelines. The pure water outlet of the coalescence separator is communicated with the water inlet of the absorber through pipelines. The utility model can safely, reliably, conveniently and effectively remove and recovery the scattered oil and emulsified oil contained in oil containing wastewater, which makes the discharged water can meet Class One of national emission standard.
Description
Technical field
The utility model relates to a kind of light oil sewage integrated treating device, and this device integrates sedimentation, filtration, accurate coalescent and efficient adsorption technology, can be applicable to the oily water treatment that the lightweight oil POL storage operation produces.
Background technology
Chinese patent 200410044206.0 disclose that a kind of integrated form oil field mining liquid separates and waste disposal plant by the drum type brake horizontal tank and the swirler of setting in jar outside, the labyrinth cowling panel, waved plate, swash plate, oil spill stream weir plate, the radio frequency admittance detector, gas outlet, receive the grease chamber, the grease chamber, the modified polypropene bead, the hydraulic sand washing device, chemical feed pipe, mixing tank, water outlet, pump circulation receiving port, oil outlet is formed, it is characterized in that being provided with a whirlwind-type gas-liquid separator in the upper vertical of cylinder horizontal tank left end, be provided with oil distributor in the middle part of cylinder horizontal tank down at it, interior dress polypropylene pellets, be provided with the labyrinth cowling panel on oil distributor the right by preface, waved plate, the organic swash plate of modification, small oil distributing, the organic swash plate of modification, water-supplying chamber, oil-collecting cavity, accumulator, at small oil distributing, the upper top of big organic swash plate of modification and receipts grease chamber is provided with an oil spill stream weir plate, be provided with a filter inflator in the right part of cylinder horizontal tank, pot bottom between oil distributor and small oil distributing is provided with the hydraulic sand washing sand removing device, in water-supplying chamber, the base of receiving grease chamber and grease chamber is respectively equipped with water outlet separately, receiving port and oil outlet.But this apparatus structure complexity, and can not handle light oil sewage, light oil sewage is meant lightweight oil (gasoline, kerosene, diesel oil) POL storage operation sewage, the oily(waste)water that discharges when comprising cleaning of evaporator water, the flight-line maintenance of tank station, puts and puts a heavy jar every day such as the heavy oily(waste)water that produces etc.Contain suspended solids such as a large amount of oil contents and silt, iron rust, greasy filth in this oily(waste)water, handle comparatively difficulty.Therefore, need to propose a kind of new light oil sewage integrated treating device.
Summary of the invention
The purpose of this utility model is to provide a kind of light oil sewage integrated treating device, and this device integrates inclined plate sedimentation, filtration, accurate coalescent and efficient adsorption technology, can be widely used in the oily water treatment that the lightweight oil POL storage operation produces.
The purpose of this utility model is realized by following technical proposals: a kind of light oil sewage integrated treating device, a pedestal is arranged, and tilted plate separator, buffer tank, strainer, coalescing separator, adsorber, controlling box are housed on the described pedestal; Described tilted plate separator water inlet is connected with sump pump by pipeline, and the water port of described tilted plate separator is connected with described buffer tank inlet by pipeline; The oil slick mouth of described tilted plate separator is communicated with a sump oil case by pipeline; Described buffer tank water outlet is connected with described filter inlet by in-line pump; Described filter outlet is connected with described coalescing separator oily(waste)water inlet by pipeline; Described coalescing separator pure water inlet is communicated with described adsorber water inlet by pipeline.
Compared with the prior art the utility model has following advantage:
1, dispersed oil and the oil in water emulsion in the oily(waste)water can be removed and reclaim to the utility model safely, reliably, conveniently, effectively, makes discharge water meet or exceed national grade one discharge standard (oil-contg is less than 5ppm).
2, the utility model is rational in infrastructure, handsome in appearance, floor space is little.
3, the utility model adopts full physics method to handle oily(waste)water, not dosing, need not back flushing, does not produce secondary pollution.
4, the recyclable oil slick of the utility model, additional income reduces running cost.
5, the utility model filter core contamination capacity is big, and is insensitive to coming the water oleaginousness to change, long service life.
6, automatization level height of the present utility model, system operation is simple, and labour intensity is little.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples
Fig. 1 is that structure of the present utility model is launched synoptic diagram
Fig. 2 is a front view of the present utility model
Fig. 3 is a vertical view of the present utility model
Fig. 4 is sectional view of the present utility model (the A-A sectional view of Fig. 3)
Fig. 5 is a strainer synoptic diagram of the present utility model
Fig. 6 is a coalescing separator synoptic diagram of the present utility model
Fig. 7 is a coalescent filter core synoptic diagram of the present utility model
Fig. 8 is a coalescent fundamental diagram of the present utility model
Embodiment
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, light oil sewage integrated treating device of the present utility model has the pedestal 18 of a steel, and tilted plate separator 2, buffer tank 3, strainer 5, coalescing separator 6, adsorber 8, controlling box 7 are housed on the pedestal; Described tilted plate separator water inlet is connected with sump pump 1 by pipeline, and the water port of described tilted plate separator is connected with described buffer tank inlet by pipeline; The oil slick mouth of described tilted plate separator is communicated with a sump oil case 16 by pipeline; Described buffer tank water outlet is connected with described filter inlet by sewage pump; Described filter outlet is connected with described coalescing separator oily(waste)water inlet by pipeline; Described coalescing separator pure water inlet is communicated with described adsorber water inlet by pipeline, on this adsorber water purification output tube valve 9 is housed.The blow-off pipe of described tilted plate separator bottom is communicated with blowdown main road 17 by wash water valve 15, the blow-off pipe of buffer tank bottom is communicated with the blowdown main road by wash water valve 14, the blow-off pipe of filter bottom is communicated with the blowdown main road by wash water valve 12, the blow-off pipe of coalescing separator bottom is communicated with the blowdown main road by wash water valve 11, and the blow-off pipe of adsorber bottom is communicated with the blowdown main road by wash water valve 10.
In the present embodiment, how not sump pump adopts positive displacement pump, and this pump has stronger suction capacity, and flow is even, and oil content is not had the side effect of mechanical shearing emulsive.How sewage is by not being pumped in the tilted plate separator, and tilted plate separator adopts two-stage process to handle to remove oils and the suspended solids in the oily(waste)water.Oily(waste)water enters the water-and-oil separator inlet, this moment, flow direction made progress, this flowing of initially making progress, can guarantee that most free oil (oil slick) can be climbed to separator surface in the water, the oil slick gravity flow that rises to separator surface enters the sump oil case, and settled mud is regularly taken away.Sewage flows down to the separator bottom by first group of compact arranged coalescing-plate then.In the process that current move downward, oil droplet rising collision coalescence is at the lower surface of swash plate, and adverse current rises to the surface in pond.The swash plate angle of inclination is 60 °, has guaranteed higher suspended solid separation efficiency, and flowing under the current direction can help the cleaner plate face, guarantees the lasting optimization of water-and-oil separator processing property, reduces its maintenance workload.Sewage after the processing changes the flow direction once more on the surface, flow out below the sump oil baffle plate, flows through overflow weir, discharges from water outlet.Tilted plate separator separation efficiency height, the residence time of oily(waste)water in tilted plate separator is usually less than 10 minutes.Because the tilted plate separator in the present embodiment adopts the structure of prior art, is not described in detail at this.
Sewage gravity flow after tilted plate separator is handled enters buffer tank, and this water tank is provided with liquid level switch, has high-order and low alarm function.When water level reach a certain height, start sewage pump 4 automatically, when water level drops to certain position, stop lift pump automatically.Lift pump is sent into the strainer follow-up equipment to sewage and is continued to handle.A pipeline ball valve 13 is housed in the pipeline of sewage pump.
Referring to Fig. 5, in the present embodiment, strainer is a kind of pot type high efficiency filter, in be equipped with that contamination capacity is big, long service life, filter core that filtering accuracy is high, this strainer is made of wash water valve, thief hole, impulse mouth, pallet, filter core, housing, safety valve, drain, lifting swivel arrangement, differential manometer.Strainer adopts quick-opening device, and working service is very easy fast, good seal performance; The filter core contamination capacity that it adopts is big, long service life, and it is convenient to change, economical and effective.Strainer is as the protective device of coalescing separator and active carbon adsorber; has high filtering accuracy; can filter and remove tiny suspended contamination (＞10 μ m), can effectively prolong coalescent filter core and the work-ing life of adsorbing filter core in the follow-up equipment, reduce operation expense.After sewage entered strainer, thicker particle can precipitate immediately, and thinner particle is tackled by cartridge surface, and last water purification enters coalescing separator through the outlet conduit outflow filter through the oily(waste)water inlet.
Referring to Fig. 6, Fig. 7, Fig. 8, the coalescing separator in the present embodiment is the oily water separating equipment that adopts international advanced coalescence technology.Described coalescing separator is made of tank body 601, the coalescent district 602 of filtration, come-up disengaging zone 607, oil collecting zone 608, and filtering left side, coalescent district is the come-up disengaging zone, and the right side is oily(waste)water inlet 603 and sewage draining exit 604.Be provided with a plurality of coalescent filter cores 621 in filtering coalescent district, be provided with oil collecting zone at come-up top, disengaging zone, the bottom is provided with pure water inlet 606 and discharge outlet 605, and the oil collecting zone top is provided with venting port 609 and oil discharge outlet 610.Described coalescent filter core has a cylindric inner framework 623 and a cylindric outer skeleton 626, the skeleton two ends are provided with end ring 622, described inner framework center one side is provided with polyester filtering layer 624, be provided with breakdown of emulsion layer 625 between described inner framework and the outer skeleton, the outside of described outer skeleton is provided with coalescent layer 627, drain layer 628 in proper order.The oily(waste)water coalescent filter core of flowing through from inside to outside, this filter core has special micro-filtration, breakdown of emulsion and coalescent oil content multi-efficiency.Coalescent filter core by the high precision micro-filtration, is effectively tackled the granule foreign in the water on the one hand, especially tackles greasy filth impurity such as the tangible ferric oxide of stable emulsion state, iron sulphide, helps follow-up breakdown of emulsion and coalescent function.Breakdown of emulsion and coalescent effect are by exotic materials oily substance extremely strong avidity and hydrophobic nature to be realized on the other hand, coalescent filter core comes out to become big oil droplet with small in the water, free oil content is coalescent, and make it rapid come-up, come together in the oil bag of oil collecting zone, oil-contg can directly discharge less than 5mg/l in the water after the processing; Strong (the import:＜5000ppm of coalescing separator de-oiling ability of the present utility model; Outlet :≤5ppm), oil slick and oil in water emulsion in the energy effective elimination water; Coalescing separator de-oiling efficient height, disengaging time is short; Tensio-active agent is low to coalescent influence.
In the present embodiment, active carbon adsorber mainly is to realize its function by compacting charcoal absorption filter core.Activated carbon granule has very many micropores and huge specific surface area, and the organic pollutant in the water is had very strong physical adsorption ability, can effectively reduce organic content in the water, COD, colourity, peculiar smell etc., realizes the purpose of water quality advanced processing.
In the present embodiment, the Level Detection of the Level Detection of the open and close of sump pump, the open and close of sewage pump, buffer tank and control, sump oil case is all finished by controlling box with control, because what use is routine techniques, the electrical schematic diagram of controlling box reaches the wiring scheme omission with controlled member.
Claims (2)
1, a kind of light oil sewage integrated treating device has a pedestal, it is characterized in that: tilted plate separator (2), buffer tank (3), strainer (5), coalescing separator (6), adsorber (8), controlling box (7) are housed on the described pedestal; Described tilted plate separator water inlet is connected with sump pump by pipeline, and the water port of described tilted plate separator is connected with described buffer tank inlet by pipeline; The oil slick mouth of described tilted plate separator is communicated with a sump oil case (16) by pipeline; Described buffer tank water outlet is connected with described filter inlet by in-line pump; Described filter outlet is connected with described coalescing separator oily(waste)water inlet by pipeline; Described coalescing separator pure water inlet is communicated with described adsorber water inlet by pipeline.
2, light oil sewage integrated treating device according to claim 1, it is characterized in that: described coalescing separator by tank body, filter coalescent district, come-up disengaging zone, oil collecting zone constitute, in filtering coalescent district, be provided with a plurality of coalescent filter cores, this coalescent filter core has a cylindric inner framework, with a cylindric outer skeleton, the skeleton two ends are provided with end ring, described inner framework center one side is provided with the polyester filtering layer, be provided with the breakdown of emulsion layer between described inner framework and the outer skeleton, the outside of described outer skeleton is provided with coalescent layer, drain layer in proper order.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520113839 CN2892839Y (en) | 2005-07-20 | 2005-07-20 | Light oil polluted water integrated processing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520113839 CN2892839Y (en) | 2005-07-20 | 2005-07-20 | Light oil polluted water integrated processing apparatus |
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| Publication Number | Publication Date |
|---|---|
| CN2892839Y true CN2892839Y (en) | 2007-04-25 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 200520113839 Expired - Lifetime CN2892839Y (en) | 2005-07-20 | 2005-07-20 | Light oil polluted water integrated processing apparatus |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150675A (en) * | 2014-01-10 | 2014-11-19 | 广东金明环保科技有限公司 | Base used on domestic sewage treatment integrated equipment |
| CN105567408A (en) * | 2016-01-25 | 2016-05-11 | 华侨大学 | Cutting liquid purifying treatment device |
| CN106277411A (en) * | 2015-05-11 | 2017-01-04 | 余福华 | Oil-sewage separation device |
| CN107215920A (en) * | 2017-06-10 | 2017-09-29 | 武汉中舟环保设备股份有限公司 | One kind processing oil emulsion device |
| CN110844970A (en) * | 2019-12-02 | 2020-02-28 | 杈惧己 | Processing and recycling device for mixed waste emulsion |
-
2005
- 2005-07-20 CN CN 200520113839 patent/CN2892839Y/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150675A (en) * | 2014-01-10 | 2014-11-19 | 广东金明环保科技有限公司 | Base used on domestic sewage treatment integrated equipment |
| CN104150675B (en) * | 2014-01-10 | 2016-02-10 | 广东金明环保科技有限公司 | Be used in the pedestal of sanitary sewage disposal integrated equipment |
| CN106277411A (en) * | 2015-05-11 | 2017-01-04 | 余福华 | Oil-sewage separation device |
| CN105567408A (en) * | 2016-01-25 | 2016-05-11 | 华侨大学 | Cutting liquid purifying treatment device |
| CN105567408B (en) * | 2016-01-25 | 2022-05-03 | 华侨大学 | Cutting fluid purification unit |
| CN107215920A (en) * | 2017-06-10 | 2017-09-29 | 武汉中舟环保设备股份有限公司 | One kind processing oil emulsion device |
| CN110844970A (en) * | 2019-12-02 | 2020-02-28 | 杈惧己 | Processing and recycling device for mixed waste emulsion |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20150720 Granted publication date: 20070425 |
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| EXPY | Termination of patent right or utility model |