CN209997464U - organic silicon hybrid membranes - Google Patents

organic silicon hybrid membranes Download PDF

Info

Publication number
CN209997464U
CN209997464U CN201920287905.XU CN201920287905U CN209997464U CN 209997464 U CN209997464 U CN 209997464U CN 201920287905 U CN201920287905 U CN 201920287905U CN 209997464 U CN209997464 U CN 209997464U
Authority
CN
China
Prior art keywords
layer
cellulose
silicone
ceramic support
adhered
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
Application number
CN201920287905.XU
Other languages
Chinese (zh)
Inventor
廖明佳
贺小兰
蒋清梅
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Chemical Industry Vocational College
Original Assignee
Chongqing Chemical Industry Vocational College
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chongqing Chemical Industry Vocational College filed Critical Chongqing Chemical Industry Vocational College
Priority to CN201920287905.XU priority Critical patent/CN209997464U/en
Application granted granted Critical
Publication of CN209997464U publication Critical patent/CN209997464U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The utility model discloses an organosilicon hybrid membrane, including ceramic support body 1, ceramic support body 1 left side has set gradually transition layer 2, cellulose layer 3, organosilicon layer 4, second cellulose layer 5, ceramic support body 1 right side has set gradually second transition layer 6, third cellulose layer 7, second organosilicon layer 8, second transition layer 6 is in through the coating mode adhesion ceramic support body 1 is last, third cellulose layer 7 is in through the coating mode adhesion on second transition layer 6, second organosilicon layer 8 is in through the coating mode adhesion on third cellulose layer 7 the permeability of this organosilicon hybrid membrane's water reaches 1.9 x 10‑13m3·m‑2·s‑1·Pa‑1Interception of salt ionsThe retention rate reaches 99.0 percent.

Description

organic silicon hybrid membranes
Technical Field
The utility model belongs to the membrane material field relates to kinds of organosilicon hybrid membranes.
Background
The aromatic polyamide composite membrane prepared by an interfacial polymerization method has the advantages of high desalination rate, large flux, organic solvent resistance and the like, and dominates the current reverse osmosis membrane market, but the aromatic polyamide membrane has poor pollution resistance, and particles, colloidal particles, organic matters and the like in water are adsorbed on the surface of the membrane to cause membrane pollution, wherein the organic matters and the microbial pollution are difficult to solve, the water flux of the membrane can be rapidly reduced, and the service life of the membrane is greatly shortened.
At the end of the twentieth century, excellent performance bridged organosilicon functional materials received much attention from , such organosilicon materials are typically bridged silsesquioxane (R' O)3Si–R–Si(OR’)3Is a silicon source precursor and is obtained by hydrolysis and polycondensation reaction. Compared with the traditional inorganic SiO based on tetraethyl orthosilicate (TEOS)2Compared with the material, the bridged organosilicon has the advantages of regular structure, adjustable pore channel type, size, surface property and the like. To increase the water permeability of the bridged organosilicon films, different methods have been used for modification. The affinity of the organic silicon membrane to water is obviously improved by regulating the structure of a bridging group, and the-CH 2-CH 2-group bridged by a BTESO network is replaced by introducing more polar-CH-and-C-bridge groups, so that the water permeability of the membrane is improved, but the salt rejection rate is reduced in the reverse osmosis process. Therefore, modifying the membrane material, improving the water permeability and the salt ion rejection rate of the membrane and breaking the mutual restriction relationship is the key point of the research in the field of reverse osmosis membranes at present.
SUMMERY OF THE UTILITY MODEL
In view of this, the utility model aims at providing kinds of organosilicon hybrid membranes, improve the water permeability and the salt ion retention rate of membrane simultaneously, for reaching above-mentioned purpose, the utility model provides a following technical scheme:
A silicone hybrid membrane, comprising a ceramic support (1), wherein the left side of the ceramic support (1) is sequentially provided with a transition layer (2), a cellulose layer (3), a silicone layer (4) and a second cellulose layer (5), the transition layer (2) is adhered to the ceramic support (1) through coating, the cellulose layer (3) is adhered to the transition layer (2) through coating, the silicone layer (4) is adhered to the cellulose layer (3) through coating, the second cellulose layer (5) is adhered to the silicone layer (4) through coating, the right side of the ceramic support (1) is sequentially provided with a second transition layer (6), a third cellulose layer (7) and a second silicone layer (8), the second transition layer (6) is adhered to the ceramic support (1) through coating, the third cellulose layer (7) is adhered to the second transition layer (6) through coating, and the second cellulose layer (7) is adhered to the second transition layer (8) through coating.
, the ceramic support body (1) is α -Al2O3The thickness of the ceramic film is 500-1000 nm.
, the transition layer (2) is silica sol, the second transition layer (6) is zirconium sol, and the thickness of the second transition layer is 50-100 nm.
, the organic silicon layer (4) and the second organic silicon layer (8) are bis (triethoxy silicon) methane films, and the thickness is 400-500 nm.
, the cellulose layer (3), the second cellulose layer (5) and the third cellulose layer (7) are hydroxypropyl cellulose films, and the thickness is 200-300 nm.
, the transition layer (2) and the second transition layer (6) are equal in thickness and are arranged equidistantly.
The utility model has the advantages that α -Al is used2O3The cellulose layer rich in hydroxyl is alternately and stably distributed in the organic silicon film layer in order, so that the hydrophilicity of the film can be effectively improved, the organic silicon layer can enable the film structure to be more compact, and the hybrid structure can simultaneously improve the pair of hybrid filmsThe permeability of water and the retention rate (apparent retention rate) of salt ions enable the permeability of water to reach 1.9 multiplied by 10-13m3·m-2·s-1·Pa-1The retention rate of salt ions reaches 99.0%.
Drawings
Fig. 1 is a schematic structural view of the present invention;
in the figure, 1 ceramic support, 2 th th transition layer, 3 rd th cellulose layer, 4 th th organosilicon layer, 5 th cellulose layer,
6 second transition layer, 7 third cellulose layer, 8 second silicone layer.
Fig. 2 is a long-term stability test chart of the silicone hybrid membrane.
Detailed Description
The preferred embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
Example 1
As shown in FIG. 1, the present invention provides embodiments, organosilicon hybrid membranes, including a ceramic support 1, wherein the left side of the ceramic support 1 is sequentially provided with a 0 th transition layer 2, a th cellulose layer 3, a th organosilicon layer 4, and a second cellulose layer 5, the th transition layer 2 is adhered to the ceramic support 1 by coating, the th cellulose layer 3 is adhered to the th transition layer 2 by coating, the th organosilicon layer 4 is adhered to the th cellulose layer 3 by coating, the second cellulose layer 5 is adhered to the th organosilicon layer 4 by coating, the right side of the ceramic support (1) is sequentially provided with a second transition layer 6, a third cellulose layer 7, and a second organosilicon layer 8, the second transition layer 6 is adhered to the ceramic support 1 by coating, the third cellulose layer 7 is adhered to the second transition layer 6 by coating, the second organosilicon layer 8 is adhered to the third cellulose layer 637 by coating, the ceramic support 1 is Al 1- 12O3A ceramic film, the thickness of which is 800nm, the thickness of the th transition layer 2 is silica sol, the thickness of the second transition layer 6 is zirconium sol, the thickness of which is 80nm, the thickness of the th organic silicon layer 4 and the thickness of the second organic silicon layer 8 are bis (triethoxysilyl) methane films, the thickness of which is 450nm, the thickness of the th cellulose layer 3,The second cellulose layer 5 and the third cellulose layer 7 are hydroxypropyl cellulose films and have a thickness of 250nm, and the th transition layer 2 and the second transition layer 6 are equal in thickness and equal in distance.
Example 2 film Performance testing
And (3) adopting a reverse osmosis device to carry out performance test on the membrane, conveying the raw material liquid to the membrane component by using a high-pressure constant flow pump at the flow rate of 10mL/min, and stirring the NaCl solution in the membrane component by using an external magnetic stirrer (the rotating speed is 300r/min) so as to reduce the concentration polarization effect. The experimental operating pressure is controlled by the membrane interception side through a precision back pressure valve, and the feed liquid on the interception side is circulated to the feed tank. Before testing, the reverse osmosis system is firstly operated for at least 5h to ensure that the membrane mass transfer process reaches a stable state, then sampling is carried out at intervals of preset time intervals, the quality of the penetrating fluid is measured, and the salt ion concentration in the penetrating fluid is analyzed.
The effect of the silicone hybrid membrane on the reverse osmosis desalination performance results: water permeability Lp of 1.9X 10-13,m3·m-2·s-1·Pa-1Apparent retention rate RobsThe content was 99.0%.
Example 3 Effect of operating time on reverse osmosis Performance
FIG. 2 is the long term stability of the organosilicon hybrid membrane during temperature change, from which it can be seen that the apparent rejection R of the membrane is obtained during 50h of continuous reverse osmosis desalinationobsThe change is not big, remains more than 97% throughout, shows that the network structure of membrane does not take place great change, proves the utility model discloses an organosilicon hybridization membrane has good hydrothermal stability.
Finally, although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims (6)

  1. A silicone hybrid membrane, which is characterized in that the membrane comprises a ceramic support (1), wherein the left side of the ceramic support (1) is sequentially provided with a transition layer (2), a cellulose layer (3), a silicone layer (4) and a second cellulose layer (5), the transition layer (2) is adhered to the ceramic support (1) in a coating mode, the cellulose layer (3) is adhered to the transition layer (2) in a coating mode, the silicone layer (4) is adhered to the cellulose layer (3) in a coating mode, the second cellulose layer (5) is adhered to the silicone layer (4) in a coating mode, the right side of the ceramic support (1) is sequentially provided with a second transition layer (6), a third cellulose layer (7) and a second silicone layer (8), the second transition layer (6) is adhered to the ceramic support (1) in a coating mode, the third cellulose layer (7) is adhered to the second silicone layer (7) in a coating mode, and the second transition layer (6) is adhered to the second silicone layer (8) in a coating mode.
  2. 2. The hybrid silicone membranes according to claim 1, wherein the ceramic support (1) is α -Al2O3The thickness of the ceramic film is 500-1000 nm.
  3. 3. The silicone hybrid film according to claim 1, wherein the transition layer (2) and the second transition layer (6) are SiO2–ZrO2The thickness of the sol is 50-100 nm.
  4. 4. The kinds of silicone hybrid membranes according to claim 1, wherein the st and second silicone layers (4, 8) are bis (triethoxysilyl) methane membranes with a thickness of 400-500 nm.
  5. 5. The kinds of silicone hybrid membranes according to claim 1, wherein the th cellulose layer (3), the second cellulose layer (5), and the third cellulose layer (7) are hydroxypropyl cellulose films with a thickness of 200-300 nm.
  6. 6. The silicone hybrid film according to claim 1, wherein the transition layer (2) and the second transition layer (6) are equal in thickness and are disposed equidistantly.
CN201920287905.XU 2019-03-07 2019-03-07 organic silicon hybrid membranes Expired - Fee Related CN209997464U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920287905.XU CN209997464U (en) 2019-03-07 2019-03-07 organic silicon hybrid membranes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920287905.XU CN209997464U (en) 2019-03-07 2019-03-07 organic silicon hybrid membranes

Publications (1)

Publication Number Publication Date
CN209997464U true CN209997464U (en) 2020-01-31

Family

ID=69301111

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201920287905.XU Expired - Fee Related CN209997464U (en) 2019-03-07 2019-03-07 organic silicon hybrid membranes

Country Status (1)

Country Link
CN (1) CN209997464U (en)

Similar Documents

Publication Publication Date Title
Liu et al. Pervaporation membrane materials: Recent trends and perspectives
Yu et al. Fabrication of a low‐cost nano‐SiO2/PVC composite ultrafiltration membrane and its antifouling performance
Xu et al. Development of robust organosilica membranes for reverse osmosis
Xu et al. Reverse osmosis performance of organosilica membranes and comparison with the pervaporation and gas permeation properties
Bian et al. Effect of nano-TiO2 particles on the performance of PVDF, PVDF-g-(maleic anhydride), and PVDF-g-poly (acryl amide) membranes
CN111773928B (en) Aerogel composite membrane and preparation method and application thereof
Li et al. Pinning down the water transport mechanism in graphene oxide pervaporation desalination membranes
Liu et al. Influence of graphene oxide sheets on the pore structure and filtration performance of a novel graphene oxide/silica/polyacrylonitrile mixed matrix membrane
CN114073898B (en) Forward osmosis membrane with two-dimensional MOFs as intermediate layer and preparation method thereof
KR20150064456A (en) Organic/inorganic hybrid membrane for fouling resistance, method of preparing membrane for fouling resistance, and water treatment device including said membrane
JP5837480B2 (en) Composite semipermeable membrane
Wei et al. SiO2‐modified nanocomposite nanofiltration membranes with high flux and acid resistance
JP2016144798A (en) Oxygen enrichment membrane and production method of oxygen enrichment membrane
CN107824060A (en) A kind of polyhedral oligomeric silsesquioxane composite nanometer filter membrane preparation method
JP6196178B2 (en) Separation membrane for gas treatment containing acid gas and method for producing separation membrane for gas treatment containing acid gas
Aoyama et al. Nanogradient hydrophilic/hydrophobic organosilica membranes developed by atmospheric-pressure plasma to enhance pervaporation performance
CN209997464U (en) organic silicon hybrid membranes
Xu et al. Co-assembly of soluble metal–organic polyhedrons for high-flux thin-film nanocomposite membranes
Wang et al. Toward explicit anion transport nanochannels for osmotic power energy using positive charged MXene membrane via amination strategy
CN112933981B (en) Ethanol selective pervaporation composite membrane, preparation method thereof and method for separating and purifying ethanol
Zhang et al. Development of highly water-permeable robust PSQ-based RO membranes by introducing hydroxyethylurea-based hydrophilic water channels
Zhang et al. Chitosan/polyvinylpyrrolidone‐silica hybrid membranes for pervaporation separation of methanol/ethylene glycol azeotrope
Liu et al. Cross-flow deposited hydroxyethyl cellulose (HEC)/polypropylene (PP) thin-film composite membrane for aqueous and non-aqueous nanofiltration
Liang et al. Preparation of dopamine/Ag‐modified graphene oxide/polysulfone/poly (vinylidene fluoride) ultrafiltration membrane with hydrophilic and antibacterial dual function
Zhan et al. Breakthroughs on tailoring membrane materials for ethanol recovery by pervaporation

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
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: 20200131

Termination date: 20210307