CN106167284A - A kind of jet bubble generator of cyclone air-flotation device - Google Patents

A kind of jet bubble generator of cyclone air-flotation device Download PDF

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Publication number
CN106167284A
CN106167284A CN201610699562.9A CN201610699562A CN106167284A CN 106167284 A CN106167284 A CN 106167284A CN 201610699562 A CN201610699562 A CN 201610699562A CN 106167284 A CN106167284 A CN 106167284A
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CN
China
Prior art keywords
flotation device
bubble generator
cyclone air
jet bubble
jet
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.)
Pending
Application number
CN201610699562.9A
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Chinese (zh)
Inventor
周伟强
吴伟平
周莹
吴旭
李诚成
李亮亮
居朝乐
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Point Of Jiangsu Environmental Protection Technology Co Ltd
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Point Of Jiangsu Environmental Protection Technology Co Ltd
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Publication date
Application filed by Point Of Jiangsu Environmental Protection Technology Co Ltd filed Critical Point Of Jiangsu Environmental Protection Technology Co Ltd
Priority to CN201610699562.9A priority Critical patent/CN106167284A/en
Publication of CN106167284A publication Critical patent/CN106167284A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/38Treatment of water, waste water, or sewage by centrifugal separation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/26Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

The jet bubble generator of a kind of cyclone air-flotation device, including body, body is divided into suction casing, contraction section, trunnion section and diffuser from left to right, and suction casing is provided centrally with nozzle, and suction casing sidewall is provided with fluid inlet tube.Utilizing nozzle to spray into formation high-speed jet, by the pulsation turbulent flow of jet, suction chamber forms negative pressure, and collide after air suction generation micro-bubble with liquid mixing, liquid and gas, and bubble is distributed in container by expansion pipe.

Description

A kind of jet bubble generator of cyclone air-flotation device
Technical field
The present invention relates to technical field of sewage.
Background technology
Along with oil field development enters the later stage, in Produced Liquid, moisture content raises, and causes and needs oil-polluted water amount to be processed significantly Increasing, existing sewage disposal system treating capacity cannot meet requirement, and especially offshore production platform limited space, sets process Standby floor area requirement is strict.The 1st compact vertical-type air-flotation device (Compact is researched and developed from calendar year 2001 EPCON company Flotation Unit, CFU) at sea oil field succeed application since, successively have Siemens water utilities, Veolia water utilities, The companies more than 10 such as Cameron group are proposed Related product, and Oil Field is installed sum and exceeded 50 sets).CFU technology is taken The immense success obtained also result in the attention of domestic enterprise.
The maximum feature of cyclone air-flotation integrated technique gives full play to dissolved air flotation and centrifugation in pre-separation district exactly Synergism, increase substantially the collision sticking probability of micro air bubble and dispersion phase oil particles in pre-separation district, promote its shape Become " microbubble-oil droplet sticks body ", accelerate its separation process.Obviously, the bubble that in CFU equipment, micro bubble generation device produces is big The little operational effect on equipment has directly impact.This paper presents a kind of and CFU coordinative composition of equipments jet bubble generator, To promote development and the process of industrialization of CFU technology.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, it is provided that a kind of have higher product bubble rate and suitable bubble diameter, carries The jet flow generating apparatus of the cyclone air-flotation device of the efficiency of the cyclone air-flotation device that high oil field extracted water processes.
For realizing the object of the invention, it is provided that techniques below scheme: the jet bubble of a kind of cyclone air-flotation device occurs Device, it is characterised in that include body, body is divided into suction casing, contraction section, trunnion section and diffuser from left to right, inhales The section of entering is provided centrally with nozzle, and suction casing sidewall is provided with fluid inlet tube.
As preferably, in contraction section, it is provided with spiral type flow-disturbing part.
As preferably, before diffuser, it is provided with filter screen.
As preferably, produced by nozzle, aqueous phase flow adjustment range is defined to 0.5 ~ 1.5m3/h。
As preferably, produced by suction casing, gas phase flow rate range of accommodation is defined to 0.5 ~ 1.55m3/h。
As preferably, in contraction section, maximum pressure limits position 0.2MPa.
As preferably, the larynx mouth of trunnion section and the distance range of accommodation of nozzle are defined to 15 ~ 25mm.
As preferably, contraction section is from the conical pipe diminished greatly.
As preferably, diffuser is from the big conical pipe of little change.
Described jet bubble generator, its material is carbon steel;
As preferably, this device uses the current tendency of level;
As preferably, the discharge at nozzle is 1.28m3/ h, pressure is 0.4MPa;
As preferably, the discharge at suction chamber is 0.25 m3/ h, pressure is 0.3MPa;
As preferably, jet bubble generator and current take T-shape to install.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Detailed description of the invention
The jet bubble generator of a kind of cyclone air-flotation device, including body 1, body 1 is divided into from left to right Suction casing 1.1, contraction section 1.2, trunnion section 1.3 and diffuser 1.3, suction casing 1.1 is provided centrally with nozzle 2, suction casing 1.1 Sidewall is provided with fluid inlet tube 3.Spiral type flow-disturbing part 4 it is provided with in contraction section 1.2.Diffuser 1.3 is above provided with filter screen 4.Nozzle 2 Produced aqueous phase flow adjustment range is defined to 0.5 ~ 1.5m3/h.Gas phase flow rate range of accommodation limit produced by suction casing 1.1 It is set to 0.5 ~ 1.55m3/h.In contraction section 1.2, maximum pressure limits position 0.2MPa.The larynx mouth 1.3.1 of trunnion section 1.3 and nozzle 2 Distance range of accommodation be defined to 15 ~ 25mm.Contraction section 1.2 is from the conical pipe diminished greatly, and tapering is 35 degree.Diffuser 1.3 For the conical pipe big from little change, tapering is 15 degree.
Case history:
Embodiment 1: as shown in Figure 1, connects each parts of device, the Produced Liquid that waste water oil exploitation group provides, and passes through Lucite tube directly observes bubble result: the bubble diameter of generating means release is more than 1mm;Bubble is intensive, overlapping serious; Bubble deformation is obvious, similar elliposoidal, and a large amount of air mass occurs, the generating means exit bubble diameter of high-speed camera instrument shooting More than 3mm, the such as table 1 below of running parameter now:
Table 1 jet bubble generator initialization parameter
Bubble diameter from recording: debugging working condition is not optimum condition.Analyze its reason: the gas-water ratio of setting does not conforms to Suitable, air flow rate is excessive;Larynx mouth distance 20mm set is not optimum;The bubble of release is at lucite tube caliber 100mm Insufficient space with fully diffusion, create coalescence.
Embodiment 2
As shown in Figure 1, connect each parts of device, the Produced Liquid that waste water oil exploitation group provides.
Operating condition adjustment is carried out for the problems referred to above:Reduce gas flow;Adjust nozzle and larynx mouth distance.First protect Holding larynx mouth distance 20mm constant, reduce tolerance, the operational factor after adjustment is shown in Table 2.The bubble of generating means release is in outlet Side 200mm, the size of bubble declines in reducing trend with tolerance.Tolerance is 0.27m3During/h, in photo, air pocket number reduces, And bubble overlap weakens;When tolerance is down to 0.25m3/ h(marks condition), bubble number significantly reduces, and overlapping phenomenon almost disappears.Therefore Select the operational factor that operating mode 5 detects as bubble.
Table 2
Under the conditions of operating mode 5, adjust nozzle and trunnion distance, observe the Air Bubble Size change of generator release;When both distances Being gradually lowered, air pocket quantity reduces, and minute bubbles density increases;Nozzle and trunnion distance are best results during 15mm.Each liquid level Bubble ratio see table
The optimal operating parameter of jet bubble generator be inlet water flow be 1.28m3/ h, pressure is 0.4MPa;Enter implication Flow is 0.25 m3/ h(marks condition), pressure is 0.3MPa, and larynx mouth distance is set to 15mm.

Claims (9)

1. the jet bubble generator of a cyclone air-flotation device, it is characterised in that include that body, body depend on from left to right Secondary being divided into suction casing, contraction section, trunnion section and diffuser, suction casing is provided centrally with nozzle, and suction casing sidewall is provided with stream Body inlet pipe.
The jet bubble generator of a kind of cyclone air-flotation device the most according to claim 1, it is characterised in that shrink Spiral type flow-disturbing part it is provided with in Duan.
The jet bubble generator of a kind of cyclone air-flotation device the most according to claim 1, it is characterised in that diffusion Filter screen it is provided with before Duan.
The jet bubble generator of a kind of cyclone air-flotation device the most according to claim 1, it is characterised in that nozzle Produced aqueous phase flow adjustment range is defined to 0.5 ~ 1.5m3/h。
The jet bubble generator of a kind of cyclone air-flotation device the most according to claim 1, it is characterised in that suck The produced gas phase flow rate range of accommodation of section is defined to 0.5 ~ 1.55m3/h。
The jet bubble generator of a kind of cyclone air-flotation device the most according to claim 1, it is characterised in that shrink In section, maximum pressure limits position 0.2MPa.
The jet bubble generator of a kind of cyclone air-flotation device the most according to claim 1, it is characterised in that trunnion The larynx mouth of section is defined to 15 ~ 25mm with the distance range of accommodation of nozzle.
The jet bubble generator of a kind of cyclone air-flotation device the most according to claim 1, it is characterised in that shrink The conical pipe that Duan Weicong diminishes greatly.
The jet bubble generator of a kind of cyclone air-flotation device the most according to claim 1, it is characterised in that diffusion The conical pipe that the little change of Duan Weicong is big.
CN201610699562.9A 2016-08-22 2016-08-22 A kind of jet bubble generator of cyclone air-flotation device Pending CN106167284A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610699562.9A CN106167284A (en) 2016-08-22 2016-08-22 A kind of jet bubble generator of cyclone air-flotation device

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Application Number Priority Date Filing Date Title
CN201610699562.9A CN106167284A (en) 2016-08-22 2016-08-22 A kind of jet bubble generator of cyclone air-flotation device

Publications (1)

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CN106167284A true CN106167284A (en) 2016-11-30

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113144929A (en) * 2021-05-08 2021-07-23 中海石油(中国)有限公司 Premixing homogeneous coupling type bubble generator
CN114920320A (en) * 2022-06-06 2022-08-19 内蒙古美方煤焦化有限公司 Coke-oven plant waste water tar recovery unit

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201124121Y (en) * 2007-11-21 2008-10-01 昆明理工大学 Combined Jet Microbubble Generator
CN201140931Y (en) * 2008-01-15 2008-10-29 董跃祥 Pressure-reducing increment device
CN202237768U (en) * 2011-10-07 2012-05-30 刘军 Desulfurization regeneration ejector
CN103084022A (en) * 2013-02-21 2013-05-08 中国矿业大学 Self-absorption air type cyclone foaming device for dust removal of coal mine
CN203183861U (en) * 2013-04-30 2013-09-11 张树唐 Jet-flow water saving and dust removing device
CN105214531A (en) * 2015-09-11 2016-01-06 中国石油化工股份有限公司 Foam-making apparatus

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201124121Y (en) * 2007-11-21 2008-10-01 昆明理工大学 Combined Jet Microbubble Generator
CN201140931Y (en) * 2008-01-15 2008-10-29 董跃祥 Pressure-reducing increment device
CN202237768U (en) * 2011-10-07 2012-05-30 刘军 Desulfurization regeneration ejector
CN103084022A (en) * 2013-02-21 2013-05-08 中国矿业大学 Self-absorption air type cyclone foaming device for dust removal of coal mine
CN203183861U (en) * 2013-04-30 2013-09-11 张树唐 Jet-flow water saving and dust removing device
CN105214531A (en) * 2015-09-11 2016-01-06 中国石油化工股份有限公司 Foam-making apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113144929A (en) * 2021-05-08 2021-07-23 中海石油(中国)有限公司 Premixing homogeneous coupling type bubble generator
CN114920320A (en) * 2022-06-06 2022-08-19 内蒙古美方煤焦化有限公司 Coke-oven plant waste water tar recovery unit

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Application publication date: 20161130

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