CN101716431A - Self-priming centrifugal emulsion breaking processing machine for emulsified oil - Google Patents
Self-priming centrifugal emulsion breaking processing machine for emulsified oil Download PDFInfo
- Publication number
- CN101716431A CN101716431A CN200910191339A CN200910191339A CN101716431A CN 101716431 A CN101716431 A CN 101716431A CN 200910191339 A CN200910191339 A CN 200910191339A CN 200910191339 A CN200910191339 A CN 200910191339A CN 101716431 A CN101716431 A CN 101716431A
- Authority
- CN
- China
- Prior art keywords
- oil
- self
- emulsion
- rotary drum
- drum body
- 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.)
- Granted
Links
- 239000000839 emulsion Substances 0.000 title claims abstract description 49
- 238000005119 centrifugation Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000012530 fluid Substances 0.000 claims abstract description 11
- 230000005540 biological transmission Effects 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 7
- 230000015556 catabolic process Effects 0.000 claims description 16
- 230000008859 change Effects 0.000 claims description 2
- 238000000926 separation method Methods 0.000 abstract description 9
- 230000009471 action Effects 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 42
- 230000000694 effects Effects 0.000 description 4
- 238000004945 emulsification Methods 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000001804 emulsifying effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000010723 turbine oil Substances 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000007738 vacuum evaporation Methods 0.000 description 1
- 239000002569 water oil cream Substances 0.000 description 1
Landscapes
- Centrifugal Separators (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention relates to a self-priming centrifugal emulsion breaking processing machine for emulsified oil, which applies the centrifugation technology to the emulsion breaking processing of oil and mainly comprises a power device, a transmission shaft, a rotary drum body, tapered blades, a water outlet, a water storage device, an oil discharge outlet and the like. The self-priming centrifugal emulsion breaking processing machine for the emulsified oil is characterized in that: the rotating rotary drum body is utilized to perform self-priming action, and a separate solution feed pump is not needed to arranged; an oil inlet is connected with a shaft sleeve on the transmission shaft by an electromagnetic flow valve, and continuous liquid feeding is realized by fluid guide holes on the shaft sleeve and small holes uniformly distributed on the tapered blades; a plurality of layers of tapered blades are overlaid and arranged in the rotary drum body to perform the centrifugation of the emulsified oil; and the lower end of the rotary drum body is provided with the water outlet and the water storage device and are mutually locked with the electromagnetic flow valve. The invention has the advantages of continuous separation, high separation efficiency, simple and convenient operation, low cost, emulsion breaking realization of the emulsified oil and the like.
Description
Technical field
The present invention relates to a kind of emulsion breaking processing machine for emulsified oil of self-priming centrifugation, specifically be a kind of by the rotation rotary drum body carry out the emulsion breaking processing machine that centrifugation contains water-emulsified oil liquid, be used to be in the purifying processing device of emulsified state oil.
Background technology
Oil very easily forms emulsion under moisture, colloid, energy, in case emulsion deterioration, fluid no longer have good profit voltinism energy, and extremely difficult regeneration breakdown of emulsion, therefore usually emulsification fluid is used as " waste oil " in the engineering and scraps processing, " changing once, scrap a collection of ".The serious waste that this had both caused petroleum resources causes a large amount of waste oil to be drained or sedimentation is gone into underground.In the breakdown of emulsion separation process of oil emulsion, the physics breakdown of emulsion separation method of employing mainly contains gravity settling separation, centrifugation, ultrasonic wave or microwave demulsifying separation, the separation of electric field breakdown of emulsion etc. at present.The basic ideas of its breakdown of emulsion may be summarized to be external force and energy to emulsion are provided, the skin covering of the surface that makes its dispersed phase drop destroys and regroups big drop and realize its separation, these methods are primarily aimed at moisture bigger oil emulsion, as breakdown of emulsion processing of crude oil etc., effect for these methods of processing of the oil emulsion in the engineering actual production is quite limited, also needs to set up some other devices." 92238237.9 " relate to a kind of demulsification treating apparatus of turbine oil, are in front end position utilization low velocity shear power the most of moisture of emulsification turbine oil to be removed, and the degree of depth dewaters in the vacuum evaporation oil purifier of the fluid input postposition after will purifying again." CN 1605375A " discloses the equipment of a kind of convolution cavitation device and convolution cavitation breakdown of emulsion, carry out after breakdown of emulsion handles containing water-emulsified oil or emulsified oily watewater, its dehydration rate or oil removal rate all can reach more than 92%, can dewater or oil removal treatment to water-oil emulsion under the condition that does not add or add less chemical demulsifier.It is more that these methods all exist mechanism, the operation sequence complexity, and the production cost height, and specific aim is stronger, and pervasive degree is not enough, is unfavorable for popularizing and promoting.
Summary of the invention
In order to overcome the deficiencies in the prior art, the present invention proposes a kind of emulsion breaking processing machine for emulsified oil of self-priming centrifugation, do not need specialized configuration oil transportation drive unit, the negative pressure oil suction of adopting rotary drum body self rotation to produce, because the decentralized photo (water droplet) in the oil emulsion is different with the proportion of continuous phase (oil), under the turning effort of rotary drum body inner conical blade, generation centrifugal force difference, wherein decentralized photo can flow to the rotary drum body wall along the lower surface of taper blade, enter in the accumulator through discharge outlet, the top that the less continuous phase of while proportion then flows to taper blade from bottom to top enters oil drain out.Realize separation, purifying and emulsifying oil continuously, have separative efficiency height, easy and simple to handle, advantages such as cost is low, minimizing user operation sequence.
The technical solution adopted for the present invention to solve the technical problems is:
A kind of emulsion breaking processing machine for emulsified oil of self-priming centrifugation, mainly comprise oil-in, power set, power transmission shaft, rotary drum body and taper blade, discharge outlet, accumulator and oil drain out, oil-in connects the axle sleeve on the power transmission shaft, uniform aperture is arranged on the taper blade, described taper blade is installed in the rotary drum body by the multilayer stack, and the lower end of rotary drum body is provided with discharge outlet, accumulator, and oil drain out is installed on top.
An electromagnetic flow valve is set on the described oil-in, liquid level display window, fluid level controller are set on the accumulator, realize interlocking with electromagnetic flow valve.
The invention has the beneficial effects as follows, utilize the self-priming effect of the rotation realization oil-feed of rotary drum body inner conical blade, saved than complex drive mechanism and pipeline, reduced direct cost, the taper blade that utilizes multilayer to be superimposed carries out centrifugation to oil emulsion, adjusting vane gap easily, handle with the breakdown of emulsion that adapts to different types of oil emulsion, the scope of application is more extensive, and under the effect of centrifugal revolving force, oil emulsion is begun upwards to flow step by step by first taper blade of rotary drum body bottom, until the vertex of a cone of last blade and discharge outside the rotary drum body, the breakdown of emulsion that the circulation of realization one action obtains repeatedly oil emulsion is handled, and has reduced operational sequence, has improved the breakdown of emulsion separative efficiency; Be provided with discharge outlet and accumulator in the bottom of rotary drum body, accumulator is placed a certain amount of water in advance before operation, utilizes the compatibility of water, is beneficial to compile herein from the moisture that rotary drum body is discharged, and forms bigger water droplet, enters in the accumulator; Float is set in the accumulator, linkage and solenoid, realize interlocking with the electromagnetic flow valve of oil-in, change and control the openings of sizes of oil-feed flow valve automatically according to the lifting of the water yield in the accumulator, and then control enters the flow velocity of the oil emulsion in the taper blade, the separative efficiency that realization is best.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Among the figure: 1-power set, 2-power transmission shaft, 3-driving sleeve, 4-liquid level interlocking controller, 5-oil-in, 6-oil-in switch valve, the 7-filter, 8-electromagnetic flow valve, 9-rotary drum body, the 10-taper blade, 11-oil drain out, 12-oil drain out switch valve, pod apertures on the 13-axle sleeve, 14-cutoff board, 15-liquid level display window, the 16-accumulator, 17-discharge outlet, 18-outlet switch valve.
The specific embodiment
Describe technical scheme of the present invention in detail below in conjunction with accompanying drawing.
As shown in Figure 1, the present invention is by oil-in 5, power set 1, power transmission shaft 2, rotary drum body 9 and taper blade 10, compositions such as discharge outlet 17 and accumulator 16 and oil drain out 11, the flow velocity of an electromagnetic flow valve 8 with the control oil emulsion is set on the oil-in 5, the axle sleeve 3 that oil-in 5 connects on the power transmission shaft, by the pod apertures on the axle sleeve 13 oil emulsion is connected with taper blade 10, uniform aperture is arranged on the taper blade 10, be installed in the rotary drum body 9 by the multilayer stack, be convenient to oil emulsion and from bottom to top flow under centrifugal action power, the fluid outflow of oil drain out 11 for demulsification installed on the top of rotary drum body 9, the lower end is provided with discharge outlet 17, discharge outlet 17 connects accumulator 16, and fluid level controller 4 is set on the accumulator 16, realizes interlocking with electromagnetic flow valve 8.
The present invention realizes what its breakdown of emulsion was handled like this: treat that the oil emulsion that breakdown of emulsion is handled enters the interior pod apertures 13 of axle sleeve through electromagnetic flow valve 8, the negative pressure that produces under the turning effort of taper blade 10 realizes that self-priming flows into its underpart, because the decentralized photo (water droplet) in the oil emulsion is different with the proportion of continuous phase (oil), under the turning effort of rotary drum body 9 inner conical blades 10, generation centrifugal force difference, wherein the top that then flows to taper blade 10 from bottom to top of the fluid behind the breakdown of emulsion enters oil drain out 11, decentralized photo can flow to rotary drum body 9 walls along the lower surface of taper blade 10, the decentralized photo of multilayer blade constantly compiles, polymerization forms big water droplet, in accumulator 16 under the compatibility effect of water, enter in the accumulator 16 through discharge outlet 17, the fluid level controller 4 that is provided with in the accumulator 16 is by the variation of mechanisms such as float according to liquid level, automatically detect the component that breakdown of emulsion separates moisture, and then control enters the oil emulsion flow in the rotary drum body 9, realize efficient, separate continuously, purifying and emulsifying oil has easy and simple to handle, cost is low, reduce advantages such as user's operation sequence.
Claims (4)
1. the emulsion breaking processing machine for emulsified oil machine of a self-priming centrifugation, it is characterized in that, comprise oil-in, power set, power transmission shaft, rotary drum body and taper blade, discharge outlet, accumulator and oil drain out, oil-in connects the axle sleeve on the power transmission shaft, and uniform aperture is arranged on the taper blade, and described taper blade is installed in the rotary drum body by the multilayer stack, the lower end of rotary drum body is provided with discharge outlet, accumulator, and oil drain out is installed on top.
2. the emulsion breaking processing machine for emulsified oil of self-priming centrifugation according to claim 1, it is characterized in that, an electromagnetic flow valve is set on the described oil-in, change and control the openings of sizes of oil-feed flow valve automatically according to the lifting of the water yield in the accumulator, and then control enters the flow velocity of the oil emulsion in the taper blade.
3. the emulsion breaking processing machine for emulsified oil of self-priming centrifugation according to claim 1 is characterized in that, liquid level display window, fluid level controller are set on the accumulator, realizes interlocking with electromagnetic flow valve.
4. the emulsion breaking processing machine for emulsified oil of self-priming centrifugation according to claim 1, it is characterized in that, oil-in is connected on the axle sleeve on the power transmission shaft, the negative pressure that produces under the turning effort of taper blade realizes self-priming, by the pod apertures on the axle sleeve oil emulsion is connected with taper blade, uniform aperture is arranged on the taper blade, realize the breakdown of emulsion passage of fluid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910191339.3A CN101716431B (en) | 2009-11-06 | 2009-11-06 | Self-priming centrifugal emulsion breaking processing machine for emulsified oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910191339.3A CN101716431B (en) | 2009-11-06 | 2009-11-06 | Self-priming centrifugal emulsion breaking processing machine for emulsified oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101716431A true CN101716431A (en) | 2010-06-02 |
| CN101716431B CN101716431B (en) | 2014-07-09 |
Family
ID=42431126
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200910191339.3A Expired - Fee Related CN101716431B (en) | 2009-11-06 | 2009-11-06 | Self-priming centrifugal emulsion breaking processing machine for emulsified oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101716431B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105107234A (en) * | 2015-09-28 | 2015-12-02 | 河北工业大学 | Dehydrating plant, and oil purifier and continuous pre-dehydrating method using dehydrating plant |
| CN107715500A (en) * | 2017-08-04 | 2018-02-23 | 怡然科技（深圳）有限公司 | turbulent flow type oil-water separator |
| CN108726753A (en) * | 2018-06-19 | 2018-11-02 | 濮阳职业技术学院 | A kind of oil field waste microwave processing equipment |
| CN114669084A (en) * | 2022-03-17 | 2022-06-28 | 山东渤泰能源科技有限公司 | Mineral turbine oil dewatering device and dewatering system thereof |
| CN115232637A (en) * | 2022-08-11 | 2022-10-25 | 北京石油化工学院 | Vertical crude oil dehydration equipment |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN86104596A (en) * | 1986-07-05 | 1988-01-27 | 中国科学院生物物理研究所 | Self-pumping and continuous-flowing centrifuger |
| JP2004034017A (en) * | 2002-07-05 | 2004-02-05 | Cnk:Kk | Centrifugal separator provided with liquid separation function |
| CN101384371A (en) * | 2006-02-13 | 2009-03-11 | 阿尔法拉瓦尔股份有限公司 | Method for supervising a centrifugal separator |
| CN101384329A (en) * | 2006-02-13 | 2009-03-11 | 阿尔法拉瓦尔股份有限公司 | Centrifugal separator |
| CN201524452U (en) * | 2009-11-06 | 2010-07-14 | 重庆工商大学 | Self-absorption centrifugal separation demulsification processing machine for emulsified oil |
-
2009
- 2009-11-06 CN CN200910191339.3A patent/CN101716431B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN86104596A (en) * | 1986-07-05 | 1988-01-27 | 中国科学院生物物理研究所 | Self-pumping and continuous-flowing centrifuger |
| JP2004034017A (en) * | 2002-07-05 | 2004-02-05 | Cnk:Kk | Centrifugal separator provided with liquid separation function |
| CN101384371A (en) * | 2006-02-13 | 2009-03-11 | 阿尔法拉瓦尔股份有限公司 | Method for supervising a centrifugal separator |
| CN101384329A (en) * | 2006-02-13 | 2009-03-11 | 阿尔法拉瓦尔股份有限公司 | Centrifugal separator |
| CN201524452U (en) * | 2009-11-06 | 2010-07-14 | 重庆工商大学 | Self-absorption centrifugal separation demulsification processing machine for emulsified oil |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105107234A (en) * | 2015-09-28 | 2015-12-02 | 河北工业大学 | Dehydrating plant, and oil purifier and continuous pre-dehydrating method using dehydrating plant |
| CN107715500A (en) * | 2017-08-04 | 2018-02-23 | 怡然科技（深圳）有限公司 | turbulent flow type oil-water separator |
| CN108726753A (en) * | 2018-06-19 | 2018-11-02 | 濮阳职业技术学院 | A kind of oil field waste microwave processing equipment |
| CN114669084A (en) * | 2022-03-17 | 2022-06-28 | 山东渤泰能源科技有限公司 | Mineral turbine oil dewatering device and dewatering system thereof |
| CN115232637A (en) * | 2022-08-11 | 2022-10-25 | 北京石油化工学院 | Vertical crude oil dehydration equipment |
| CN115232637B (en) * | 2022-08-11 | 2023-08-22 | 北京石油化工学院 | Vertical crude oil dehydration equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101716431B (en) | 2014-07-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106630514B (en) | Treatment system for oily sludge, separation equipment and treatment method thereof | |
| CN101716431B (en) | Self-priming centrifugal emulsion breaking processing machine for emulsified oil | |
| US11123754B2 (en) | Liquid-liquid-solid three-phase separator for waste oil | |
| CN104944619B (en) | Electric Desalting Wastewater deoiling method in heavy crude process | |
| CN102188840B (en) | Centrifugal vacuum degassing device | |
| CN108423897A (en) | A kind of oiliness sewage treatment equipment and technique | |
| CN107216912A (en) | A kind of oil field emulsifies Method for treatment of oil and processing unit always | |
| CN105107234A (en) | Dehydrating plant, and oil purifier and continuous pre-dehydrating method using dehydrating plant | |
| CN106542684A (en) | A kind of processing equipment of quick process oil-polluted water | |
| CN110314416A (en) | A kind of equipment for water-oil separating | |
| CN102515308A (en) | Self-inflating micro-bubble oil remover and oil removing method | |
| CN201524452U (en) | Self-absorption centrifugal separation demulsification processing machine for emulsified oil | |
| CN202016989U (en) | Electric desalting and dehydrating device | |
| CN205055497U (en) | Dewatering device and use device's absolute oil machine | |
| CN114477576B (en) | Oil removal method for high-concentration oily sewage | |
| CN212051026U (en) | Decontamination system for oily solid waste | |
| CN101070199B (en) | Oil-phase enrichment method and apparatus for oil-contained dirt water | |
| CN107253749A (en) | A kind of pre- arranging device of industrial emulsion oil | |
| CN102351363B (en) | Kitchen waste treatment system | |
| CN102120630A (en) | Novel high-concentration emulsified wastewater deemulsification device | |
| CN105668961A (en) | Sludge treatment device and method | |
| JP2005246219A (en) | Oil-containing waste water treatment apparatus | |
| CN213771799U (en) | Deoiling, desanding and dewatering device for light oil sludge in oil field | |
| CN211645000U (en) | Processing system of oily sludge | |
| CN204958651U (en) | Oiliness chemical industry sewage treatment plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C53 | Correction of patent of invention or patent application | ||
| CB02 | Change of applicant information |
Address after: 400067 waste oil center of Industrial and Commercial University Of Chongqing, No. 19, Xuefu Road, Nan'an District, Chongqing Applicant after: CHONGQING TECHNOLOGY AND BUSINESS University Address before: 400067 Chongqing Nan'an District University Avenue, No. 19 Applicant before: Chongqing Technology and Business University |
|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20100602 Assignee: CHONGQING TECHNOLOGY AND BUSINESS UNIVERSITY TECHNOLOGY DEVELOPMENT GENERAL CO. Assignor: Chongqing Technology and Business University Contract record no.: 2015500000044 Denomination of invention: Self-priming centrifugal emulsion breaking processing machine for emulsified oil Granted publication date: 20140709 License type: Common License Record date: 20150925 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| DD01 | Delivery of document by public notice |
Addressee: Chen Bin Document name: Notice of Termination of Patent Rights |
|
| DD01 | Delivery of document by public notice | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140709 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |