CN202070289U - Inorganic ultra-filtration oil and water separation equipment - Google Patents
Inorganic ultra-filtration oil and water separation equipment Download PDFInfo
- Publication number
- CN202070289U CN202070289U CN2011201258756U CN201120125875U CN202070289U CN 202070289 U CN202070289 U CN 202070289U CN 2011201258756 U CN2011201258756 U CN 2011201258756U CN 201120125875 U CN201120125875 U CN 201120125875U CN 202070289 U CN202070289 U CN 202070289U
- Authority
- CN
- China
- Prior art keywords
- equipment
- ultra
- filtration
- inorganic
- hyperfiltration
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The utility model provides inorganic ultra-filtration oil and water separation equipment, which is characterized by consisting of a circulation groove (1), ultra-filtration equipment a (2), ultra-filtration equipment b (3) and a circulation pump (4). The ultra-filtration equipment a (2) is connected with the ultra-filtration equipment b (3) in parallel after being serially connected with the circulation pump (4), and then is connected with a first input opening (11) and an output opening (13) of the circulation groove (1). A complex pretreatment process of industrial wastewater is reduced due to investment of the inorganic ultra-filtration oil and water separation equipment, and one-time investment and operation cost are saved. The inorganic ultra-filtration oil and water separation equipment resolves the difficult problem of filtering precision at one step, realizes double benefits of high-precision emulsified oil separation and waste oil recycling at one step, and is an effective pretreatment scheme and equipment for realizing 'zero' drainage of water resources in the present industrial application field.
Description
Technical field
The utility model relates to the Treatment of Industrial Water application, and a kind of inorganic ultrafiltration oily water separating equipment is provided especially.
Background technology
Inorganic ultrafiltration oily water separating equipment is mainly used in the separation of oil emulsion and removes the field, and the separation at oil emulsion was the forward position project that a lot of experts and scholar pay close attention to always in the last few years, and its treatment process is also varied.Such as physics method oil removal by air bubbling, filtration oil removing, hydraulic cyclone oil removing, chemical method coagulation-flocculation, chemical oxidation, highly efficiency compositional type degreaser, various application technologies such as bioanalysis activated sludge process, biomembrance process, Anaerobic Microbiological Treatment Technology.Above technology respectively has advantage, adapts to various environment, but on treatment effeciency and precision certain limitation is arranged all, has various practical challenges in actual applications., acid and alkali corrosion not enough such as precision, temperature effect or the like are all brought resistance to its application.Therefore we have invented inorganic ultrafiltration oily water separating equipment in the practical application of numerous engineering projects, have alleviated some difficult problems to a great extent.
The utility model content
The purpose of this utility model provides a kind of inorganic ultrafiltration oily water separating equipment, to improve the oil emulsion separation accuracy, alleviates the influence to Treatment of Industrial Water such as acid and alkali corrosion and temperature.
The utility model provides a kind of inorganic ultrafiltration oily water separating equipment, it is characterized in that: described equipment is made up of circulating slot 1, hyperfiltration equipment a 2, hyperfiltration equipment b 3 and circulating pump 4;
---wherein, the top of circulating slot 1 is provided with first input port 11, second input port 12 and delivery outlet 13, preferably is provided with heater 14 in circulating slot 1 inside, to improve the efficient of water treatment;
---described hyperfiltration equipment a 2 bottoms are provided with charging aperture a 21, and the top is provided with dense water out a 22, and sidewall is provided with and produces mouth of a river a 23, and inside is provided with inorganic ceramic membrane;
---described hyperfiltration equipment b 3 bottoms are provided with charging aperture b 31, and the top is provided with dense water out b 32, and sidewall is provided with and produces mouth of a river b 33, and inside is provided with inorganic ceramic membrane;
---described hyperfiltration equipment a 2 is with after circulating pump 4 is connected, and is in parallel with hyperfiltration equipment b 3 again, links to each other with delivery outlet 13 with first input port 11 of circulating slot 1 then.
Wherein, all can be provided with two on the sidewall of described hyperfiltration equipment a 2 and hyperfiltration equipment b 3 and produce the mouth of a river, to improve the efficient of water outlet.
In the utility model, circulating pump is linked in the hyperfiltration device systems, can be realized that the dense water of part does inner high speed circulation in inorganic ultrafiltration apparatus, constantly the film surface is cleaned in cross-flow, to reduce the pollution level of film.
The inorganic ultrafiltration oily water separating equipment that the utility model provides, the ultrafiltration apparatus that utilizes inorganic ceramic membrane to make filters emulsified oil-containing waste water, according to the content of oil emulsion and the filtering accuracy of the ratio of removal selective membrane, channel sized according to influent quality situation selective membrane, be equipped with corresponding pre-processing device in case of necessity, its operation principle is as follows: the waste water that will contain oil emulsion is removed and directly to be entered inorganic ultrafiltration apparatus behind the bulky grain shape solid and filter, its filter type belongs to a kind of of cross-flow filtration, total water inlet is divided into two-way, one the tunnel is to filter the back to produce the water that water promptly sees through film, and another part is that dense water does not promptly see through the water after film concentrates.Producing water enters in next treatment process, and dense water reenters inorganic ultrafiltration apparatus after returning circulating slot and new water mixing according to a certain percentage again, and remaining dense water is done inner high speed and circulated continuous cross-flow cleaning film surface to reduce the pollution level of film in inorganic ultrafiltration apparatus.Water inlet like this, product water, dense water constantly concentrate product water via inorganic ultrafiltration apparatus and have reached processing intent, promptly produce the purpose that water and dense water concentrate oil removing.
A kind of inorganic ultrafiltration oily water separating equipment that the utility model provides, its advantage is: the operation of this equipment has reduced industrial wastewater complicated pretreatment process, has saved one-time investment and operating cost.And a disposable difficult problem that solves filtering accuracy settles at one go and realizes that the high accuracy oil emulsion separates the double benefit that reclaims with waste oil, is the effective pretreating scheme and the equipment of present industrial application water resource " zero " discharging.
Description of drawings
Below in conjunction with drawings and the embodiments the utility model is described in further detail:
Fig. 1 is the structural representation of inorganic ultrafiltration oily water separating equipment.
The specific embodiment
A kind of inorganic ultrafiltration oily water separating equipment, concrete structure as shown in Figure 1, this equipment is made up of circulating slot 1, hyperfiltration equipment a 2, hyperfiltration equipment b 3 and circulating pump 4; Wherein, the top of circulating slot 1 is provided with first input port 11, second input port 12 and delivery outlet 13; Hyperfiltration equipment a 2 bottoms are provided with charging aperture a 21, and the top is provided with dense water out a 22, and sidewall is provided with and produces mouth of a river a 23, and inside is provided with inorganic ceramic membrane; Hyperfiltration equipment b 3 bottoms are provided with charging aperture b 31, and the top is provided with dense water out b 32, and sidewall is provided with and produces mouth of a river b 33, and inside is provided with inorganic ceramic membrane; Described hyperfiltration equipment a 2 is with after circulating pump 4 is connected, and is in parallel with hyperfiltration equipment b 3 again, links to each other with delivery outlet 13 with first input port 11 of circulating slot 1 then.
A kind of inorganic ultrafiltration oily water separating equipment, concrete structure as shown in Figure 1, this equipment is made up of circulating slot 1, hyperfiltration equipment a 2, hyperfiltration equipment b 3 and circulating pump 4; Wherein, the top of circulating slot 1 is provided with first input port 11, second input port 12 and delivery outlet 13, and inside is provided with heater 14; Hyperfiltration equipment a 2 bottoms are provided with charging aperture a 21, and the top is provided with dense water out a 22, and sidewall is provided with and produces mouth of a river a 23 and produce mouth of a river c 24, and inside is provided with inorganic ceramic membrane; Hyperfiltration equipment b 3 bottoms are provided with charging aperture b 31, and the top is provided with dense water out b 32, and sidewall is provided with and produces mouth of a river b 33 and produce mouth of a river d 34, and inside is provided with inorganic ceramic membrane; Described hyperfiltration equipment a 2 is with after circulating pump 4 is connected, and is in parallel with hyperfiltration equipment b 3 again, links to each other with delivery outlet 13 with first input port 11 of circulating slot 1 then.
Claims (4)
1. inorganic ultrafiltration oily water separating equipment, it is characterized in that: described equipment is by circulating slot (1), hyperfiltration equipment a(2), hyperfiltration equipment b(3) and circulating pump (4) form;
---wherein, the top of circulating slot (1) is provided with first input port (11), second input port (12) and delivery outlet (13);
---described hyperfiltration equipment a(2) bottom is provided with charging aperture a(21), the top is provided with dense water out a(22), sidewall is provided with and produces mouth of a river a(23), inside is provided with inorganic ceramic membrane;
---described hyperfiltration equipment b(3) bottom is provided with charging aperture b(31), the top is provided with dense water out b(32), sidewall is provided with and produces mouth of a river b(33), inside is provided with inorganic ceramic membrane;
---described hyperfiltration equipment a(2) with after circulating pump (4) is connected, again with hyperfiltration equipment b(3) in parallel, link to each other with delivery outlet (13) with first input port (11) of circulating slot (1) then.
2. according to the described inorganic ultrafiltration oily water separating equipment of claim 1, it is characterized in that: described circulating slot (1) inside is provided with heater (14).
3. according to the described inorganic ultrafiltration oily water separating equipment of claim 1, it is characterized in that: sidewall described hyperfiltration equipment a(2) is provided with two and produces the mouth of a river.
4. according to the described inorganic ultrafiltration oily water separating equipment of claim 1, it is characterized in that: sidewall described hyperfiltration equipment b(3) is provided with two and produces the mouth of a river.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201258756U CN202070289U (en) | 2011-04-26 | 2011-04-26 | Inorganic ultra-filtration oil and water separation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201258756U CN202070289U (en) | 2011-04-26 | 2011-04-26 | Inorganic ultra-filtration oil and water separation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202070289U true CN202070289U (en) | 2011-12-14 |
Family
ID=45108405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201258756U Expired - Fee Related CN202070289U (en) | 2011-04-26 | 2011-04-26 | Inorganic ultra-filtration oil and water separation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202070289U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102701553A (en) * | 2012-06-26 | 2012-10-03 | 清华大学 | Solid-liquid separation device for organic carbon sources in excess sludge |
| CN102910706A (en) * | 2012-10-16 | 2013-02-06 | 中国石油化工股份有限公司 | Method and device for performing precise processing to thin interbed low permeability oilfield produced water through ceramic membranes |
| CN104307381A (en) * | 2014-10-11 | 2015-01-28 | 中国农业科学院油料作物研究所 | Inorganic film and device and method for recovering solvents in mixed oil |
| CN104402132A (en) * | 2014-09-28 | 2015-03-11 | 中石化石油工程设计有限公司 | Equipment and method for fine filtering of ultra-low permeability oil field A1-grade reinjection water |
| CN104784999A (en) * | 2015-03-31 | 2015-07-22 | 韶关市贝瑞过滤科技有限公司 | Jet-type filtering equipment and application method thereof |
| CN104837776A (en) * | 2012-11-13 | 2015-08-12 | 艾威拉股份公司 | Purification of oil-polluted water and device suitable therefor |
| CN108031291A (en) * | 2017-12-11 | 2018-05-15 | 安徽霍尔斯工程技术有限公司 | A kind of multifunctional membrane filtration system |
| CN109052571A (en) * | 2018-09-13 | 2018-12-21 | 上海科琅膜科技有限公司 | A kind of processing equipment for emulsifying wastewater |
-
2011
- 2011-04-26 CN CN2011201258756U patent/CN202070289U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102701553A (en) * | 2012-06-26 | 2012-10-03 | 清华大学 | Solid-liquid separation device for organic carbon sources in excess sludge |
| CN102910706A (en) * | 2012-10-16 | 2013-02-06 | 中国石油化工股份有限公司 | Method and device for performing precise processing to thin interbed low permeability oilfield produced water through ceramic membranes |
| CN104837776A (en) * | 2012-11-13 | 2015-08-12 | 艾威拉股份公司 | Purification of oil-polluted water and device suitable therefor |
| US10358360B2 (en) | 2012-11-13 | 2019-07-23 | Eviola S.A. | Purification of oil-polluted water and device suitable therefor |
| CN104402132A (en) * | 2014-09-28 | 2015-03-11 | 中石化石油工程设计有限公司 | Equipment and method for fine filtering of ultra-low permeability oil field A1-grade reinjection water |
| CN104307381A (en) * | 2014-10-11 | 2015-01-28 | 中国农业科学院油料作物研究所 | Inorganic film and device and method for recovering solvents in mixed oil |
| CN104307381B (en) * | 2014-10-11 | 2016-05-25 | 中国农业科学院油料作物研究所 | The retracting device of solvent and method in a kind of inoranic membrane and miscella |
| CN104784999A (en) * | 2015-03-31 | 2015-07-22 | 韶关市贝瑞过滤科技有限公司 | Jet-type filtering equipment and application method thereof |
| CN108031291A (en) * | 2017-12-11 | 2018-05-15 | 安徽霍尔斯工程技术有限公司 | A kind of multifunctional membrane filtration system |
| CN109052571A (en) * | 2018-09-13 | 2018-12-21 | 上海科琅膜科技有限公司 | A kind of processing equipment for emulsifying wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202070289U (en) | Inorganic ultra-filtration oil and water separation equipment | |
| CN100572306C (en) | Oil-contained waste water treatment system that a kind of saltiness is high and technology | |
| CN102690003A (en) | Device and method for performing advanced treatment on citric acid waste water through dual membrane process | |
| CN102020385A (en) | Method for treating electroplate rinsing wastewater | |
| CN201610402U (en) | Recycling and deep treatment device for electronic electroplating wastewater | |
| CN102633378A (en) | Method and system for recycling catalyst from coal chemical liquid waste | |
| CN101767890B (en) | Method applying membrane combining process to dispose garbage percolate | |
| CN105384216A (en) | Separating device of ceramic membrane for waste liquid cycling filtration | |
| CN103880206B (en) | The heavy metal wastewater thereby deep treatment method of the dynamic nucleation flocculation of mud | |
| CN202272789U (en) | Nickel sulphamate electroplating wastewater recovery and utilization system | |
| CN210286943U (en) | Geothermal tail water desalination recycling treatment system | |
| CN204569594U (en) | Efficient embrane method strainer Sewage treatment systems | |
| CN207056106U (en) | A kind of small-sized liquid hazardous waste minimizing film concentrator | |
| CN203253363U (en) | External tubular membrane filter device | |
| CN201200865Y (en) | High-recovery rate hyperfiltration device | |
| CN202080990U (en) | Refinery waste water advanced-treatment system | |
| CN206156907U (en) | Sewage treatment system is arranged in thermal power plant's circulation | |
| CN102372624B (en) | Method for extracting sodium gulonate from sodium gulonate fermented liquid | |
| CN107502947A (en) | A kind of electroplating liquid purifying system and method | |
| CN108128847A (en) | A kind of film integrates the device of processing emulsifying liquid waste water | |
| CN208008514U (en) | A kind of integration emulsifying liquid waste water processing equipment | |
| CN206232567U (en) | The full embrane method waste water recycling processing unit of high-recovery | |
| CN205635230U (en) | Energy -efficient salt effluent disposal system that contains | |
| CN206437963U (en) | A kind of liquid waste processing direct discharge system | |
| CN203007055U (en) | Device for recycling wastewater containing heavy metal |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111214 Termination date: 20140426 |