CN207108544U - 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 PDFInfo
- Publication number
- CN207108544U CN207108544U CN201620914460.XU CN201620914460U CN207108544U CN 207108544 U CN207108544 U CN 207108544U CN 201620914460 U CN201620914460 U CN 201620914460U CN 207108544 U CN207108544 U CN 207108544U
- Authority
- CN
- China
- Prior art keywords
- nozzle
- bubble
- suction casing
- flotation device
- bubble generator
- 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.)
- Active
Links
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
A kind of jet bubble generator of cyclone air-flotation device, including body, body are 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 side wall is provided with fluid inlet tube.Spray into form high-speed jet using nozzle, by the pulsation turbulent flow of jet, suction room forms negative pressure, mixes with liquid after air suction, and liquid is collided with gas and produces micro-bubble, and bubble is distributed in container by expanding pipe.
Description
Technical field
It the utility model is related to technical field of sewage.
Background technology
As oil field development enters the later stage, moisture content raises in Produced Liquid, causes to need oil-polluted water amount to be processed significantly
Increase, existing sewage disposal system treating capacity can not meet to require, especially offshore production platform space is limited, and processing is set
Standby floor area requirement is strict.The 1st compact vertical-type air-flotation device is researched and developed from EPCON companies in 2001(Compact
Flotation Unit, CFU)At sea oil field has been succeeded since application, successively have Siemens water utilities, Veolia water utilities,
The company more than 10 such as Cameron groups is proposed Related product, and Oil Field installation sum has exceeded 50 sets).CFU technologies are taken
The immense success obtained also result in the attention of domestic enterprise.
The maximum feature of cyclone air-flotation integrated technique is exactly to give full play to dissolved air flotation and centrifugation in pre-separation area
Synergy, increase substantially the collision sticking probability of micro air bubble and dispersed phase oil particles in pre-separation area, promote its shape
Into " microbubble-oil droplet sticks body ", accelerate its separation process.Obviously, bubble caused by micro bubble generation device is big in CFU equipment
The small operational effect on equipment has direct influence.This paper presents a kind of with CFU coordinative composition of equipments jet bubble generator,
To promote the development of CFU technologies and process of industrialization.
The content of the invention
The utility model is in view of the shortcomings of the prior art, there is provided a kind of with higher production bubble rate and suitable bubble grain
Footpath, improve the jet flow generating apparatus of the cyclone air-flotation device of the efficiency of the cyclone air-flotation device of oil field produced water process.
To realize the utility model purpose, there is provided following technical scheme:A kind of jet bubble of cyclone air-flotation device
Generating means, it is characterised in that including body, body is divided into suction casing, contraction section, trunnion section and diffusion from left to right
Section, suction casing are provided centrally with nozzle, and suction casing side wall is provided with fluid inlet tube.
Preferably, it is provided with spiral shape spoiler in contraction section.
Preferably, filter screen is provided with before diffuser.
Preferably, aqueous phase flow adjustment range is defined to 0.5 ~ 1.5m caused by nozzle3/h。
Preferably, gas phase flow rate adjustable range is defined to 0.5 ~ 1.55m caused by suction casing3/h。
Preferably, maximum pressure limits position 0.2MPa in contraction section.
Preferably, the larynx mouth and nozzle of trunnion section apart from adjustable range are defined to 15 ~ 25mm.
Preferably, contraction section is from the conical pipe to diminish greatly.
Preferably, diffuser is to become big conical pipe from small.
The jet bubble generator, its material are carbon steel;
Preferably, the present apparatus is using horizontal current tendency;
Preferably, the water-carrying capacity at nozzle is 1.28m3/ h, pressure 0.4MPa;
Preferably, the water-carrying capacity at suction room is 0.25 m3/ h, pressure 0.3MPa;
Preferably, jet bubble generator takes T-shape to install with current.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
A kind of jet bubble generator of cyclone air-flotation device, including body 1, body 1 are 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 are provided centrally with nozzle 2, suction casing 1.1
Side wall is provided with fluid inlet tube 3.Spiral shape spoiler 4 is provided with contraction section 1.2.Diffuser 1.3 is above provided with filter screen 4.Nozzle 2
Caused aqueous phase flow adjustment range is defined to 0.5 ~ 1.5m3/h.Gas phase flow rate adjustable range caused by suction casing 1.1 limits
It is set to 0.5 ~ 1.55m3/h.Maximum pressure limits position 0.2MPa in contraction section 1.2.The larynx mouth 1.3.1 of trunnion section 1.3 and nozzle 2
Be defined to 15 ~ 25mm apart from adjustable range.Contraction section 1.2 is from the conical pipe to diminish greatly, and taper is 35 degree.Diffuser 1.3
To become big conical pipe from small, taper is 15 degree.
Case history:
Embodiment 1:As shown in Figure 1, each part of device is connected, the Produced Liquid that waste water oil exploitation group provides,
Bubble result is directly observed by lucite tube:The bubble diameter of generating means release is more than 1mm;Bubble is intensive, overlapping tight
Weight;Bubble deformation is obvious, similar elliposoidal, and a large amount of air mass occurs, the generating means exit bubble of high-speed camera instrument shooting
Particle diameter is more than 3mm, running parameter such as table 1 below now:
The jet bubble generator initialization parameter of table 1
From the bubble diameter measured:Debugging working condition is not optimum condition.Analyze its reason:The gas-water ratio of setting is not
Properly, air flow rate is excessive;The larynx mouth distance 20mm of setting is not optimum value;The bubble of release is in lucite tube caliber
100mm insufficient space generates coalescence fully to spread.
Embodiment 2
As shown in Figure 1, each part of device, the Produced Liquid that waste water oil exploitation group provides are connected.
Operating condition adjustment is carried out regarding to the issue above:Reduce gas flow;Adjust nozzle and larynx mouth distance.Keep first
Larynx mouth distance 20mm is constant, reduces tolerance, and the operational factor after adjustment is shown in Table 2.The bubble of generating means release is away from outlet top
200mm, it is in reduction trend that the size of bubble declines with tolerance.Tolerance is 0.27m3During/h, air pocket number is reduced in photo, and
The overlapping decrease of bubble;When tolerance is down to 0.25m3/h(Mark condition), bubble number significantly reduces, and overlapping phenomenon almost disappears.Therefore select
The operational factor detected by the use of operating mode 5 as bubble.
Table 2
Under the conditions of operating mode 5, adjustment nozzle and trunnion distance, the Air Bubble Size change of observation generator release;When both
Distance is gradually reduced, and air pocket quantity is reduced, the increase of minute bubbles density;Best results when nozzle and trunnion distance are 15mm.Respectively
Liquid level bubble ratio see the table below
The optimal operating parameter of jet bubble generator is that entrance water-carrying capacity is 1.28m3/ h, pressure 0.4MPa;Enter
Oral air flow is 0.25 m3/h(Mark condition), pressure 0.3MPa, larynx mouth distance is set to 15mm.
Claims (3)
- A kind of 1. jet bubble generator of cyclone air-flotation device, it is characterised in that including body, body from left to right according to Secondary to be divided into suction casing, contraction section, trunnion section and diffuser, suction casing is provided centrally with nozzle, and suction casing side wall is provided with stream Body inlet pipe;Aqueous phase flow adjustment range is defined to 1.28 m caused by nozzle3/h;Gas phase flow rate caused by suction casing is adjusted Scope is defined to 0.25 m3/h;The larynx mouth of trunnion section and nozzle are defined to 15mm apart from adjustable range.
- 2. the jet bubble generator of a kind of cyclone air-flotation device according to claim 1, it is characterised in that shrink The conical pipe that Duan Weicong diminishes greatly.
- A kind of 3. jet bubble generator of cyclone air-flotation device according to claim 1, it is characterised in that diffusion Duan Weicong is small to become big conical pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620914460.XU CN207108544U (en) | 2016-08-22 | 2016-08-22 | A kind of jet bubble generator of cyclone air-flotation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620914460.XU CN207108544U (en) | 2016-08-22 | 2016-08-22 | A kind of jet bubble generator of cyclone air-flotation device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207108544U true CN207108544U (en) | 2018-03-16 |
Family
ID=61595655
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620914460.XU Active CN207108544U (en) | 2016-08-22 | 2016-08-22 | A kind of jet bubble generator of cyclone air-flotation device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207108544U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110240288A (en) * | 2019-07-15 | 2019-09-17 | 沁济(上海)环境科技有限公司 | Biological nano aerating system |
CN113461196A (en) * | 2021-07-27 | 2021-10-01 | 华东理工大学 | Fiber particle combined double-bubble enhanced oil-water separation complete equipment and method |
-
2016
- 2016-08-22 CN CN201620914460.XU patent/CN207108544U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110240288A (en) * | 2019-07-15 | 2019-09-17 | 沁济(上海)环境科技有限公司 | Biological nano aerating system |
CN113461196A (en) * | 2021-07-27 | 2021-10-01 | 华东理工大学 | Fiber particle combined double-bubble enhanced oil-water separation complete equipment and method |
CN113461196B (en) * | 2021-07-27 | 2022-10-21 | 华东理工大学 | Fiber particle combined double-bubble enhanced oil-water separation complete equipment and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20160082366A1 (en) | Apparatus for liquid degassing using coupling of swirling flow or centrifugal field and pressure gradient field | |
CN207108544U (en) | A kind of jet bubble generator of cyclone air-flotation device | |
CN104773789A (en) | Compact three-phase separation method and device | |
CN103979637A (en) | Purification device and separation method of oily sewage | |
CN103351043A (en) | Vortex-type mixing sedimentation integrated reactor | |
CN107473306A (en) | A kind of adjustable single tank twin-stage cyclone air-flotation device of stabilizing feed well | |
CN104478114A (en) | Rotational flow air flotation separation device of tar ammonia water | |
CN204265551U (en) | A kind of cyclone air-flotation tripping device of tar ammonia | |
JP4009180B2 (en) | Suspended water separation treatment system | |
US9975061B2 (en) | Evaporative concentrator and associated methods | |
CN106167284A (en) | A kind of jet bubble generator of cyclone air-flotation device | |
CN104445569A (en) | Method and system for seawater foam control | |
CN103086455A (en) | Oilfield sewage treatment apparatus | |
CN106957082B (en) | Geothermal water gas-liquid-solid separation device | |
CN207391128U (en) | A kind of oil-containing waste water treating device | |
CN206881951U (en) | It is a kind of to be flowed back supersonic cyclone separator from ejection circulation | |
CN208065955U (en) | A kind of novel gas-liquid line separator | |
CN204910903U (en) | Take whirl dirt separator of gas -liquid separation function | |
CN109956587B (en) | Quick separation system for coagulation air-floatation copolymerization | |
CN212924481U (en) | Cyclone desander with pressurization gas circuit | |
CN206751456U (en) | A kind of high-efficiency hydraulic air air-dissolving apparatus for air-dissolving air-float | |
CN208345806U (en) | The device of suspended particulate substance in a kind of processing water body | |
CN206587509U (en) | A kind of gas-liquid two-stage cyclone separator | |
JP2017105423A (en) | Floating matter collection ship | |
CN206266262U (en) | A kind of vertical jet cyclone multistage air-floating apparatus |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20191011 Address after: 214200 No.105, floor 1-2, building 74, China Yixing international environmental protection city, Gaocheng Town, Yixing City, Wuxi City, Jiangsu Province Patentee after: Jiangsu Kangyue Environmental Protection Technology Co., Ltd. Address before: 214200 Jiangsu city of Wuxi province Yixing gaochengzhen international environmental protection city 74 Building No. 2112 Patentee before: The point of Jiangsu Environmental Protection Technology Co. Ltd |
|
TR01 | Transfer of patent right |