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 PDFInfo
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- 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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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
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.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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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)
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CN201621362756.1U CN206467098U (en) | 2016-12-13 | 2016-12-13 | A kind of biological reinforced processing unit of oil-polluted water |
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CN206467098U true CN206467098U (en) | 2017-09-05 |
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CN201621362756.1U Active CN206467098U (en) | 2016-12-13 | 2016-12-13 | A kind of biological reinforced processing unit of oil-polluted water |
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Cited By (1)
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 |
-
2016
- 2016-12-13 CN CN201621362756.1U patent/CN206467098U/en active Active
Cited By (1)
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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