CN206467098U - A kind of biological reinforced processing unit of oil-polluted water - Google Patents

A kind of biological reinforced processing unit of oil-polluted water Download PDF

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Publication number
CN206467098U
CN206467098U CN201621362756.1U CN201621362756U CN206467098U CN 206467098 U CN206467098 U CN 206467098U CN 201621362756 U CN201621362756 U CN 201621362756U CN 206467098 U CN206467098 U CN 206467098U
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China
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water
oil
air
processing unit
tank
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CN201621362756.1U
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盖忠辉
蒋立民
赵文博
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Heilongjiang Jinasen Bioengineering Co Ltd
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Heilongjiang Jinasen Bioengineering Co Ltd
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Abstract

The utility model discloses a kind of biological reinforced processing unit of oil-polluted water, device is designed to pot type, is divided into air-dissolving air-float area and microbial reaction area Liang Ge functional areas.Air-dissolving air-float area is located at the central tube of tank.Including water inlet, water distributor, dissolved air release.Air flotation zone effect is to remove most of oil slick in sewage by molten gas mixing water.Microbial reaction area includes microbe stuffing region, aerated portion.Effect is that the passage of air flotation zone middle and upper part from top to bottom enters microbial reaction area, and in the presence of microorganism, oil emulsion is separated after being demulsified and removed, and gravity flow enters downstream processing unit after water is collected through bottom collector pipe after processing;The crude oil of collection enters oil storage tank by collection tank through flowline;Sludge is periodically discharged into station through discharge pipeline and reclaims pond.The utility model can effectively solve the problem that the complicated oil-polluted water sedimentation time is elongated, the problem of disposal ability declines.

Description

A kind of biological reinforced processing unit of oil-polluted water
Technical field
The utility model is related to sewage treatment area, and in particular to a kind of biological reinforced processing unit of oil-polluted water.
Background technology
With putting more effort that tertiary oil production in oil field is developed, the development mode such as high concentration, ternary composite driving causes current original Water water-quality constituents is complicated and is difficult to handle, and water drive contains poly- concentration more and more higher, and the change of this raw water quality is dirty to oil field oil-containing Water treatment system causes huge impact.It is mainly manifested in:1st, the sedimentation time extends, popularization:Tertiary oil recovery exploitation Contain in recovered water after the chemical substances such as polymer, surfactant, aqueous viscosity increase, oil-water emulsion is serious, causes water-oil separating Time lengthening.The sewage sedimentation time increased to 18 hours of ternary composite driving by 6 hours of water drive during current sewage plant design, sank The extension of drop time directly results in sewage plant sedimentation tank volume increase, and floor space is increased.2nd, filtering velocity declines, and filter tank quantity increases Plus:The filtering tank filtering velocity design parameter of oily waste water treatment, after it experienced from water drive to poly- drive raw water quality constantly change, Driven from early stage pure water(16/8)M/h, is progressively shown in after gathering to the nineties later stage raw water and is adjusted to(12/8)M/h, be within 2005 Preferably ensure water quality, reduce the injury to stratum, filtering velocity is adjusted to again(10/6)M/h, considers to see in raw water for 2008 Poly- concentration is likely to be breached 350 mg/L, and to ensure effluent quality, design filtering velocity is reduced to again(8/4)M/h, to 2009 due to Filtering velocity reduces the problems such as occupation of land brought is big, construction investment is high, and design filter tank is returned to(12/8)M/h, but construction scale consideration 20% water more than needed, the ternary sewage plant of tertiary oil recovery and the design filtering velocity at high-concentration sewage station are(7/5)m/h.Design filter The reduction of speed causes filter tank quantity increase in sewage plant, and occupation of land is big, investment is high, while operating cost is high.
In order to tackle the situation of water degradation, it is necessary to develop a kind of new technical matters, the solution sedimentation time is elongated, filtering Slow, the problem of disposal ability declines.
Utility model content
Structure in view of settling tank is easy to old station transformation, and the present apparatus is designed to pot type, is divided into air-dissolving air-float area and micro- life Two functional areas of thing reaction zone.Air-dissolving air-float area is located at the central tube of tank.Including water inlet, water distributor, dissolved air release.Air supporting Area's effect is to remove most of oil slick in sewage by molten gas mixing water.Microbial reaction area include microbe stuffing region, Aerated portion.Effect is that the passage of air flotation zone middle and upper part from top to bottom enters bio-reaction zone, in the presence of microorganism, emulsification Oil is separated after being demulsified and removed, and gravity flow enters downstream processing unit after water is collected through bottom collector pipe after processing;The crude oil of collection Enter oil storage tank through flowline by collection tank;Sludge is periodically discharged into station through discharge pipeline and reclaims pond.
Brief description of the drawings
Accompanying drawing 1 is structural representation of the present utility model;
In figure:1st, tank body 2, water inlet water distributor 3, molten gas liberation port 4, collection tank 5, water outlet regulating tank 6, rotary-cutting type aeration First 7, inclined plate sedimentation case 8, water outlet inlet 9, mud-collecting slot 10, observation panel 11, light-transmitting opening 12, anti-explosion exhaust mouth 13, air dissolved pump enter Water pipe 14, overflow pipe 15, water outlet exhaust outlet 16, water outlet newel 17, heat traced pipeline.
Embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings:
The pot type oil-polluted water biochemical treatment apparatus.What it was realized in:Water enters middle and upper part cloth by water inlet pipe Water pipe 2 starts water distribution.It is dissolved air release 3 below water-locator, the water outlet of release 3 is to pass through reflux pump water inlet pipe 13 by reflux pump Draw the water handled in tank and enter air-dissolving apparatus, the dissolved air water of generation discharges the dissolved air water of micro-bubble by release 3, Oil slick and particulate contamination during band is leaked water during bubble in dissolved air water is floated up enter collection tank 4, pass through collection tank 4 Outside the delivery pipeline drain tank of connection.Water inlet distributor 2 and release 3 are placed in the central tube at Guan Nei centers, constitute gas Floating region domain.The biologic packing material area of two layers of steel framework composition is with outside central tube.Biologic packing material can be combined fiber filler, stand Body elasticity filler, soft or semi soft packing.Gas from roots blower is sent to below filler region by air line Aeration coil pipe on, be discharged into by gas release device 6 in water body, life provided for the microorganism that is attached in tank body on filler region Long required dissolved oxygen.Water down moves across the microbial reaction being attached in filler body and removes oil emulsion and dissolved oil;Place The tilting box 7 that water after reason enters below aeration coil pipe, the inside of tilting box 7 has inclined plate packing to play the work that oil removal is removed in sedimentation With.Water after the connection processing of collector pipe 8 above the inclined plate packing of tilting box 7 enters collector pipe 8 by tilting box 7.And by center Water is delivered to water outlet Adjustable water tank 5 and discharged by post.Newel has exhaust outlet 15 in upper end, plays regulation newel current pressure Power and outer air pressure balance.
The tank structure that the pot type oil-polluted water biochemical treatment apparatus is used is vertical settling tank(Natural subsidence tank or Coagulating setting tank)Tank body, original heat traced pipeline 17, collection mud pit 9, tank top observation panel 10, light-transmitting opening 11, exhaust outlet 12 in tank It is constant etc. structure.Aerating gas amount is set after being adjusted according to the water quality condition of sewage.
Present treatment device has following characteristics:
1st, device of the present utility model, with sedimentation, air supporting and microbiological treatment triple functions, can effectively go water removal In suspension, oil slick and oil emulsion, improve treatment effeciency.
2nd, using pot type structure, there is very high versatility with existing system, be conducive to transformation and upgrade of standing always.Using this When technique carries out old station transformation, existing equipment can be made full use of, the quantity of newly-built equipment is reduced, reduction to greatest extent is run into This.

Claims (3)

1. a kind of biological reinforced processing unit of oil-polluted water, it is characterised in that be that by 1, tank body 2, water inlet water distributor, 3, molten gas is released Put mouth, 4, collection tank, 5, water outlet regulating tank, 6, rotary-cutting type aeration head, 7, inclined plate sedimentation case, 8, water outlet inlet, 9, collection mud Groove, 10, observation panel, 11, light-transmitting opening, 12, anti-explosion exhaust mouthful, 13, air dissolved pump water inlet pipe, 14, overflow pipe, 15, water outlet exhaust outlet, 16th, water outlet newel, 17, heat traced pipeline composition.
2. the biological reinforced processing unit of a kind of oil-polluted water according to claim 1, it is characterised in that water inlet water distributor and release Put device to be placed in the central tube at Guan Nei centers, composition air supporting region.
3. the biological reinforced processing unit of a kind of oil-polluted water according to claim 1, it is characterised in that two are with outside central tube The biologic packing material area of floor steel framework composition, biologic packing material can be combined fiber filler, 3 D elastic filler, soft or medium-soft Property filler.
CN201621362756.1U 2016-12-13 2016-12-13 A kind of biological reinforced processing unit of oil-polluted water Active CN206467098U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621362756.1U CN206467098U (en) 2016-12-13 2016-12-13 A kind of biological reinforced processing unit of oil-polluted water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621362756.1U CN206467098U (en) 2016-12-13 2016-12-13 A kind of biological reinforced processing unit of oil-polluted water

Publications (1)

Publication Number Publication Date
CN206467098U true CN206467098U (en) 2017-09-05

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108218098A (en) * 2016-12-13 2018-06-29 黑龙江吉纳森生物工程股份有限公司 A kind of biological reinforced processing unit of oily wastewater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108218098A (en) * 2016-12-13 2018-06-29 黑龙江吉纳森生物工程股份有限公司 A kind of biological reinforced processing unit of oily wastewater

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