CN101653700B - Membrane module supported by rigid rotatable barrel body and working under supergravity condition - Google Patents
Membrane module supported by rigid rotatable barrel body and working under supergravity condition Download PDFInfo
- Publication number
- CN101653700B CN101653700B CN 200810054213 CN200810054213A CN101653700B CN 101653700 B CN101653700 B CN 101653700B CN 200810054213 CN200810054213 CN 200810054213 CN 200810054213 A CN200810054213 A CN 200810054213A CN 101653700 B CN101653700 B CN 101653700B
- Authority
- CN
- China
- Prior art keywords
- membrane module
- membrane
- barrel body
- supported
- rotatable barrel
- 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
- 239000012528 membrane Substances 0.000 title claims abstract description 131
- 239000007788 liquid Substances 0.000 claims abstract description 77
- 239000000463 material Substances 0.000 claims description 50
- 238000009792 diffusion process Methods 0.000 claims description 33
- 230000004888 barrier function Effects 0.000 claims description 32
- 238000000034 method Methods 0.000 claims description 20
- 239000000835 fiber Substances 0.000 claims description 12
- 239000004677 Nylon Substances 0.000 claims description 9
- 239000003822 epoxy resin Substances 0.000 claims description 9
- 229920001778 nylon Polymers 0.000 claims description 9
- 229920000647 polyepoxide Polymers 0.000 claims description 9
- 239000004033 plastic Substances 0.000 claims description 6
- 229920003023 plastic Polymers 0.000 claims description 6
- 238000009795 derivation Methods 0.000 claims description 5
- 238000009954 braiding Methods 0.000 claims description 4
- 239000004744 fabric Substances 0.000 claims description 3
- 239000003365 glass fiber Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000005245 sintering Methods 0.000 claims description 3
- 239000002131 composite material Substances 0.000 claims description 2
- 239000007769 metal material Substances 0.000 claims description 2
- 238000000926 separation method Methods 0.000 abstract description 31
- 230000000694 effects Effects 0.000 abstract description 20
- 230000010287 polarization Effects 0.000 abstract description 14
- 238000005516 engineering process Methods 0.000 abstract description 8
- 230000002411 adverse Effects 0.000 abstract description 5
- 239000002994 raw material Substances 0.000 abstract description 5
- 230000008901 benefit Effects 0.000 abstract description 4
- 230000008569 process Effects 0.000 description 10
- 239000002904 solvent Substances 0.000 description 5
- 230000005484 gravity Effects 0.000 description 4
- 230000002787 reinforcement Effects 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000002950 deficient Effects 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000012925 reference material Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention relates to a membrane module supported by a rigid rotatable barrel body and working under a supergravity condition, which consists of a membrane module shell, a raw material liquid distributor, a separation membrane and a bubble light liquid guiding device, wherein one end of the separation membrane is fixed on the side wall of the membrane module shell; the outside of the side wall of the membrane module shell is provided with a groove corresponding to the end part of the separation membrane; the groove is communicated with the inner cavity of the separation membrane; the other end of the separation membrane is a closed end capable of freely moving; the outer edge of an upper end cover of the membrane module shell is provided with a chamfer; the outer edge of a lower end cover of the membrane module is provided with a concentrated solution outlet; the center of the membrane module shell is fixed with the raw material liquid distributor; the center of the upper end of the raw material liquid distributor is provided with the bubble light liquid guiding device; the side wall of the bubble light liquid guiding device is provided with a raw material liquid guiding outlet; and the outside of the side wall of the bubble light liquid guiding device is provided with a bubble light liquid guiding groove. The membrane module has the advantage that the membrane separation technology is effectively combined with the supergravity technology to effectively overcome adverse effects brought by concentration difference polarization in the membrane separation process so as to improve the effect of membrane separation.
Description
Technical field:
The invention belongs to a kind of membrane module, particularly a kind ofly can carry out under the hypergravity condition that film separates, and rely on rigid rotatable barrel body to make the membrane module that supports.
Background technology:
Membrane separation technique has been widely used in the fields such as chemical industry, medicine, food, the energy, environmental protection at present because of advantages such as it is efficient, energy-conservation, the easy amplifications of process.Yet since concentration polarization in the film separation process, the existence of the aspect problems such as film pollution, and applying of membrane separation technique has been subject to a lot of restrictions, although people have researched and developed a lot of methods and attempted to address the above problem, is not very desirable.For example with the film separation process of pressure as driving force, concentration difference extreme difference phenomenon ubiquity.Because the concentration of the film separating layer outer surface material that plays a crucial role in the film separation process during generation of concentration difference extreme difference is higher than the main body concentration of material far away, brought a lot of adverse influences therefore for the film separation process, specifically have: 1, the rejection of solute reduces (being used for desalinization such as anti-seepage membrane) in a lot of film separation processes.2, the film permeation flux reduces, and the production capacity of device descends.3, the osmotic pressure on the membrane interface increases, and must improve feed pressure or improve the feeding liquid flow velocity for improving permeation flux, thereby cause the raising of energy consumption.4, film pollutes aggravation, and membrane lifetime descends.5. the film concentration rate descends, and is difficult to obtain the high concentration product.In order to reduce concentration polarization and concentration polarization adverse effect, people have proposed many solutions, and be applied to the film separation process, but practice show these methods all exist to some extent such or such defective as: 1. energy consumption strengthens and (to increase flow velocity method, turbulence promoter is installed, impulse method, paddling process, improve the diffusion coefficient method, rotation reinforcement etc.) 2. the packed density of film is low.3. the film separating layer is easily impaired for elementary membrane area membrane module cost high (stuffing process is installed turbulator, the rotation reinforcement), and membrane lifetime reduces (turbulator being installed, stuffing process, rotation reinforcement)
Hypergravity refers to than terrestrial gravitation acceleration (9.8m/s
2) the suffered power of material (comprising gravitation or repulsive force) under the much bigger environment, utilize hypergravity the practical technique created of the principles of science be called high-gravity technology.The suffered power relevant with material mass of material has obtained great reinforcement thereby has strengthened greatly mass transfer effect under the hypergravity condition, this feature has great using value, the present hypergravity machine that produces Elevated Gravity by High Rotation Speed is at separating technology, and the aspects such as nano material preparation have obtained very successful application.
Film under the hypergravity separates, and is the technical process that film separates to be placed under the hypergravity condition carry out, and this is the combination of membrane separation technique and high-gravity technology.The data that can look at present in this regard seldom, in known consulting reference materials, there are Yan Jianmin " the rotating bed super gravity field device with tubular structure " (number of applying for a patent 03115674.6) and above-mentioned 2 patents of " centrifugal rotation hypergravity---membrane separation technique " (number of applying for a patent 03100089.4) membrane separation technique and high-gravity technology to be carried out combination, and proposed specific embodiment.But carefully analyze research and be not difficult to find that above-mentioned 2 patents are not mentioned solves operation principle and the solution that on film separation process affects great concentration polarization problem after above-mentioned 2 patents, in its structure and embodiment, also there is obvious defective, makes a concrete analysis of as follows:
Patent " the rotating bed super gravity field device with tubular structure " emphasizes it is characterized in that in its claim the axis of pipe and rotating shaft are perpendicular or parallel in 1., the two ends of pipe are fixed, in fact the coriolis force that when pipe is organic tubular membrane or hollow-fibre membrane and other flexible material films, is subject to owing to liquid in the membrane module, the effect of inertia of feed liquid all can will produce huge side force when revolving bed stopped in the startup formula to pipe, the axis of pipe can not be straight line under the effect of this side force, thereby just do not have vertical with rotating shaft yet, if by the fixing method in two ends keep its axis be straight line and with rotating shaft axis perpendicular or parallel so under the effect of above-mentioned side force film be easy to be broken and make the membrane separation device inefficacy.In its specification and accompanying drawing, can find in it is implemented, can't solve the discharge problem of dam thing or seepage remaining liquid.
Patent " centrifugal rotation hypergravity---membrane separation technique ", emphasize that in its claims " the separation driving force take rotary centrifugal force as film is the membrane separation technique of principle; comprise technical process and theoretical meter mark " is according to this principle in one's power, technical process and theoretical calculating all can't solve the great concentration polarization problem of impact in the film concentration process.2. the separating layer surface of the selected Flat Membrane of this patent all is towards rotating shaft axis, such film device when its work, concentration polarization that can aggravation film surface under the effect of centrifugal force.
Summary of the invention:
Purpose of the present invention just is to overcome above-mentioned the deficiencies in the prior art, and provide a kind of membrane module that relies on rigid rotatable barrel body to be supported on and to work under the hypergravity condition, this membrane module can overcome the adverse effect that the concentration polarization in the film separation process brings effectively, thereby has improved the effect that film separates.
Technical scheme of the present invention is: a kind of dependence rigid rotatable barrel body supports, and the membrane module of working under the hypergravity condition is characterized in that: be comprised of membrane module housing, material liquid distributor, diffusion barrier and bubble light liquid exporter; One end of diffusion barrier is fixed on the sidewall of membrane module housing, and the outside of membrane module housing sidewall has groove corresponding to the end of diffusion barrier, and groove is communicated with the inner chamber of diffusion barrier; The other end of diffusion barrier is the blind end that can move freely; The outward flange of membrane module housing upper end cover has a chamfering, membrane module bottom end cover outward flange has concentrated solution outlet, the central authorities of membrane module housing are fixed with the material liquid distributor, bubble light liquid exporter is equipped with in material liquid distributor upper end central authorities, its sidewall has the material liquid export mouth, and has bubble light liquid derivation groove in its sidewall outside.
The center line of above-mentioned membrane module housing can be installed perpendicular to horizontal plane, also can install horizontal by certain angle.
Above-mentioned diffusion barrier can be tubular film, hollow-fibre membrane and Flat Membrane.
Above-mentioned raw materials liquid export mouth is symmetrical along the membrane module central shaft, and shape is identical, and its center line can be identical with diametric(al), also can be at an angle.
The upper end cover inboard of above-mentioned membrane module housing is tapered.
The blind end of above-mentioned diffusion barrier can adopt the method for glue, epoxy resin, heating or sintering to seal.
Above-mentioned membrane module housing can be truncated cone-shaped, cylindrical; Its material can be epoxy resin, also can be the composite that epoxy resin and metal material or plastic nylon form.
The internal diameter of above-mentioned hollow-fibre membrane is between the 0.005-0.1mm.
The material of above-mentioned diffusion barrier can adopt has flexible organic film or inoranic membrane, also can adopt the screen cloth by wire, glass fibre, nylon yarn, chemical fibre, animal and plant fiber, silk braiding.
The separating layer surface of above-mentioned Flat Membrane is the turning cylinder axis dorsad, and the back side is pasted with thin plate, and the material of thin plate can be plastics, nylon sheet, metallic plate; Flat Membrane also can be fixed by the Flat Membrane support near an end of pivot center; The bus of Flat Membrane can be parallel with the central axis of membrane module, also can with the membrane module central axis at an angle.
Operation principle of the present invention is: same feed liquid its concentration behind solvent removal strengthens, strengthening its density with its concentration can change, the density of feed liquid can raise with the increasing of its concentration as a rule, the sedimentation of the sedimentation of high concentration feed liquid and solvent or diluent liquid is not all hindered settling, the solute granule interacts when being the high concentration material sedimentation, infall process is communality, the broad perspectives sedimentation.In the film separation process because concentration polarization, the feed concentration on film surface is far above the main body concentration of feed liquid, particularly the high concentration feed liquid can be along the identical of super gravity field or rightabout fast moving under the hypergravity condition in the existence of this density contrast so there are difference in the feed liquid density on film surface and the body density of feed liquid, thereby break away from the film surface, thereby and the additional space of abdicating because of the dense material disengaging of height film surface of new solvent or diluent liquid makes film surface feed concentration reduce (being the concentration polarization reduction).Constantly replenishing of the continuous disengaging of the high dense material in film surface and rare material, when reaching this weighing apparatus film surface and near say and form that a concentration is higher than feed liquid theme concentration but far below a comparatively stable area level of concentration polarization layered material liquid concentration under the non-hypergravity condition, the existence of this area level, be similar to Dynamic Membrane, separation process produces preferably effect to film.
Advantage of the present invention is: membrane separation technique and high-gravity technology are combined effectively, have higher feasibility, can effectively overcome the adverse effect that the concentration polarization in the film separation process brings, thereby improved the effect that film separates.
Description of drawings:
Fig. 1 is the main pseudosection of the present invention when adopting tubular film or Middle hollow fiber membrane film
Fig. 2 is the top plan view of Fig. 1.
Fig. 3 is the main pseudosection of the present invention when adopting Flat Membrane.
Fig. 4 is the top plan view of Fig. 3.
The specific embodiment:
Fig. 1, Fig. 2 are main pseudosection and the top plan view of diffusion barrier 3 membrane module when selecting tubular film or hollow-fibre membrane.Membrane module housing center line can be installed perpendicular to horizontal plane, also can install horizontal by certain angle.Membrane module housing 1 is fixedly mounted on rigid crust and rotates in the staving 4.
Fig. 3 and Fig. 4 be diffusion barrier when selecting Flat Membrane the master of membrane module look section and top plan view.The structure of membrane module and Fig. 1, membrane module structure shown in Figure 2 are roughly the same, the separating layer surface of Flat Membrane turning cylinder axis dorsad when mounted just, like this because the high dense material on the film surface that concentration polarization produces can be away from the film surface under the effect of centrifugal force, thereby reduce the impact of concentration polarization.The back side of Flat Membrane 16 is pasted with thin plate 15, and to accept dense feed liquid and it is derived, the material of thin plate can be plastics, nylon sheet, metallic plate.Flat Membrane also can be fixing by Flat Membrane support 14 near an end of pivot center, and is balanced with the spacing that guarantees film and film.The bus of Flat Membrane can be parallel with the central axis of membrane module, also can with the membrane module central axis at an angle.This Flat Membrane can be organic film and inoranic membrane, also can be the screen cloth by wire, glass fibre, nylon yarn, chemical fibre, animal and plant fiber, silk braiding.
The course of work of the present invention is: the membrane module housing that is installed in the rigid rotatable barrel body rotates with it when rigid rotatable barrel body rotates, and make material liquid in membrane module and the body thereof, seeing through liquid is under the overweight condition, material liquid enters the middle part cavity of material liquid distributor by the material liquid entrance, under the effect of the input pressure of material liquid and centrifugal force, material liquid enters membrane module housing inner chamber equably by the material liquid export mouth, contact with diffusion barrier, the material liquid pressure that produces in the effect of the input pressure of material liquid and centrifugal force and under the common material liquid pressure-acting that forms, the absciss layer that water in the material liquid or solvent see through diffusion barrier enters the inner chamber of diffusion barrier, and discharges through seeing through the liquid outlet under the effect of overbottom pressure behind centrifugal force and the film.Along with water or solvent constantly see through diffusion barrier, the concentration of surface, the separating layer surface material of diffusion barrier constantly increases, and its density also strengthens the density contrast of formation and main body material along with the increase of concentration.Under the effect of overweight centrifugal force dense material break away from the film surface and in the membrane module housing cavity edge concentrate, and discharge by concentrated solution outlet.Be lower than the light feed liquid of feed liquid main body concentration and bubble and under the effect of buoyancy, concentrate to material liquid distributor outward flange, and derive groove by the bubble light liquid and upwards compile through bubble light liquid export mouth and discharge.
Claims (10)
1. a membrane module that relies on rigid rotatable barrel body to be supported on and to work under the hypergravity condition is characterized in that: be comprised of membrane module housing, material liquid distributor, diffusion barrier and bubble light liquid exporter; One end of diffusion barrier is fixed on the sidewall of membrane module housing, and the outside of membrane module housing sidewall has groove corresponding to the end of diffusion barrier, and groove is communicated with the inner chamber of diffusion barrier; The other end of diffusion barrier is the blind end that can move freely; The outward flange of membrane module housing upper end cover has a chamfering, membrane module bottom end cover outward flange has concentrated solution outlet, the central authorities of membrane module housing are fixed with the material liquid distributor, bubble light liquid exporter is equipped with in material liquid distributor upper end central authorities, its sidewall has the material liquid export mouth, and has bubble light liquid derivation groove in its sidewall outside.
2. dependence rigid rotatable barrel body according to claim 1 is supported on the membrane module of working under the hypergravity condition, it is characterized in that: the central shaft of above-mentioned membrane module housing is installed perpendicular to horizontal plane, or installs horizontal by certain angle.
3. dependence rigid rotatable barrel body according to claim 1 is supported on the membrane module of working under the hypergravity condition, it is characterized in that: above-mentioned diffusion barrier is tubular film or hollow-fibre membrane or Flat Membrane.
4. dependence rigid rotatable barrel body according to claim 1 is supported on the membrane module of working under the hypergravity condition, it is characterized in that: the material liquid export mouth is symmetrical along the membrane module central shaft, shape is identical, and its center line is identical with diametric(al) or at an angle.
5. dependence rigid rotatable barrel body according to claim 1 is supported on the membrane module of working under the hypergravity condition, it is characterized in that: the upper end cover inboard of above-mentioned membrane module housing is tapered.
6. dependence rigid rotatable barrel body according to claim 1 is supported on the membrane module of working under the hypergravity condition, it is characterized in that: the blind end of above-mentioned diffusion barrier adopts the method for epoxy resin heating or sintering to seal.
7. dependence rigid rotatable barrel body according to claim 1 is supported on the membrane module of working under the hypergravity condition, it is characterized in that: above-mentioned membrane module housing is truncated cone-shaped or cylindrical; Its material composite that to be epoxy resin or epoxy resin form with metal material or plastic nylon.
8. dependence rigid rotatable barrel body according to claim 1 is supported on the membrane module of working under the hypergravity condition, it is characterized in that: the internal diameter of above-mentioned hollow-fibre membrane is between the 0.005-0.1mm.
According to claim 1 or 3 described dependence rigid rotatable barrel bodies be supported on the membrane module of working under the hypergravity condition, it is characterized in that: the material of above-mentioned diffusion barrier adopt have flexible organic film, inoranic membrane or by the screen cloth of a kind of braiding in wire, glass fibre, nylon yarn, the animal and plant fiber braiding.
10. dependence rigid rotatable barrel body according to claim 3 is supported on the membrane module of working under the hypergravity condition, it is characterized in that: the separating layer surface of above-mentioned Flat Membrane is the turning cylinder axis dorsad, and the back side is pasted with thin plate, and the material of thin plate adopts plastics or nylon sheet or metallic plate; Flat Membrane is fixed by the Flat Membrane support near an end of pivot center; The bus of Flat Membrane parallel with the central axis of membrane module or with the membrane module central axis at an angle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200810054213 CN101653700B (en) | 2008-08-22 | 2008-08-22 | Membrane module supported by rigid rotatable barrel body and working under supergravity condition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200810054213 CN101653700B (en) | 2008-08-22 | 2008-08-22 | Membrane module supported by rigid rotatable barrel body and working under supergravity condition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101653700A CN101653700A (en) | 2010-02-24 |
| CN101653700B true CN101653700B (en) | 2013-02-13 |
Family
ID=41708283
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200810054213 Expired - Fee Related CN101653700B (en) | 2008-08-22 | 2008-08-22 | Membrane module supported by rigid rotatable barrel body and working under supergravity condition |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101653700B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104785115B (en) * | 2014-01-16 | 2018-02-13 | 周志杰 | Membrane module is arranged on the hypergravity membrane separator rotated coaxially on auger conveyor with rotary drum differential |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1424134A (en) * | 2003-01-09 | 2003-06-18 | 邵显东 | Centrifugal rotary supergravity-membrane separating technology |
| CN1465428A (en) * | 2002-06-20 | 2004-01-07 | 杨时英 | Application method for membrane |
| CN2925588Y (en) * | 2006-02-16 | 2007-07-25 | 三达膜科技（厦门）有限公司 | Rotary-film apparatus |
-
2008
- 2008-08-22 CN CN 200810054213 patent/CN101653700B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1465428A (en) * | 2002-06-20 | 2004-01-07 | 杨时英 | Application method for membrane |
| CN1424134A (en) * | 2003-01-09 | 2003-06-18 | 邵显东 | Centrifugal rotary supergravity-membrane separating technology |
| CN2925588Y (en) * | 2006-02-16 | 2007-07-25 | 三达膜科技（厦门）有限公司 | Rotary-film apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101653700A (en) | 2010-02-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101700472B (en) | Rotary membrane separation device and application thereof | |
| CN108939922A (en) | A kind of rotary type ceramic film is separated by filtration technique and device | |
| CN204911253U (en) | Dull and stereotyped membrane separation device of rotation type disc | |
| CN204107190U (en) | Self-rotary gas-liquid separator | |
| CN208906018U (en) | A kind of rotary type ceramic film filtering separation device | |
| CN201244450Y (en) | Film component working under hypergravity condition | |
| CN102000508A (en) | Reciprocating rotation type feed liquid and film separation method and device | |
| CN201586483U (en) | Novel rotary membrane separation device | |
| CN108993784B (en) | Method and device for separating two-dimensional nano material by continuous supergravity | |
| CN203112587U (en) | Water treatment device of rotary flat membrane bioreactor | |
| CN101653700B (en) | Membrane module supported by rigid rotatable barrel body and working under supergravity condition | |
| CN110075717B (en) | Rotary type filtering structure, device and method for reducing pollution of ceramic membrane | |
| CN108926881B (en) | Device and method for separating two-dimensional nano material by continuous hypergravity percolation | |
| CN113209831A (en) | Flat ceramic membrane stack | |
| CN208022751U (en) | A kind of tablet forward osmosis membrane pond | |
| CN202015517U (en) | Composite high-efficiency phase separator | |
| CN105478011B (en) | A kind of intelligent modules pipe-type rotary-flow vibration microfiltration membranes processing equipment | |
| CN101940860B (en) | Gas-liquid segregating unit | |
| CN204727643U (en) | A kind of rotation film sewage filter device | |
| CN101890298B (en) | Rotating centrifugal hypergravity membrane separator | |
| CN211706108U (en) | Filtering separation device for chemical production | |
| CN113814062B (en) | Separation device and method for forest soil micro-plastic | |
| CN201454424U (en) | Film separator which working in the high gravity condition | |
| CN205620204U (en) | Combined water sample filter | |
| CN215311492U (en) | Single-double-pass bare vertical special-shaped bundle-shaped gas-liquid flow type hollow fiber membrane element |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: DALIAN SHENGREN ENERGY TECHNOLOGY DEVELOPMENT CO., Free format text: FORMER OWNER: ZHOU ZHIJIE Effective date: 20150122 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 300000 HEXI, TIANJIN TO: 116600 DALIAN, LIAONING PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20150122 Address after: 116600 bonded Building No. 1, Dongting Road, Dalian Free Trade Zone, Liaoning, 733F-18 Patentee after: Dalian Sheng Ren energy science and technology Development Co., Ltd Address before: 5 Tianjin city Hexi District District 300000 North 57-1103 Patentee before: Zhou Zhijie |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160705 Address after: 301800 Guangzhou Road, Tanggu District, Shiyan, No. 3, No. 4, building No. 102 Patentee after: Zhou Zhijie Address before: 116600 bonded Building No. 1, Dongting Road, Dalian Free Trade Zone, Liaoning, 733F-18 Patentee before: Dalian Sheng Ren energy science and technology Development Co., Ltd |
|
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zhou Zhijie Inventor after: Sun Yunfei Inventor before: Zhou Zhijie |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170327 Address after: 164100 Heihe city of Heilongjiang province Wudalianchi City Zhanhe Forestry Bureau five Committee five group No. 170 Patentee after: Sun Yunfei Address before: 301800 Guangzhou Road, Tanggu District, Shiyan, No. 3, No. 4, building No. 102 Patentee before: Zhou Zhijie |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130213 Termination date: 20170822 |