CN2175225Y - Combination type equipment for removing oil - Google Patents
Combination type equipment for removing oil Download PDFInfo
- Publication number
- CN2175225Y CN2175225Y CN 92213254 CN92213254U CN2175225Y CN 2175225 Y CN2175225 Y CN 2175225Y CN 92213254 CN92213254 CN 92213254 CN 92213254 U CN92213254 U CN 92213254U CN 2175225 Y CN2175225 Y CN 2175225Y
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- China
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- oil
- constituent element
- unit
- sewage
- removing device
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- Expired - Lifetime
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- Physical Water Treatments (AREA)
- Removal Of Floating Material (AREA)
Abstract
The utility model relates to a device for removing oil in sewage, which breaks the limit of conventional water treating equipment. A critical core part is designed to be a processing unit that is then standardized and serialized. Then, a plurality of oil removing processing units are optimally combined into the entire equipment according to the actual conditions of engineering so that once sewage lifting can be used for completing the whole treating process. The utility model which has the advantages of small occupation area, investment saving, low energy consumption and high function is suitable for treating various kinds of oily sewage.
Description
The utility model relates to a kind of egg Shape Plate Separator.
Present sewage degrease is general to adopt many different single function treatment equipment to finish the entire treatment technological process, take up an area of big, investment is high, can not adopt long flow process and finish the big contradiction of existence in treatment effect and working cost in sewage once promotes.Existing so far combined oil removing device all keeps original single function treatment equipment and profile, just adopts public base and appropriate design connecting tube, make it compact, reduce floor space, they generally only are used for little treatment capacity and a certain extraordinary occasion, as marine oil-water separator etc.
The purpose of this utility model provides a kind of egg Shape Plate Separator, be suitable for various treatment capacities, various oily(waste)waters, and occupation of land is so small to have only part to tens/one of conventional equipment, thereby can be placed in the workshop, on the production line, so that make an integral body with processing unit, be convenient to oily(waste)water reuse on the spot, oily in situ recovery.
The purpose of this utility model is achieved in that it has broken the boundary line of the single function treatment equipment of present routine, gets wherein core key component transfer design and becomes functional element (unit), and with these unit stdn seriations.Carry out the three-dimensional optimized combination with regard to choosing required unit like this, promptly design an integral device that meets concrete engine request according to the practical situation of concrete engineering.Therefore the present invention can adapt to any oil product, any processing water yield and various oil removing occasion.It is not only equipment also is equipment design method fast.
The utility model ties up to the various processing units of reasonable Arrangement on the three-dimensional space, and making it total floor space is the total floor space of conventional single-function device group part to tens/one.It can adopt more processing unit and can finish the entire treatment process from flowing through each unit after allowing sewage once promote this equipment of entering.Therefore it has effect height, advantage of low energy consumption, takes up an area of little, easy to maintenance and do not have a disadvantage of line clogging.
Below in conjunction with drawings and Examples the utility model is further specified.Fig. 1 is the structure diagram of embodiment.Present embodiment is to handle to contain heavy oil residue, sticking oil of lightweight and the serious oily(waste)water of emulsification.Present embodiment is made up of five constituent elements, and I is the breakdown of emulsion constituent element, and II is the coarse constituent element, and III is a Dou plate oil removal constituent element, and IV is the air supporting constituent element, and V is the Filtration Adsorption constituent element.Each constituent element comprises some processing units again, and 1 is floating oil suction unit, and 2 is eddy flow breakdown of emulsion unit; 3 is diffusion unit, and 4 is mud sump oil sedimentation unit, and 5 is mud sump oil upgrading unit; 6 revolve the unit for taking off, and 7 is the coarse unit, and 8 is Dou plate oil removal unit; 9 is the air-flotation reactor unit, and 10 are the dissolved air flotation chamber unit, and 11 are the current-sharing pipe unit; 12 is the froth breaking unit; 13 for drawing together the foam unit, and 14 is the Filtration Adsorption unit, also need have the emulsion splitter device 15 of throwing and sump pump 16 in addition beyond equipment.
Oily(waste)water A is after throwing emulsion splitter device 15 adds emulsion splitter, be pumped to this oil removal plant by sump pump 16, by tangentially enter swirler unit 2 there sharply eddy flow emulsion splitter and waste water are mixed rapidly take off surely, be heated simultaneously make the thinning general of heavy oil residue wherein the moisture content that wraps emit.Then waste water in the annular channel of diffusion unit 3 backspin, on revolve, backspin, on revolve.The eddy flow flow velocity is more and more slow, forms the good condition of cohesion, and twice backspin, on gradually mink cell focus, water and lightweight oil are separated in the motion of revolving.Mink cell focus sinks and to concentrate the higher heavy sump oil C of back oleaginousness through sedimentation unit 4 and upgrading unit 5 and arrange to the heavy oil collecting tank.Float over surface enrichment on the lightweight oil B and after floating is received 1 collection of oily unit, be discharged into the light oil collecting tank.Water then takes off through labyrinth type from the centre and revolves the unit and remove eddy flow and upwards flow through the coarse unit, perlite particle suction back proportion be slightly smaller than water and half keep afloat, half immerses in water, forms the semi-floating filter bed.Its underpart is more open, plays the collision cohesive action with elaioleucite in the water, and adherent elaioleucite will form more for a long time that bigger oil droplet separates with perlite, light come-up, heavy sinking.When the heavy viscosity of residual oil matter is big again, will together sink together with accompanying perlite particle.The heavy oil that sinks becomes greasy filth C through sedimentation unit 4, upgrading unit 5 and is discharged into the heavy oil collecting tank, and wherein the perlite particle of Huning can separate with heavy oil after heating.Lightweight elaioleucite and water are to the upper reaches.Through close water surface one deck filter bed; because buoyancy and action of gravity, this metafiltration bed is very tight, hole is very little, and the light oil particle is played the effect of micropore coarse; even it further becomes to large diameter elaioleucite leaves filter bed, flow into Dou plate oil removal unit 8 with water.Elaioleucite adheres to Dou plate surface formation oil film and moves on the whole and float to the water surface in long and narrow Dou plate passage, flows in the floating oil suction unit 1, flow to the light oil collecting tank then.In this process in the water with the heavy elaioleucite have an opportunity again through sedimentation unit 4, upgrading unit 5 becomes sump oil C and enters the heavy oil collecting tank.The elaioleucite of larger particles substantially but removes clean in the water so far.Remaining very tiny elaioleucite is floating 10 to form scum silica frost to the surface isolation unit, strikes off and enters the light oil collecting tank by drawing together foam unit 13.The water froth breaking unit 12 of then flowing through downwards, the bubble disappearance of breaking, adherent elaioleucite then sinks through sedimentation unit 4, and upgrading unit 5 becomes sump oil C and drains into the heavy oil collecting tank, and water then rises to middle part current-sharing pipe unit 11 and enters mechanical filter absorption constituent element V behind the froth breaking constituent element.If also residual in the water have oil then to be removed in the coke granule filter bed, water is discharged by filter bed.Regularly with the water backwashing filter bed of processing, equipment importation row processing is more then arrived in the recoil draining.Sewage flows automatically from access arrangement 20 processing units of experience and finishes the entire treatment process.The clearance of oil can be up to 99.99%.And heavy oil, light oil is separated and enters collecting tank separately, can carry out reuse.
Claims (5)
1, a kind of combined oil removing device that is used for removing the sewage oil-contg; it is characterized in that: the mode of employing Highgrade integration will make up breakdown of emulsion constituent element, coarse constituent element, Dou plate oil removal constituent element, air supporting constituent element and the optimum combination of mechanical filter absorption constituent element becomes an integral device; after sewage is raised access arrangement; from five processing units of flowing through; discharge after finishing the entire treatment process, all processing constituent elements carry out stdn, seriation, application by the inflow-rate of water turbine size and select for use and optimum combination according to concrete engineering practical situation.
2, combined oil removing device according to claim 1, it is characterized in that: the flaring annular channel that combination breakdown of emulsion constituent element adopts swirler and several circular cone machine to be formed, sewage enters the back and forms by being screwed into soon on twice of twice backspin revolving slowly gradually and revolve motion, chemical agent and heating mix with under finish by taking off steady to condensing light oil, water and heavy oil three separating process.
3, combined oil removing device according to claim 1 is characterized in that: the coarse constituent element places before the Dou plate oil removal constituent element, and the former removes mink cell focus and makes the lightweight oil coarse, to prevent that the Dou plate from stopping up and raising Dou plate oil removal effect.
4, combined oil removing device according to claim 1 is characterized in that: the air supporting constituent element, in the same space, arrange reaction chamber unit, unit, separate chamber, froth breaking unit, sedimentation unit and mud sump oil upgrading unit from top to bottom.
5, combined oil removing device according to claim 1 is characterized in that: the mechanical filter constituent element adopts stepless coke granule as the Filtration Adsorption medium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92213254 CN2175225Y (en) | 1992-02-22 | 1992-02-22 | Combination type equipment for removing oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92213254 CN2175225Y (en) | 1992-02-22 | 1992-02-22 | Combination type equipment for removing oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2175225Y true CN2175225Y (en) | 1994-08-24 |
Family
ID=33763520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 92213254 Expired - Lifetime CN2175225Y (en) | 1992-02-22 | 1992-02-22 | Combination type equipment for removing oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2175225Y (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101148278B (en) * | 2006-09-19 | 2010-11-03 | 威海广泰环保科技有限公司 | Oil-water purifying method and equipment thereof |
| CN101602528B (en) * | 2009-06-09 | 2011-03-09 | 舟山中邦节能科技有限公司 | Oil-water separation device for treating oil-containing wastewater |
| CN102600642A (en) * | 2012-03-21 | 2012-07-25 | 泉州市泉港迅达石化设备安装有限公司 | Efficient three-liquid level oil-water automatic separation equipment |
| CN103224299A (en) * | 2013-05-14 | 2013-07-31 | 大连福佳·大化石油化工有限公司 | Oily sewage oil-skimming and deslagging system |
| CN103351037A (en) * | 2013-07-09 | 2013-10-16 | 中铁第四勘察设计院集团有限公司 | Oily wastewater and sludge treatment device and treatment method thereof |
| CN104649453A (en) * | 2015-02-27 | 2015-05-27 | 江苏江大环境工程有限责任公司 | Oil-separation recovery combination apparatus |
| CN105347568A (en) * | 2015-11-30 | 2016-02-24 | 无锡工源机械有限公司 | Restaurant waste water treatment device |
| CN105776663A (en) * | 2016-04-12 | 2016-07-20 | 国家海洋局第海洋研究所 | Process for treating ship oily water with enteromorpha |
| CN108623041A (en) * | 2018-05-18 | 2018-10-09 | 沈阳建筑大学 | A kind of mobile water producing system for well-drilling waste water |
-
1992
- 1992-02-22 CN CN 92213254 patent/CN2175225Y/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101148278B (en) * | 2006-09-19 | 2010-11-03 | 威海广泰环保科技有限公司 | Oil-water purifying method and equipment thereof |
| CN101602528B (en) * | 2009-06-09 | 2011-03-09 | 舟山中邦节能科技有限公司 | Oil-water separation device for treating oil-containing wastewater |
| CN102600642B (en) * | 2012-03-21 | 2015-07-08 | 泉州市泉港迅达石化设备安装有限公司 | Efficient three-liquid level oil-water automatic separation equipment |
| CN102600642A (en) * | 2012-03-21 | 2012-07-25 | 泉州市泉港迅达石化设备安装有限公司 | Efficient three-liquid level oil-water automatic separation equipment |
| CN103224299A (en) * | 2013-05-14 | 2013-07-31 | 大连福佳·大化石油化工有限公司 | Oily sewage oil-skimming and deslagging system |
| CN103351037A (en) * | 2013-07-09 | 2013-10-16 | 中铁第四勘察设计院集团有限公司 | Oily wastewater and sludge treatment device and treatment method thereof |
| CN103351037B (en) * | 2013-07-09 | 2014-10-08 | 中铁第四勘察设计院集团有限公司 | Oily wastewater and sludge treatment device and treatment method thereof |
| CN104649453A (en) * | 2015-02-27 | 2015-05-27 | 江苏江大环境工程有限责任公司 | Oil-separation recovery combination apparatus |
| CN104649453B (en) * | 2015-02-27 | 2016-11-30 | 江苏江大环境工程有限责任公司 | Unit equipment is reclaimed in a kind of oil removal |
| CN105347568A (en) * | 2015-11-30 | 2016-02-24 | 无锡工源机械有限公司 | Restaurant waste water treatment device |
| CN105776663A (en) * | 2016-04-12 | 2016-07-20 | 国家海洋局第海洋研究所 | Process for treating ship oily water with enteromorpha |
| CN108623041A (en) * | 2018-05-18 | 2018-10-09 | 沈阳建筑大学 | A kind of mobile water producing system for well-drilling waste water |
| CN108623041B (en) * | 2018-05-18 | 2021-10-29 | 沈阳建筑大学 | Movable water treatment system for drilling wastewater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |