CN201186181Y - Ceramic film filter - Google Patents
Ceramic film filter Download PDFInfo
- Publication number
- CN201186181Y CN201186181Y CNU2008200530703U CN200820053070U CN201186181Y CN 201186181 Y CN201186181 Y CN 201186181Y CN U2008200530703 U CNU2008200530703 U CN U2008200530703U CN 200820053070 U CN200820053070 U CN 200820053070U CN 201186181 Y CN201186181 Y CN 201186181Y
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- Prior art keywords
- ceramic membrane
- membrane filter
- filter
- chamber
- face plate
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Abstract
The utility model discloses a ceramic membrane filter, which comprises a tube body, a filter unit, a liquid inlet, a liquid outlet, a sewage outlet and a trash-cleaning hole. The utility model is characterized in that the filter unit is formed by ceramic membrane filter pipes whose bore diameters are 1-100um and which are connected in parallel, the ceramic membrane filter pipes are fixed between an upper figure pattern card and a lower figure pattern card, the tube body is divided into three chambers by the upper figure pattern card and the lower figure pattern card, wherein the upper layer is an oil collection chamber, the middle layer is a filter chamber, and the lower layer is a slag chamber, wherein the liquid inlet and an oil drain hole are arranged in the oil collection chamber, a liquid outlet is arranged on the outer wall at the bottom of the filter chamber, and the trash-cleaning hole and the sewage outlet are arranged in the slag chamber. The utility model has the advantages of simple structure, convenient processing, installation and employment, big filter area, big water handling capacity, easy recoiling, excellent quality of filter water, not easy clogging and long service span, which can be applied to process oil-containing or macromolecular sewage water in petrifaction, metallurgy, electric power, chemical industry, chemical fertilizers, pharmacy, municipality and the like.
Description
Technical field
The utility model relates to a kind of wastewater treatment equipment.Specifically a kind of ceramic membrane filter device.
Background technology
The filter of existing wastewater treatment generally comprises cylindrical shell, filter element, and inlet, liquid outlet, sewage draining exit, soil cleaning port, its filter element mainly adopts sandstone, and its shortcoming is that filtering velocity is slow, water outlet is little, and poor filtration effect easily hardens, and easily causes line clogging; Also have and adopt screen pack, filter cloth or with filtering materials such as activated carbon, these kinds filter element is not long common service life, often change; Especially can only be applicable to the filtration of larger particles material, range of application is little, and is not suitable for the filtration of oil-containing or other macromolecular substances.
The utility model content
The purpose of this utility model is to overcome above shortcoming, provides a kind of filter area big, and treating capacity is big, easily recoil, the filtering water quality is good, is not easy to stop up, long service life, applied range can be used for the ceramic membrane filter device that oil-containing or other macromolecular substances filter.
The technical solution of the utility model is: comprise cylindrical shell, filter element, inlet, liquid outlet, sewage draining exit, soil cleaning port is characterized in that, described filter element is that the ceramic membrane filter tube of 1-100 μ m is formed side by side by the aperture, described ceramic membrane filter tube is fixed between upper face plate and the lower face plate, and upper face plate and lower face plate are separated into three chambers with cylindrical shell, and the upper strata is a gathering room, the middle level is the filter chamber, and lower floor is a cinder pocket; In gathering room, be provided with inlet and oil drain out, on the outer wall of bottom, filter chamber, be provided with liquid outlet, in cinder pocket, be provided with soil cleaning port and sewage draining exit.
Described ceramic membrane filter tube is to make matrix by porous ceramic pipe, and table side face is compounded with the inorganic ceramic membrane working lining of one deck aperture 1-100 μ m in it.
The blowdown coil pipe that is communicated with sewage draining exit is housed in the described cinder pocket.
Be provided with the steam soaking pipe in the described gathering room.
Be respectively equipped with inspection manhole in described gathering room, filter chamber, the cinder pocket.
The course of work: industrial wastewater enters gathering room from inlet, entrained oil is all accumulated in the top layer of gathering room, gather when a certain amount of, discharge by oil drain out, waste water arrives the filter chamber through the micropore permeation of ceramic membrane filter tube under external pressure, discharges through liquid outlet; Impurity then sinks in the cinder pocket, gathers when a certain amount of, is discharged by sewage draining exit; Operation certain hour rear impurity can influence filter efficiency attached to the surface of ceramic membrane filter tube, carry out backwash, and promptly backwashing water advances, goes out from inlet from liquid outlet.
The utility model is simple in structure, processing, easy to install and use; Especially filter area is big, treating capacity big, easily recoil, the filtering water quality is good, be not easy obstruction; Long service life can be applicable to oil-containing or the processing of molecule sewage greatly such as petrochemical industry, metallurgy, electric power, chemical industry, chemical fertilizer, pharmacy, municipal administration.
Description of drawings
Accompanying drawing is the utility model one example structure schematic diagram.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
Embodiment 1: steel plant's limit casting secondary cooling water is handled
With reference to accompanying drawing: present embodiment comprises cylindrical shell 1, the 80-800 root hole is housed in cylindrical shell 1 directly is the ceramic membrane filter tube 2 of 1-100 μ m, ceramic membrane filter tube is fixed between upper face plate 3 and the lower face plate 4, upper face plate and lower face plate are separated into three chambers with cylindrical shell, the upper strata is a gathering room 5, and the middle level is filter chamber 6, and lower floor is a cinder pocket 7; Be provided with inlet 8 and oil drain out 9 in gathering room, liquid outlet 10 is located on the outer wall of bottom, filter chamber, is provided with soil cleaning port 11 and sewage draining exit 12 in cinder pocket, and oil content is 100-300mg/L in the former water, and the suspension in the former water is 150-800mg/L.Handling the back oil content is 2-30mg/L, and handling the back suspension content is 5-100mg/L.
Embodiment 2: coke-oven plant's remained ammonia and rich solution water treatment
Increase the steam soaking pipe at gathering room as different from Example 1.
Claims (5)
1. ceramic membrane filter device, comprise cylindrical shell, filter element, inlet, liquid outlet, sewage draining exit, soil cleaning port, it is characterized in that described filter element is that the ceramic membrane filter tube of 1-100 μ m is formed side by side by the aperture, described ceramic membrane filter tube is fixed between upper face plate and the lower face plate, upper face plate and lower face plate are separated into three chambers with cylindrical shell, the upper strata is a gathering room, and the middle level is the filter chamber, and lower floor is a cinder pocket; In gathering room, be provided with inlet and oil drain out, on the outer wall of bottom, filter chamber, be provided with liquid outlet, in cinder pocket, be provided with soil cleaning port and sewage draining exit.
2. ceramic membrane filter device according to claim 1 is characterized in that described ceramic membrane filter tube is to make matrix by porous ceramic pipe, and table side face is compounded with the inorganic ceramic membrane working lining of one deck aperture 1-100 μ m in it.
3. ceramic membrane filter device according to claim 1 is characterized in that, the blowdown coil pipe that is communicated with sewage draining exit is housed in the described cinder pocket.
4. ceramic membrane filter device according to claim 1 is characterized in that, is provided with the steam soaking pipe in the described gathering room.
5. ceramic membrane filter device according to claim 1 is characterized in that, is respectively equipped with inspection manhole in described gathering room, filter chamber, the cinder pocket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200530703U CN201186181Y (en) | 2008-05-06 | 2008-05-06 | Ceramic film filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200530703U CN201186181Y (en) | 2008-05-06 | 2008-05-06 | Ceramic film filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201186181Y true CN201186181Y (en) | 2009-01-28 |
Family
ID=40309196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200530703U Expired - Fee Related CN201186181Y (en) | 2008-05-06 | 2008-05-06 | Ceramic film filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201186181Y (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225263A (en) * | 2011-04-15 | 2011-10-26 | 青岛大学 | Dismountable cross-flow type filter for liquid with high viscosity |
| CN102515312A (en) * | 2011-12-21 | 2012-06-27 | 北京大学 | Composite ceramic membrane-based filtration method and filtration device for cooling water produced in steel making and continuous casting |
| CN103112972A (en) * | 2013-03-17 | 2013-05-22 | 惠州市银嘉环保科技有限公司 | Ceramic membrane liquid suction tube |
| CN103949100A (en) * | 2013-06-21 | 2014-07-30 | 天津滨瀚环保科技发展有限公司 | Ceramic filter apparatus for separating magnesium hydrate solution, and process thereof |
| CN105174526A (en) * | 2015-07-14 | 2015-12-23 | 江苏华杉环保科技有限公司 | Ceramic membrane filter |
| CN106422468A (en) * | 2016-10-31 | 2017-02-22 | 刘国敏 | Cross-flow backflushing ceramic membrane liquid ammonia deoiling filtering device |
| CN107140778A (en) * | 2017-06-30 | 2017-09-08 | 江苏彬鹏环保有限公司 | A kind of oiliness sewage treatment equipment |
| CN110604956A (en) * | 2019-08-28 | 2019-12-24 | 广西天源新能源材料有限公司 | A precision filter for production of lithium hydroxide monohydrate |
| CN112125481A (en) * | 2020-09-29 | 2020-12-25 | 中建水务环保有限公司 | Multistage ceramic membrane rural sewage treatment plant |
-
2008
- 2008-05-06 CN CNU2008200530703U patent/CN201186181Y/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225263A (en) * | 2011-04-15 | 2011-10-26 | 青岛大学 | Dismountable cross-flow type filter for liquid with high viscosity |
| CN102225263B (en) * | 2011-04-15 | 2014-05-21 | 青岛大学 | Dismountable cross-flow type filter for liquid with high viscosity |
| CN102515312A (en) * | 2011-12-21 | 2012-06-27 | 北京大学 | Composite ceramic membrane-based filtration method and filtration device for cooling water produced in steel making and continuous casting |
| CN103112972A (en) * | 2013-03-17 | 2013-05-22 | 惠州市银嘉环保科技有限公司 | Ceramic membrane liquid suction tube |
| CN103112972B (en) * | 2013-03-17 | 2014-03-26 | 惠州市银嘉环保科技有限公司 | Ceramic membrane liquid suction tube |
| CN103949100B (en) * | 2013-06-21 | 2015-10-07 | 天津滨瀚环保科技发展有限公司 | Be separated ceramic filter devices and the technique of magnesium hydroxide solution |
| CN103949100A (en) * | 2013-06-21 | 2014-07-30 | 天津滨瀚环保科技发展有限公司 | Ceramic filter apparatus for separating magnesium hydrate solution, and process thereof |
| CN105174526A (en) * | 2015-07-14 | 2015-12-23 | 江苏华杉环保科技有限公司 | Ceramic membrane filter |
| CN106422468A (en) * | 2016-10-31 | 2017-02-22 | 刘国敏 | Cross-flow backflushing ceramic membrane liquid ammonia deoiling filtering device |
| CN107140778A (en) * | 2017-06-30 | 2017-09-08 | 江苏彬鹏环保有限公司 | A kind of oiliness sewage treatment equipment |
| CN110604956A (en) * | 2019-08-28 | 2019-12-24 | 广西天源新能源材料有限公司 | A precision filter for production of lithium hydroxide monohydrate |
| CN112125481A (en) * | 2020-09-29 | 2020-12-25 | 中建水务环保有限公司 | Multistage ceramic membrane rural sewage treatment plant |
| CN112125481B (en) * | 2020-09-29 | 2021-04-27 | 中建水务环保有限公司 | Multistage ceramic membrane rural sewage treatment plant |
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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: 20090128 Termination date: 20140506 |