CN1476924A - Vibration bed membrane separator - Google Patents
Vibration bed membrane separator Download PDFInfo
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- CN1476924A CN1476924A CNA031282806A CN03128280A CN1476924A CN 1476924 A CN1476924 A CN 1476924A CN A031282806 A CNA031282806 A CN A031282806A CN 03128280 A CN03128280 A CN 03128280A CN 1476924 A CN1476924 A CN 1476924A
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- membrane separator
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- vibrated
- separator
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Abstract
The vibration bed membrane separator is fixed on the vibration bed to make the material implement vertical reciprocating movement passing through membrane direction with vibration bed, the invented advantage is lies in that the vibration bed can effectively control pollution of membrane surface of membrane separator, can make membrane separator high-effectively stable work for a long period. It is favorable for concentration of high concentration material, and can expand working range of membrane separator.
Description
Technical field:
The present invention relates to a kind of special equipment that utilizes membrane separating method, especially a kind of vibrated bed membrane separator.
Background technology:
Membrane separator is to utilize small aperture of face and charge, different molecular weight in gas or the liquid or different electrical material is implemented the equipment that separates.Membrane separator has been applied to the desalinization desalination at present; Drink, the medicinal water removal of impurity and bacterium; The industry high purity water removes charged ion; Remove thalline in the bioengineering zymotic fluid, concentrate macromolecular substances; Effective component extracting in pharmaceutical engineering, the daily use chemicals engineering; Be used for sewage purification and reuse in the environmental protection; The Alcohol Production that is used for high concentration, low energy consumption in the Alcohol Production; Atomic energy engineering is used for radioactive wastewater and separates radioactive substance etc.The purposes of membrane separator more and more widely, the someone proposes: " having grasped the tomorrow that membrane technology just equals to have grasped Chemical Engineering ".
But membrane separator will guarantee effective application in actual engineering, must solve the problem of film surface pollution.In engineering, a part of material passes face, and a part of material is held back by face.The material that is trapped can progressively form one deck concentration difference adsorption layer from inside to outside at face, and adsorption layer is thickeied to a certain degree, will influence the flow velocity of the material that passes film, and the operating efficiency of film progressively reduces, even the face obstruction can occur, and membrane separator is quit work.Therefore to guarantee that membrane separator works effectively, generation or thickness that must control concentration difference adsorption layer.
In existing film Engineering Design Manual and data document books about film, be of the influence of control concentration difference adsorption layer to the film operating efficiency, generally adopt following method:
1. regularly Chemical cleaning is removed adsorption layer, to keep the cleaning of film.Chemistry regularly cleans the continuous operation that has influenced membrane separator, and the membrane separator operating efficiency is descended, and the cost height that cleans, and inconvenient operation is cleaned effluent and also need be handled to solve the pollution to environment.
2. compressed air oppositely blows down the removal adsorption layer.Compressed air oppositely blows down, and also can influence the continuous operation of membrane separator, and the membrane separator operating efficiency is descended, and has increased processing cost, inconvenient operation.
3. form high-velocity stream at face.By flowing of face high speed object, adsorption layer is destroyed and takes out of membrane separator.To form high-velocity stream at face, need to strengthen the internal circulating load of material handling, therefore increase the consumption of membrane separator power, increase processing cost.And this method should not be used for the concentrating of object of high concentration.
4. change the operative orientation of film device, make the neuston direction of flow opposite, make face hold back colmatation zone and come off.This method makes the control of film system complicated, and valve is many, and the material that comes off might be sneaked into again in the material that needs to handle, and has increased the difficulty of handling.
Summary of the invention:
The purpose of this invention is to provide a kind of method for designing, can reduce of the influence of face adsorption layer dirt, make membrane separator energy continuous high-efficient rate, low-cost work film work.
Vibrated bed membrane separator of the present invention is made up of membrane separator and vibrated bed two parts of routine.Designing requirement is as follows:
1, conventional membrane separator is fixed on the vibrated bed, feed and exhaust tube connects with flexible pipe with outside, and membrane separator can be moved back and forth with vibrated bed.
2, vibrated bed produces under the external force effect that motor produces and moves back and forth, and reciprocating direction is vertical with the direction that material penetrates film, promptly does the reciprocating motion that vertical material penetrates the film direction with vibrated bed.
Membrane separator can be flat sheet membrane separator, tubular membrane separator, capillary-pipe film separator, rolling diaphragm separator and hollow fiber membrane separator.
Vibrated bed can be electric vibrating bed, pneumatic vibration bed and hydraulic vibration bed.The electric vibrating bed can be eccentric gravity self-excited vibration bed or eccentric ratio forced vibration bed.Vibrated bed can be designed to resonance bed and off-resonance bed.
When equipment moves back and forth, can produce shearing along the direction of motion between object that it is surperficial and the equipment as everyone knows, the direction of shearing is opposite with the direction of motion.When the reciprocating frequency of membrane separator and amplitude acquire a certain degree, when the reciprocal shearing that membrane separator is parallel to face is attached to the cohesive force of face material greater than dirt, can make dirt can not form the face that firm adhesion layer stops that object passes through, the established concentration difference adsorption layer of face is destroyed and come off.By the reciprocating mode of vibrated bed is the membrane separator of main control film surface contamination, can be described as the vibrated bed membrane separator.The vibrated bed membrane separator can be realized the work of film system long-term stability, and the high concentration that can be used for holding back material concentrates.
Advantage of the present invention is:
(1) the effectively pollution of controlling diaphragm separator face of vibrated bed makes the longer high-efficiency stable work of vibrated bed membrane separator;
(2) the vibrated bed membrane separator helps concentrating of high concentration material, has enlarged the range of application of membrane separator;
(3) consumption little, power of vibrated bed volume is few, utilizes the design of resonance bed, and power consumption is littler, can reduce the processing cost of membrane separator.
Description of drawings:
Further specify below in conjunction with embodiment and accompanying drawing.
Fig. 1 is the 1st a kind of organization plan schematic diagram of the present invention.
Fig. 2 is the 2nd a kind of organization plan schematic diagram of the present invention.
Fig. 3 is the 3rd a kind of organization plan schematic diagram of the present invention.
The specific embodiment:
See Fig. 1: flat sheet membrane separator 1 is horizontally disposed to be placed on the central shaft 2 of vertical ground, and central shaft can make face produce a horizontal shear at reciprocally swinging in the certain angle radially under the drive of motor 3 eccentric rod gears 4.Under this power effect, the schmutzband that deposits on horizontal face is reduced by the shearing force effect or destroys, and the work of membrane separator is reduced by the influence of dirt.
Embodiment 2:
See Fig. 2: rolling diaphragm separator 1 is vertically fixed on the vibrating grid 7, and vibrating grid is bearing on the spring 5, and material is from the saturating filmed passing tube of horizontal direction, and motor 3 also is fixed on the frame 7, is fixed with eccentric weight 6 on motor 3 rotating shafts.When motor 3 high speed rotaries, 6 pairs of vibrating grids of eccentric weight 7 produce the power of vibration up and down reciprocatingly, make vibrating grid 7 produce vibration up and down reciprocatingly, and vibrating grid 7 drives membrane separator 1 again and shakes and pump.Thereby the material that vertically arranged tubular membrane separator 1 face is adhered to is destroyed by shearing force, reduces or no longer influence the work of membrane separator.
Embodiment 3:
See Fig. 3: periosteum separator 1 is fixed on the vibrating grid 7, and vibrating grid 7 is bearing on the spring 5, and material is by the saturating filmed passing tube of horizontal direction.Motor 3 and spring 5 are fixed on the spring pedestal plate 8, pump by eccentric rod gear 4 pulling vibrating grids 7 and membrane separator 1, thereby make the material that adheres on membrane separator 1 membrane tube wall destroyed by shearing force, reduce or no longer influence the work of membrane separator.
Claims (5)
1, a kind of vibrated bed membrane separator comprises membrane separator and vibrated bed two partly, and it is characterized in that: membrane separator is fixed on the vibrated bed, does the reciprocating motion that vertical material penetrates the film direction with vibrated bed.
2, vibrated bed membrane separator according to claim 1 is characterized in that: membrane separator can be flat sheet membrane separator, tubular membrane separator, capillary-pipe film separator, rolling diaphragm separator and hollow fiber membrane separator.
3, vibrated bed membrane separator according to claim 1 is characterized in that: vibrated bed can be electric vibrating bed, pneumatic vibration bed and hydraulic vibration bed.
4, vibrated bed membrane separator according to claim 3 is characterized in that: the electric vibrating bed can be eccentric gravity self-excited vibration bed or eccentric ratio forced vibration bed.
5, vibrated bed membrane separator according to claim 3 is characterized in that: vibrated bed can be designed to resonance bed and off-resonance bed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CNA031282806A CN1476924A (en) | 2003-07-03 | 2003-07-03 | Vibration bed membrane separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA031282806A CN1476924A (en) | 2003-07-03 | 2003-07-03 | Vibration bed membrane separator |
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CN1476924A true CN1476924A (en) | 2004-02-25 |
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CNA031282806A Pending CN1476924A (en) | 2003-07-03 | 2003-07-03 | Vibration bed membrane separator |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102010030A (en) * | 2010-09-21 | 2011-04-13 | 惠州七芯膜净化环保有限公司 | Hollow fiber ultrafiltration membrane water purifier and cleaning method thereof |
CN104324620A (en) * | 2014-10-16 | 2015-02-04 | 国家海洋局第三海洋研究所 | Electric strengthening water filter |
CN104906956A (en) * | 2014-03-14 | 2015-09-16 | 昆山弱水无极环保科技有限公司 | Reciprocating-type membrane separation apparatus |
CN106975361A (en) * | 2017-04-14 | 2017-07-25 | 广东创源节能环保有限公司 | A kind of vertical rolled film vibrative filter |
CN110791341A (en) * | 2019-11-14 | 2020-02-14 | 青岛九堡能源装备科技有限公司 | Small-size marsh gas purifies and purification device |
CN113069928A (en) * | 2021-03-12 | 2021-07-06 | 东北农业大学 | Torsional vibration type hollow fiber membrane filtering device |
-
2003
- 2003-07-03 CN CNA031282806A patent/CN1476924A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102010030A (en) * | 2010-09-21 | 2011-04-13 | 惠州七芯膜净化环保有限公司 | Hollow fiber ultrafiltration membrane water purifier and cleaning method thereof |
CN104906956A (en) * | 2014-03-14 | 2015-09-16 | 昆山弱水无极环保科技有限公司 | Reciprocating-type membrane separation apparatus |
CN104324620A (en) * | 2014-10-16 | 2015-02-04 | 国家海洋局第三海洋研究所 | Electric strengthening water filter |
CN106975361A (en) * | 2017-04-14 | 2017-07-25 | 广东创源节能环保有限公司 | A kind of vertical rolled film vibrative filter |
CN110791341A (en) * | 2019-11-14 | 2020-02-14 | 青岛九堡能源装备科技有限公司 | Small-size marsh gas purifies and purification device |
CN110791341B (en) * | 2019-11-14 | 2020-11-17 | 江苏德瑞环保科技有限公司 | Small-size marsh gas purifies and purification device |
CN113069928A (en) * | 2021-03-12 | 2021-07-06 | 东北农业大学 | Torsional vibration type hollow fiber membrane filtering device |
CN113069928B (en) * | 2021-03-12 | 2022-10-28 | 东北农业大学 | Torsional vibration type hollow fiber membrane filtering device |
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