WO2019165840A1 - Forward osmosis membrane, and preparation method therefor - Google Patents
Forward osmosis membrane, and preparation method therefor Download PDFInfo
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- WO2019165840A1 WO2019165840A1 PCT/CN2018/124702 CN2018124702W WO2019165840A1 WO 2019165840 A1 WO2019165840 A1 WO 2019165840A1 CN 2018124702 W CN2018124702 W CN 2018124702W WO 2019165840 A1 WO2019165840 A1 WO 2019165840A1
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- support layer
- polysulfone
- solution
- forward osmosis
- osmosis membrane
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- 239000012528 membrane Substances 0.000 title claims abstract description 76
- 238000009292 forward osmosis Methods 0.000 title claims abstract description 63
- 238000002360 preparation method Methods 0.000 title abstract description 9
- 229920002492 poly(sulfone) Polymers 0.000 claims abstract description 90
- 238000000034 method Methods 0.000 claims abstract description 54
- 229920000642 polymer Polymers 0.000 claims abstract description 26
- 101001115830 Homo sapiens Prostate-associated microseminoprotein Proteins 0.000 claims abstract description 24
- 102100025013 Prostate-associated microseminoprotein Human genes 0.000 claims abstract description 24
- 239000011148 porous material Substances 0.000 claims abstract description 17
- 239000000243 solution Substances 0.000 claims description 69
- 239000004697 Polyetherimide Substances 0.000 claims description 42
- 229920001601 polyetherimide Polymers 0.000 claims description 42
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 36
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 15
- WZCQRUWWHSTZEM-UHFFFAOYSA-N 1,3-phenylenediamine Chemical compound NC1=CC=CC(N)=C1 WZCQRUWWHSTZEM-UHFFFAOYSA-N 0.000 claims description 10
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 claims description 10
- 239000012965 benzophenone Substances 0.000 claims description 10
- 229940018564 m-phenylenediamine Drugs 0.000 claims description 10
- UWCPYKQBIPYOLX-UHFFFAOYSA-N benzene-1,3,5-tricarbonyl chloride Chemical compound ClC(=O)C1=CC(C(Cl)=O)=CC(C(Cl)=O)=C1 UWCPYKQBIPYOLX-UHFFFAOYSA-N 0.000 claims description 9
- 239000007864 aqueous solution Substances 0.000 claims description 8
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 6
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 6
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- 238000003756 stirring Methods 0.000 claims description 4
- CJPIDIRJSIUWRJ-UHFFFAOYSA-N benzene-1,2,4-tricarbonyl chloride Chemical compound ClC(=O)C1=CC=C(C(Cl)=O)C(C(Cl)=O)=C1 CJPIDIRJSIUWRJ-UHFFFAOYSA-N 0.000 claims 1
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- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 16
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Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/002—Forward osmosis or direct osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/002—Forward osmosis or direct osmosis
- B01D61/0022—Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0016—Coagulation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0081—After-treatment of organic or inorganic membranes
- B01D67/009—After-treatment of organic or inorganic membranes with wave-energy, particle-radiation or plasma
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
- B01D69/105—Support pretreatment
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
- B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
- B01D69/1251—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction by interfacial polymerisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/02—Hydrophilization
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/34—Use of radiation
- B01D2323/345—UV-treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/38—Graft polymerization
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/40—Details relating to membrane preparation in-situ membrane formation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/64—Use of a temporary support
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0006—Organic membrane manufacture by chemical reactions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/56—Polyamides, e.g. polyester-amides
Definitions
- the invention relates to the field of forward osmosis technology, in particular to a forward osmosis membrane and a preparation method thereof.
- the forward osmosis process In the field of water treatment, compared with traditional technologies such as microfiltration, ultrafiltration, nanofiltration, reverse osmosis and other membrane processes, the forward osmosis process has the advantages of low energy consumption, low pollution tendency and easy cleaning. However, forward osmosis still faces many problems, among which concentration polarization is one of the main problems affecting the positive osmosis performance. Concentration polarization phenomenon is ubiquitous in the membrane separation process, because the semipermeable membrane has a retention effect, the raw material liquid The portion that fails to pass through the semipermeable membrane accumulates on the surface of the membrane or the accumulation of the solute inside the membrane due to the non-uniform structure of the membrane significantly reduces the osmotic pressure, thereby reducing the performance of forward osmosis.
- the forward osmosis membrane is composed of an active skin layer and a porous support layer.
- a large amount of research has been devoted to improving the structure and properties of the support layer of the membrane to reduce the concentration polarization phenomenon to improve the performance of the forward osmosis membrane.
- a support layer having a finger structure can be obtained by changing the solvent of the casting solution, the composition and concentration of the polymer, or a hydrophilic support material can be obtained by adding a hydrophilic substance. Since the hydrophilic support layer pore wall surface can be effectively wetted by the solution, the mass transfer is promoted to reduce the concentration polarization.
- the hydrophilic modification of the support layer there are also the following problems: (1) the hydrophilic support has reduced mechanical stability and is easy to swell in water; (2) affects the interfacial polymerization reaction or changes the active cortex. nature.
- the object of the present invention is to provide a forward osmosis membrane and a preparation method thereof, which aim to solve the problem that the hydrophilicity of the support layer which is hydrophilically modified by the existing support layer is reduced, and the mechanical stability is reduced. Swelling in water affects interfacial polymerization or alters the properties of the active skin.
- a method for preparing a forward osmosis membrane comprising:
- Step A separately configuring a polysulfone solution and a polyetherimide solution, and respectively stirring the polysulfone solution and the polyetherimide solution at 60-80 ° C for 6-7 hours;
- Step B the polyetherimide solution is scraped into a polyetherimide film on a glass plate, and then the polysulfone solution is scraped on the polyetherimide film to form a polysulfone film;
- Step C tearing off the polyetherimide film to obtain a polysulfone support layer, and the side close to the polyetherimide film is used as the bottom of the polysulfone support layer;
- Step D The polysulfone support layer is immersed in a methanol solution of benzophenone for 1.5-2.5 hours, and the polysulfone support layer is taken out and placed in an SMP solution, and the bottom of the polysulfone support layer faces the ultraviolet lamp. Grafting a PSMP polymer on the bottom of the polysulfone support layer and the inner wall of the pore under irradiation of a UV lamp;
- Step E separately dissolving the aqueous solution of m-phenylenediamine and the solution of trimellitic acid chloride in n-hexane, and immersing the top of the polysulfone support layer obtained in step D in the aqueous solution of m-phenylenediamine for 3-10 minutes; and then obtaining the obtained polysulfone support layer.
- the top was immersed in a solution of trimesoyl chloride in hexane for 1-3 minutes.
- An active skin layer was prepared on top of the polysulfone support layer.
- the polysulfone solution is obtained by disposing N,N-dimethylacetamide, polyethylene glycol 400 and polysulfone.
- the polyetherimide solution is obtained by disposing N-methylpyrrolidone and a polyetherimide.
- step D comprises a step of: immersing the polysulfone membrane in a methanol solution for 1.5-2.5 hours.
- the method for preparing a forward osmosis membrane wherein in the step D, the concentration of the benzophenone in the methanol solution of benzophenone is 0.1-0.2 mol/L.
- the method for preparing a forward osmosis membrane wherein in the step D, the ultraviolet lamp is irradiated for 20-40 minutes.
- a forward osmosis membrane comprising a polysulfone support layer and an active skin layer compounded on top of the polysulfone support layer, a bottom of the polysulfone support layer and a pore inner wall grafted with a PSMP polymer; the forward osmosis membrane It is prepared by the method described in the present invention.
- the forward osmosis membrane wherein the polysulfone support layer has a thickness of 80 to 120 ⁇ m, and the active skin layer has a thickness of 5 to 15 nm.
- the present invention combines the method of preparing a bottom macroporous support layer by sacrificial layer joint casting for the first time and the method of ultraviolet radiation grafting hydrophilic PSMP polymer modification to comprehensively improve the positive permeability of the membrane.
- the method for grafting hydrophilic PSMP polymer by ultraviolet irradiation only hydrophilically modifies the bottom of the porous support layer and the inner wall of the pore, thereby maintaining the stability of the active skin layer and further improving the positive
- the water permeability of the permeable membrane The operation steps of the invention are simple and easy, the effect is stable and obvious, the water permeability is good, and the separation selectivity of the positive permeation is greatly improved.
- FIG. 1 is an SEM image of a forward osmosis membrane of a non-grafted PSMP and a forward osmosis membrane to which a PSMP has been grafted in the examples.
- the present invention provides a forward osmosis membrane and a preparation method thereof, and the present invention will be further described in detail below in order to clarify and clarify the objects, technical solutions and effects of the present invention. It is understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
- the invention discloses a preparation method of a forward osmosis membrane, which comprises:
- Step A separately configuring a polysulfone solution and a polyetherimide solution, and respectively stirring the polysulfone solution and the polyetherimide solution at 60-80 ° C for 6-7 hours;
- Step B the polyetherimide solution is scraped into a polyetherimide film on a glass plate, and then the polysulfone solution is scraped on the polyetherimide film to form a polysulfone film;
- Step C tearing off the polyetherimide film to obtain a polysulfone support layer, and the side close to the polyetherimide film is used as the bottom of the polysulfone support layer;
- Step D The polysulfone support layer is immersed in a methanol solution of benzophenone for 1.5-2.5 hours, and the polysulfone support layer is taken out and placed in an SMP monomer solution, and the bottom of the polysulfone support layer faces the ultraviolet lamp. Grafting a PSMP polymer on the bottom of the polysulfone support layer and the inner wall of the pore under irradiation of a UV lamp;
- Step E separately dissolving the aqueous solution of m-phenylenediamine and the solution of trimellitic acid chloride in n-hexane, and immersing the top of the polysulfone support layer obtained in step D in the aqueous solution of m-phenylenediamine for 3-10 minutes; and then obtaining the obtained polysulfone support layer.
- the top was immersed in a solution of trimesoyl chloride in hexane for 1-3 minutes.
- An active skin layer was prepared on top of the polysulfone support layer.
- the hydrophilic modification of the conventional forward osmosis membrane is a method of increasing the content of the hydrophilic group in the polymer or blending with the hydrophilic polymer, and these methods make the top and bottom of the support layer hydrophilic. Sex, which has a certain effect on the performance of the active cortex, and the retention of salt is reduced.
- a macroporous support layer having a hydrophilic top portion at the top can be prepared, so that a stable active skin layer can be prepared on the top of the support layer, thereby improving the water permeability of the forward osmosis membrane without affecting the salt retention. the amount.
- the invention grafts the hydrophilic polymer to the bottom of the porous support layer and the inner wall of the pore by the method of ultraviolet grafting.
- the method of ultraviolet grafting is simple, and the grafting time is short. The operation is simple and the grafting result is stable and controllable.
- the invention adopts a sacrificial layer joint casting method to prepare a polysulfone support layer with a large bottom hole, and the sacrificial layer joint casting method specifically includes the steps A-C:
- the step A specifically includes first configuring two polymer solutions.
- the polysulfone solution is prepared from N,N-dimethylacetamide (DMAc), polyethylene glycol 400 (PEG400) and polysulfone (PSf);
- the polyetherimide solution is composed of N-methylpyrrolidone (NMP).
- NMP N-methylpyrrolidone
- PEI polyetherimide
- the step B specifically comprises: first pouring the PEI solution on a dry and flat glass plate, scraping the PEI solution with a 100 ⁇ m scraper to form a PEI film; and then pouring the PSf solution onto the PEI film and scraping with a 300 ⁇ m scraper. A PSf film was produced.
- the step C specifically comprises: placing the glass plate in pure water for 1-2 minutes, with the purpose of utilizing phase inversion, so that the high molecular polymer is rapidly precipitated at the interface to form a very thin dense layer, and is formed under the dense layer.
- the porous layer forms a film structure with an outer dense interior.
- the PEI film was peeled off to obtain a PSf support layer, and the side close to the PEI film was used as the bottom of the PSf support layer.
- the present invention employs a method of ultraviolet grafting to graft a hydrophilic PSMP polymer to the bottom of the PSf support layer and the inner wall of the pore.
- the method of the ultraviolet grafting method of the invention has the advantages of simple steps, short grafting time, simple operation, and stable and controllable grafting results.
- the macroporous PSf support layer which is hydrophilic at the top hydrophobic bottom can be prepared by the method of ultraviolet grafting of the invention, so that a stable active skin layer is prepared on the top of the PSf support layer, so that the positive skin layer is improved without affecting the salt retention.
- the method of ultraviolet grafting is step D:
- the step D specifically includes: immersing the polysulfone support layer in a methanol solution for 1.5-2.5 hours (for example, two hours), so that impurities on the surface of the polysulfone support layer are removed. Then, the polysulfone support layer was taken out from the methanol solution and immersed in a methanol solution of 0.1-0.2 mol/L benzophenone (BP) (as a photoinitiator to activate the surface of the polysulfone support layer) for 1.5-2.5 hours ( Such as two hours).
- BP benzophenone
- the present invention prepares a polyamide active skin layer on a polysulfone support layer by an interfacial polymerization method, and the interfacial polymerization method is the step E:
- Step E specifically includes: disposing 25 mL of a 3 wt% aqueous solution of m-phenylenediamine (MPD) and 25 mL of a 0.15% by weight solution of trimesoyl chloride (TMC) in n-hexane.
- MPD m-phenylenediamine
- TMC trimesoyl chloride
- step D Place the polysulfone support layer obtained in step D on a jig, drop the MPD aqueous solution on top of the polysulfone support layer with a dropper until it is completely covered, keep it for 3-10 minutes, remove the excess MPD aqueous solution; then The TMC n-hexane solution was dropped onto the top of the polysulfone support layer using a dropper until it was completely covered for 1-3 minutes, and the excess TMC n-hexane solution was removed.
- An active skin layer is prepared by interfacial polymerization on top of the polysulfone support layer.
- the invention firstly adopts a sacrificial layer combined casting method to prepare a polysulfone support layer with a large pore at the bottom, and then grafts a hydrophilic PSMP polymer to the bottom of the PSf support layer and the inner wall of the pore by ultraviolet grafting, and finally adopts interfacial polymerization.
- the method comprises preparing an active skin layer on top of a polysulfone support layer to obtain a forward osmosis membrane. After the positive osmosis membrane is prepared by the present invention, the forward osmosis membrane is subjected to a forward osmosis desalination test.
- Forward osmosis desalination test The permeation performance of the forward osmosis membrane and the separation selectivity to NaCl were measured by a forward osmosis apparatus.
- the raw material liquid is pure water, and the extract liquid is a 0.5-4 M NaCl solution.
- Conductivity meter is used to measure the change of conductivity of the raw material liquid for a certain period of time. According to the curve of conductivity and NaCl concentration, the salt permeation amount is calculated for a certain period of time, and the volume change of the draw solution is measured to determine the forward osmosis membrane. Water flux.
- the hydrophilic modification of the conventional forward osmosis membrane is a method of increasing the content of the hydrophilic group in the polymer or blending with the hydrophilic polymer, and the present invention is to polymerize the hydrophilic PSMP by ultraviolet irradiation.
- the method of the material only hydrophilically modifies the bottom of the porous support layer and the inner wall of the pore, thereby maintaining the stability of the active skin layer and further improving the water permeability of the forward osmosis membrane.
- the invention combines the method of preparing the bottom macroporous support layer by the joint casting of the sacrificial layer for the first time and the method of modifying the hydrophilic PSMP polymer by the ultraviolet irradiation grafting to comprehensively improve the positive permeability of the membrane.
- the operation steps of the invention are simple and easy, the effect is stable and obvious, the water permeability is good, and the separation selectivity of the positive permeation is greatly improved.
- the present invention also provides a forward osmosis membrane comprising a polysulfone support layer and an active skin layer compounded on top of the polysulfone support layer, wherein the bottom of the polysulfone support layer and the inner wall of the pore are grafted with a PSMP polymer;
- the forward osmosis membrane is prepared by the method described in the present invention.
- the polysulfone support layer has an effective pore size of about 25-35 nanometers (e.g., 30 nanometers).
- the polysulfone support layer has a thickness of about 80-120 microns (e.g., 100 microns) and the active skin layer has a thickness of about 5-15 nanometers (e.g., 10 nanometers).
- polysulfone solution dissolve 18g polysulfone (PSf) material in 74g N, N-dimethylacetamide (DMAC) solution, add 15g polyethylene glycol (PEG400); polyether amide Imine solution: 17 g of polyetherimide (PEI) was dissolved in N-methylpyrrolidone (NMP). Then, the two solutions were respectively placed in a 65 ° C water bath and stirred for 7 hours, and the stirring speed was 380 r/min.
- PSf polysulfone
- DMAC N-dimethylacetamide
- NMP N-methylpyrrolidone
- PEI solution was first poured on a dry and flat glass plate, the PEI solution was scraped off with a 100 ⁇ m scraper, and the PSf solution was poured onto the PEI and scraped with a 300 ⁇ m scraper. Finally, the glass plate was placed in pure water for 1 minute, and torn. The PEI layer is removed from the PEI layer, and the side close to the PEI layer is used as the bottom of the PSf support layer. The resulting PSf support layer was stored in deionized water.
- the PSf support layer was immersed in a methanol solution for two hours to remove surface impurities.
- the PSf support layer was then immersed in a 0.13 mol/L benzophenone (BP) solution in methanol (photoinitiator) for two hours.
- BP benzophenone
- the treated PSf support layer was taken out and placed in a 100 mL 0.05 g/mL SMP monomer solution, and placed in a UV light box for half an hour to graft the PSMP polymer.
- the bottom of the PSf support layer was directed toward the UV lamp, and a piece was placed at the top. Quartz glass flakes reduce the solvent volatilization in the monomer solution to change the monomer concentration and reduce the test error.
- the permeation performance of the forward osmosis membrane and the separation selectivity to NaCl were measured by a forward osmosis apparatus.
- the raw material liquid was pure water, and the extract liquid was 0.5 M, 1 M, 1.5 M, 2 M, 4 M NaCl solution, respectively.
- the water flux and reverse salt flux of the forward osmosis membrane in the two modes of AL-FS (the cortex facing the raw material liquid) and AL-DS (the cortex facing the draw liquid) were measured.
- the reverse salt flux is the conductivity change of the raw material liquid measured by a conductivity meter for a certain period of time, and the salt permeation amount is calculated according to the curve of the conductivity and the NaCl concentration.
- the water flux is determined by measuring the volume change of the draw liquid during this period of time to determine the water flux of the forward osmosis membrane.
- the water flux can be as high as 24L/m 2 ⁇ h, while the reverse salt flux is only about 0.5g, showing excellent separation selectivity.
- Fig. 1a is a positive osmosis membrane skin layer of ungrafted PSMP
- Fig. 1d is a cross-sectional structure of a positive osmosis membrane which is not grafted with PSMP near the cortex
- Fig. 1b is a positive osmosis membrane skin layer to which PSMP has been grafted
- Figure 1e is a cross-sectional structure of a positive osmosis membrane grafted with PSMP adjacent to the skin layer. It can be seen from the figure that the ungrafted forward osmosis membrane skin layer is relatively rough, the cortex of the grafted PSMP forward osmosis membrane is relatively smoother and smoother, and the more stable skin layer contributes to the retention of NaCl.
- the present invention provides a forward osmosis membrane and a preparation method thereof.
- the hydrophilic modification of a conventional forward osmosis membrane is by increasing the content of a hydrophilic group in the polymer or co-synthesizing with a hydrophilic polymer.
- a method of mixing, and the method of grafting a hydrophilic PSMP polymer by ultraviolet irradiation only hydrophilically modifies the bottom of the porous support layer and the inner wall of the pore, thereby maintaining the stability of the active skin layer. Further improved the water permeability of the forward osmosis membrane.
- the invention combines the method of preparing the bottom macroporous support layer by the joint casting of the sacrificial layer for the first time and the method of modifying the hydrophilic PSMP polymer by the ultraviolet irradiation grafting to comprehensively improve the positive permeability of the membrane.
- the operation steps of the invention are simple and easy, the effect is stable and obvious, the water permeability is good, and the separation selectivity of the forward osmosis is greatly improved.
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Abstract
A forward osmosis membrane, and a preparation method therefor. A sacrificial layer is used, in combination with a casting method, for preparing a bottom macroporous polysulfone supporting layer; then an ultraviolet grafting method is used for grafting a hydrophilic PSMP polymer onto the bottom and pore internal walls of the supporting layer; and finally, an interfacial polymerization method is used for preparing an active skin layer on the top of the polysulfone supporting layer so as to obtain a forward osmosis membrane. According to the method, ultraviolet grafting of a hydrophilic PSMP polymer is used for implementing hydrophilic modification on the bottom and pore internal walls of a macroporous polysulfone supporting layer, so that the stability of an active skin layer is maintained, and the permeability performance of a forward osmosis membrane is further improved.
Description
本发明涉及正渗透技术领域,尤其涉及一种正渗透膜及其制备方法。The invention relates to the field of forward osmosis technology, in particular to a forward osmosis membrane and a preparation method thereof.
目前,人们为了获得足够的淡水供给采取了海水淡化、废水回收等各种水处理方法,但是却以消耗大量能源为代价,因此减小实际能耗与溶液的热力学最小分离能之间的差距一直是研究的热点。其中,正渗透是一种新兴的脱盐和分离技术,它是利用半透膜两端渗透压的不同来实现溶液的自发分离。近年来正渗透已经被应用于很多领域,例如:海水脱盐、污水处理、浓缩垃圾渗滤液等。在水处理领域中,相比于传统技术如微滤、超滤、纳滤、反渗透等膜过程,正渗透过程具有低能耗、低污染趋势、易清洗等优势。然而,正渗透仍然面临着许多问题,其中浓差极化是影响正渗透性能的主要问题之一,浓差极化现象是膜分离过程中普遍存在的,由于半透膜具有截留作用,原料液中未能透过半透膜的部分在膜表面积累或者是由于膜的非均一结构造成的溶质在膜内部的积累而显著的降低了渗透压,从而降低了正渗透的性能。At present, people have adopted various water treatment methods such as seawater desalination and wastewater recovery in order to obtain sufficient fresh water supply, but at the cost of consuming a large amount of energy, thus reducing the gap between the actual energy consumption and the thermodynamic minimum separation energy of the solution. It is a hot spot of research. Among them, forward osmosis is an emerging desalination and separation technology, which uses the difference in osmotic pressure at both ends of the semipermeable membrane to achieve spontaneous separation of the solution. In recent years, positive infiltration has been used in many fields, such as: seawater desalination, sewage treatment, and concentrated landfill leachate. In the field of water treatment, compared with traditional technologies such as microfiltration, ultrafiltration, nanofiltration, reverse osmosis and other membrane processes, the forward osmosis process has the advantages of low energy consumption, low pollution tendency and easy cleaning. However, forward osmosis still faces many problems, among which concentration polarization is one of the main problems affecting the positive osmosis performance. Concentration polarization phenomenon is ubiquitous in the membrane separation process, because the semipermeable membrane has a retention effect, the raw material liquid The portion that fails to pass through the semipermeable membrane accumulates on the surface of the membrane or the accumulation of the solute inside the membrane due to the non-uniform structure of the membrane significantly reduces the osmotic pressure, thereby reducing the performance of forward osmosis.
正渗透膜是由活性皮层和多孔支撑层构成,近年来,大量的研究致力于改进膜的支撑层的结构和性能来减少浓差极化现象以提高正渗透膜性能。例如:通过改变铸膜液的溶剂、聚合物的组成和浓度得到具有指状结构的支撑层,或者加入具有亲水性的物质得到亲水性的支撑层。由于亲水的支撑层孔壁表面能被溶液有效润湿,从而促进质量传递减少浓差极化。但是在支撑层亲水性改性中也存在以下几个方面的问题:(1)亲水性的支撑体机械稳定性降低、易在水中溶胀;(2)影响界面聚合反应或改变活性皮层的性质。The forward osmosis membrane is composed of an active skin layer and a porous support layer. In recent years, a large amount of research has been devoted to improving the structure and properties of the support layer of the membrane to reduce the concentration polarization phenomenon to improve the performance of the forward osmosis membrane. For example, a support layer having a finger structure can be obtained by changing the solvent of the casting solution, the composition and concentration of the polymer, or a hydrophilic support material can be obtained by adding a hydrophilic substance. Since the hydrophilic support layer pore wall surface can be effectively wetted by the solution, the mass transfer is promoted to reduce the concentration polarization. However, in the hydrophilic modification of the support layer, there are also the following problems: (1) the hydrophilic support has reduced mechanical stability and is easy to swell in water; (2) affects the interfacial polymerization reaction or changes the active cortex. nature.
因此,现有技术还有待于改进和发展。Therefore, the prior art has yet to be improved and developed.
发明内容Summary of the invention
鉴于上述现有技术的不足,本发明的目的在于提供一种正渗透膜及其制备方法,旨在解决现有支撑层亲水性改性存在亲水性的支撑体机械稳定性降低、易在 水中溶胀,影响界面聚合反应或改变活性皮层的性质的问题。In view of the above-mentioned deficiencies of the prior art, the object of the present invention is to provide a forward osmosis membrane and a preparation method thereof, which aim to solve the problem that the hydrophilicity of the support layer which is hydrophilically modified by the existing support layer is reduced, and the mechanical stability is reduced. Swelling in water affects interfacial polymerization or alters the properties of the active skin.
本发明的技术方案如下:The technical solution of the present invention is as follows:
一种正渗透膜的制备方法,其中,包括:A method for preparing a forward osmosis membrane, comprising:
步骤A、分别配置聚砜溶液和聚醚酰亚胺溶液,并分别将所述聚砜溶液和聚醚酰亚胺溶液在60-80℃下搅拌6-7小时;Step A, separately configuring a polysulfone solution and a polyetherimide solution, and respectively stirring the polysulfone solution and the polyetherimide solution at 60-80 ° C for 6-7 hours;
步骤B、将聚醚酰亚胺溶液在玻璃板上刮制成聚醚酰亚胺薄膜,然后将聚砜溶液在聚醚酰亚胺薄膜上刮制成聚砜薄膜;Step B, the polyetherimide solution is scraped into a polyetherimide film on a glass plate, and then the polysulfone solution is scraped on the polyetherimide film to form a polysulfone film;
步骤C、撕去所述聚醚酰亚胺薄膜得到聚砜支撑层,将靠近聚醚酰亚胺薄膜的一面作为所述聚砜支撑层的底部;Step C, tearing off the polyetherimide film to obtain a polysulfone support layer, and the side close to the polyetherimide film is used as the bottom of the polysulfone support layer;
步骤D、将聚砜支撑层放入二苯甲酮的甲醇溶液中浸泡1.5-2.5小时,取出所述聚砜支撑层放入SMP溶液中,所述聚砜支撑层的底部朝向紫外灯,在紫外灯照射下在所述聚砜支撑层的底部和孔内壁接枝PSMP聚合物;Step D: The polysulfone support layer is immersed in a methanol solution of benzophenone for 1.5-2.5 hours, and the polysulfone support layer is taken out and placed in an SMP solution, and the bottom of the polysulfone support layer faces the ultraviolet lamp. Grafting a PSMP polymer on the bottom of the polysulfone support layer and the inner wall of the pore under irradiation of a UV lamp;
步骤E、分别配置间苯二胺水溶液和均苯三甲酰氯正己烷溶液,将步骤D得到的聚砜支撑层顶部浸泡于间苯二胺水溶液3-10分钟;然后再将得到的聚砜支撑层顶部浸泡于均苯三甲酰氯正己烷溶液1-3分钟。在聚砜支撑层顶部制备得到活性皮层。Step E: separately dissolving the aqueous solution of m-phenylenediamine and the solution of trimellitic acid chloride in n-hexane, and immersing the top of the polysulfone support layer obtained in step D in the aqueous solution of m-phenylenediamine for 3-10 minutes; and then obtaining the obtained polysulfone support layer. The top was immersed in a solution of trimesoyl chloride in hexane for 1-3 minutes. An active skin layer was prepared on top of the polysulfone support layer.
所述的正渗透膜的制备方法,其中,所述步骤A中,所述聚砜溶液由N,N-二甲基乙酰胺、聚乙二醇400和聚砜配置得到。In the method for preparing a forward osmosis membrane, in the step A, the polysulfone solution is obtained by disposing N,N-dimethylacetamide, polyethylene glycol 400 and polysulfone.
所述的正渗透膜的制备方法,其中,所述步骤A中,所述聚醚酰亚胺溶液由N-甲基吡咯烷酮和聚醚酰亚胺配置得到。In the method for preparing a forward osmosis membrane, in the step A, the polyetherimide solution is obtained by disposing N-methylpyrrolidone and a polyetherimide.
所述的正渗透膜的制备方法,其中,所述步骤D之前包括步骤:将聚砜薄膜放入甲醇溶液中浸泡1.5-2.5小时。The method for preparing a forward osmosis membrane, wherein the step D comprises a step of: immersing the polysulfone membrane in a methanol solution for 1.5-2.5 hours.
所述的正渗透膜的制备方法,其中,所述步骤D中,所述二苯甲酮的甲醇溶液中,所述二苯甲酮的浓度为0.1-0.2mol/L。The method for preparing a forward osmosis membrane, wherein in the step D, the concentration of the benzophenone in the methanol solution of benzophenone is 0.1-0.2 mol/L.
所述的正渗透膜的制备方法,其中,所述步骤D中,所述紫外灯照射的时间为20-40分钟。The method for preparing a forward osmosis membrane, wherein in the step D, the ultraviolet lamp is irradiated for 20-40 minutes.
所述的正渗透膜的制备方法,其中,所述步骤D中,所述紫外灯照射的时间为30分钟。一种正渗透膜,其中,包括聚砜支撑层和复合于所述聚砜支撑层顶部的活性皮层,所述聚砜支撑层的底部和孔内壁接枝有PSMP聚合物;所述正 渗透膜采用本发明所述的方法制备得到。The method for preparing a forward osmosis membrane, wherein in the step D, the ultraviolet lamp is irradiated for 30 minutes. a forward osmosis membrane comprising a polysulfone support layer and an active skin layer compounded on top of the polysulfone support layer, a bottom of the polysulfone support layer and a pore inner wall grafted with a PSMP polymer; the forward osmosis membrane It is prepared by the method described in the present invention.
所述的正渗透膜,其中,所述聚砜支撑层的孔径为25-35纳米。The forward osmosis membrane, wherein the polysulfone support layer has a pore diameter of 25 to 35 nm.
所述的正渗透膜,其中,所述聚砜支撑层的厚度为80-120微米,所述活性皮层的厚度为5-15纳米。The forward osmosis membrane, wherein the polysulfone support layer has a thickness of 80 to 120 μm, and the active skin layer has a thickness of 5 to 15 nm.
有益效果:本发明首次将牺牲层联合铸造制备底部大孔支撑层的方法与紫外辐照接枝亲水性PSMP聚合物改性的方法结合起来综合提升膜的正渗透性能。本发明利用紫外辐照接枝亲水性PSMP聚合物的方法只对多孔支撑层的底部和孔的内壁进行亲水性改性,这样既保持了活性皮层的稳定性,又近一步提高了正渗透膜的透水性能。本发明操作步骤简单易行,效果稳定明显,透水性好,且正渗透的分离选择性有很大提高。Advantageous Effects: The present invention combines the method of preparing a bottom macroporous support layer by sacrificial layer joint casting for the first time and the method of ultraviolet radiation grafting hydrophilic PSMP polymer modification to comprehensively improve the positive permeability of the membrane. The method for grafting hydrophilic PSMP polymer by ultraviolet irradiation only hydrophilically modifies the bottom of the porous support layer and the inner wall of the pore, thereby maintaining the stability of the active skin layer and further improving the positive The water permeability of the permeable membrane. The operation steps of the invention are simple and easy, the effect is stable and obvious, the water permeability is good, and the separation selectivity of the positive permeation is greatly improved.
图1为实施例中未接枝PSMP的正渗透膜与已接枝PSMP的正渗透膜的SEM图。1 is an SEM image of a forward osmosis membrane of a non-grafted PSMP and a forward osmosis membrane to which a PSMP has been grafted in the examples.
本发明提供一种正渗透膜及其制备方法,为使本发明的目的、技术方案及效果更加清楚、明确,以下对本发明进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。The present invention provides a forward osmosis membrane and a preparation method thereof, and the present invention will be further described in detail below in order to clarify and clarify the objects, technical solutions and effects of the present invention. It is understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
本发明公开一种正渗透膜的制备方法,其中,包括:The invention discloses a preparation method of a forward osmosis membrane, which comprises:
步骤A、分别配置聚砜溶液和聚醚酰亚胺溶液,并分别将所述聚砜溶液和聚醚酰亚胺溶液在60-80℃下搅拌6-7小时;Step A, separately configuring a polysulfone solution and a polyetherimide solution, and respectively stirring the polysulfone solution and the polyetherimide solution at 60-80 ° C for 6-7 hours;
步骤B、将聚醚酰亚胺溶液在玻璃板上刮制成聚醚酰亚胺薄膜,然后将聚砜溶液在聚醚酰亚胺薄膜上刮制成聚砜薄膜;Step B, the polyetherimide solution is scraped into a polyetherimide film on a glass plate, and then the polysulfone solution is scraped on the polyetherimide film to form a polysulfone film;
步骤C、撕去所述聚醚酰亚胺薄膜得到聚砜支撑层,将靠近聚醚酰亚胺薄膜的一面作为所述聚砜支撑层的底部;Step C, tearing off the polyetherimide film to obtain a polysulfone support layer, and the side close to the polyetherimide film is used as the bottom of the polysulfone support layer;
步骤D、将聚砜支撑层放入二苯甲酮的甲醇溶液中浸泡1.5-2.5小时,取出所述聚砜支撑层放入SMP单体溶液中,所述聚砜支撑层的底部朝向紫外灯,在紫外灯照射下在所述聚砜支撑层的底部和孔内壁接枝PSMP聚合物;Step D: The polysulfone support layer is immersed in a methanol solution of benzophenone for 1.5-2.5 hours, and the polysulfone support layer is taken out and placed in an SMP monomer solution, and the bottom of the polysulfone support layer faces the ultraviolet lamp. Grafting a PSMP polymer on the bottom of the polysulfone support layer and the inner wall of the pore under irradiation of a UV lamp;
步骤E、分别配置间苯二胺水溶液和均苯三甲酰氯正己烷溶液,将步骤D得到的聚砜支撑层顶部浸泡于间苯二胺水溶液3-10分钟;然后再将得到的聚砜支撑层顶部浸泡于均苯三甲酰氯正己烷溶液1-3分钟。在聚砜支撑层顶部制备得到活性皮层。Step E: separately dissolving the aqueous solution of m-phenylenediamine and the solution of trimellitic acid chloride in n-hexane, and immersing the top of the polysulfone support layer obtained in step D in the aqueous solution of m-phenylenediamine for 3-10 minutes; and then obtaining the obtained polysulfone support layer. The top was immersed in a solution of trimesoyl chloride in hexane for 1-3 minutes. An active skin layer was prepared on top of the polysulfone support layer.
传统正渗透膜的亲水性改性都是通过增加聚合物中亲水性基团的含量或者与亲水性聚合物共混的方法,这些方法使得支撑层的顶部和底部都具备了亲水性,从而对活性皮层性能有一定的影响,盐的截留性能降低。然而,通过本发明方法可以制备得到顶部疏水底部亲水的大孔支撑层,使得在支撑层顶部制备出性能稳定的活性皮层,这样在不影响对盐截留的情况下提高正渗透膜的水通量。本发明通过紫外接枝的方法将亲水性聚合物接枝到多孔支撑层底部和孔内壁,相对于传统的表面接枝聚合物的方法,紫外接枝的方法步骤简单,接枝时间短,操作简便,接枝结果稳定可控。The hydrophilic modification of the conventional forward osmosis membrane is a method of increasing the content of the hydrophilic group in the polymer or blending with the hydrophilic polymer, and these methods make the top and bottom of the support layer hydrophilic. Sex, which has a certain effect on the performance of the active cortex, and the retention of salt is reduced. However, by the method of the present invention, a macroporous support layer having a hydrophilic top portion at the top can be prepared, so that a stable active skin layer can be prepared on the top of the support layer, thereby improving the water permeability of the forward osmosis membrane without affecting the salt retention. the amount. The invention grafts the hydrophilic polymer to the bottom of the porous support layer and the inner wall of the pore by the method of ultraviolet grafting. Compared with the traditional method of grafting the surface polymer, the method of ultraviolet grafting is simple, and the grafting time is short. The operation is simple and the grafting result is stable and controllable.
本发明采用牺牲层联合铸造方法制备得到底部大孔的聚砜支撑层,所述牺牲层联合铸造方法具体包括步骤A-C:The invention adopts a sacrificial layer joint casting method to prepare a polysulfone support layer with a large bottom hole, and the sacrificial layer joint casting method specifically includes the steps A-C:
所述步骤A具体包括:首先配置两种聚合物溶液。其中聚砜溶液由N,N-二甲基乙酰胺(DMAc)、聚乙二醇400(PEG400)和聚砜(PSf)配置得到;聚醚酰亚胺溶液由N-甲基吡咯烷酮(NMP)和聚醚酰亚胺(PEI)配置得到。分别将两溶液在60℃-80℃水浴搅拌6-7小时直至聚合物完全溶解。The step A specifically includes first configuring two polymer solutions. The polysulfone solution is prepared from N,N-dimethylacetamide (DMAc), polyethylene glycol 400 (PEG400) and polysulfone (PSf); the polyetherimide solution is composed of N-methylpyrrolidone (NMP). And polyetherimide (PEI) configuration. The two solutions were separately stirred in a water bath at 60 ° C - 80 ° C for 6-7 hours until the polymer was completely dissolved.
所述步骤B具体包括:先将PEI溶液倒在干燥平整的玻璃板上,用100μm的刮刀刮取PEI溶液,制成PEI薄膜;再将PSf溶液倒在PEI薄膜上用300μm的刮刀刮取,制成PSf薄膜。The step B specifically comprises: first pouring the PEI solution on a dry and flat glass plate, scraping the PEI solution with a 100 μm scraper to form a PEI film; and then pouring the PSf solution onto the PEI film and scraping with a 300 μm scraper. A PSf film was produced.
所述步骤C具体包括:将玻璃板置于纯水中1-2分钟,目的是利用相转化,使得高分子聚合物在界面快速析出,形成极薄的致密层,而在致密层的下面形成了多孔层,形成外密内疏的膜结构。撕去所述PEI薄膜得到PSf支撑层,将靠近PEI薄膜的一面作为PSf支撑层的底部。The step C specifically comprises: placing the glass plate in pure water for 1-2 minutes, with the purpose of utilizing phase inversion, so that the high molecular polymer is rapidly precipitated at the interface to form a very thin dense layer, and is formed under the dense layer. The porous layer forms a film structure with an outer dense interior. The PEI film was peeled off to obtain a PSf support layer, and the side close to the PEI film was used as the bottom of the PSf support layer.
本发明采用紫外接枝的方法,将亲水性的PSMP聚合物接枝到PSf支撑层的底部和孔内壁。相对于传统的表面接枝聚合物的方法,本发明紫外接枝的方法步骤简单,接枝时间短,操作简便,接枝结果稳定可控。且通过本发明紫外接枝的方法可以制备得到顶部疏水底部亲水的大孔PSf支撑层,使得在PSf支撑层顶部 制备出性能稳定的活性皮层,这样在不影响对盐截留的情况下提高正渗透膜的水通量。所述紫外接枝的方法为步骤D:The present invention employs a method of ultraviolet grafting to graft a hydrophilic PSMP polymer to the bottom of the PSf support layer and the inner wall of the pore. Compared with the conventional method for grafting a surface polymer, the method of the ultraviolet grafting method of the invention has the advantages of simple steps, short grafting time, simple operation, and stable and controllable grafting results. And the macroporous PSf support layer which is hydrophilic at the top hydrophobic bottom can be prepared by the method of ultraviolet grafting of the invention, so that a stable active skin layer is prepared on the top of the PSf support layer, so that the positive skin layer is improved without affecting the salt retention. The water flux of the permeable membrane. The method of ultraviolet grafting is step D:
步骤D具体包括:将聚砜支撑层放入甲醇溶液中浸泡1.5-2.5小时(如两小时),使所述聚砜支撑层表面杂质被清除干净。然后从甲醇溶液中取出聚砜支撑层放入0.1-0.2mol/L的二苯甲酮(BP)的甲醇溶液(作为光引发剂,使聚砜支撑层表面活化)中浸泡1.5-2.5小时(如两小时)。最后从二苯甲酮的甲醇溶液中取出聚砜支撑层放入100-200mL的一定浓度的SMP单体溶液中(其中溶剂为体积比V甲醇:V水=4:1,SMP单体的浓度为0.025-0.15g/mL,如0.05g/mL,0.1g/mL或0.15g/mL),置入紫外灯箱中光照20-40分钟(如30分钟)接枝PSMP聚合物,将聚砜支撑层的底部朝上,在顶端放置一片石英玻璃片,减小单体溶剂挥发使单体浓度变化,减少测试误差。The step D specifically includes: immersing the polysulfone support layer in a methanol solution for 1.5-2.5 hours (for example, two hours), so that impurities on the surface of the polysulfone support layer are removed. Then, the polysulfone support layer was taken out from the methanol solution and immersed in a methanol solution of 0.1-0.2 mol/L benzophenone (BP) (as a photoinitiator to activate the surface of the polysulfone support layer) for 1.5-2.5 hours ( Such as two hours). Finally, the polysulfone support layer was taken out from the methanol solution of benzophenone and placed in a concentration of 100-200 mL of SMP monomer solution (wherein the solvent is volume ratio V methanol: V water = 4:1, concentration of SMP monomer). 0.025-0.15g/mL, such as 0.05g/mL, 0.1g/mL or 0.15g/mL), placed in a UV light box for 20-40 minutes (such as 30 minutes) grafted PSMP polymer, polysulfone support The bottom of the layer faces upwards, and a piece of quartz glass is placed at the top to reduce the evaporation of the monomer solvent to change the monomer concentration and reduce the test error.
本发明通过界面聚合的方法在聚砜支撑层上制备得到聚酰胺活性皮层,所述界面聚合的方法为步骤E:The present invention prepares a polyamide active skin layer on a polysulfone support layer by an interfacial polymerization method, and the interfacial polymerization method is the step E:
步骤E具体包括:配置25mL质量百分比为3wt%的间苯二胺(MPD)水溶液和25mL质量百分比为0.15wt%的均苯三甲酰氯(TMC)正己烷溶液。将步骤D得到的聚砜支撑层放置在夹具上,利用滴管将MPD水溶液滴置于聚砜支撑层的顶部,直至完全覆盖,保持3-10分钟,将多余的MPD水溶液移除;然后再利用滴管将TMC正己烷溶液滴置于聚砜支撑层的顶部,直至完全覆盖,保持1-3分钟,将多余的TMC正己烷溶液移除。通过界面聚合在聚砜支撑层顶部制备得到活性皮层。Step E specifically includes: disposing 25 mL of a 3 wt% aqueous solution of m-phenylenediamine (MPD) and 25 mL of a 0.15% by weight solution of trimesoyl chloride (TMC) in n-hexane. Place the polysulfone support layer obtained in step D on a jig, drop the MPD aqueous solution on top of the polysulfone support layer with a dropper until it is completely covered, keep it for 3-10 minutes, remove the excess MPD aqueous solution; then The TMC n-hexane solution was dropped onto the top of the polysulfone support layer using a dropper until it was completely covered for 1-3 minutes, and the excess TMC n-hexane solution was removed. An active skin layer is prepared by interfacial polymerization on top of the polysulfone support layer.
本发明首先采用牺牲层联合铸造方法制备底部大孔的聚砜支撑层,然后采用紫外接枝的方法将亲水性的PSMP聚合物接枝到PSf支撑层的底部和孔内壁,最后采用界面聚合的方法在聚砜支撑层顶部制备活性皮层,得到正渗透膜。本发明制备得到所述正渗透膜后,对所述正渗透膜进行正渗透脱盐测试。The invention firstly adopts a sacrificial layer combined casting method to prepare a polysulfone support layer with a large pore at the bottom, and then grafts a hydrophilic PSMP polymer to the bottom of the PSf support layer and the inner wall of the pore by ultraviolet grafting, and finally adopts interfacial polymerization. The method comprises preparing an active skin layer on top of a polysulfone support layer to obtain a forward osmosis membrane. After the positive osmosis membrane is prepared by the present invention, the forward osmosis membrane is subjected to a forward osmosis desalination test.
正渗透脱盐测试:用正渗透装置测量正渗透膜的透水性能和对NaCl的分离选择性。原料液为纯水,汲取液为0.5-4M的NaCl溶液。用电导率仪测量原料液一定时间段的电导率变化,根据电导率与NaCl浓度的函数曲线计算出一定时间段盐的透过量,并测量该段时间内汲取液的体积变化来确定正渗透膜的水通量。Forward osmosis desalination test: The permeation performance of the forward osmosis membrane and the separation selectivity to NaCl were measured by a forward osmosis apparatus. The raw material liquid is pure water, and the extract liquid is a 0.5-4 M NaCl solution. Conductivity meter is used to measure the change of conductivity of the raw material liquid for a certain period of time. According to the curve of conductivity and NaCl concentration, the salt permeation amount is calculated for a certain period of time, and the volume change of the draw solution is measured to determine the forward osmosis membrane. Water flux.
传统正渗透膜的亲水改性都是通过增加聚合物中亲水性基团的含量或者与 亲水性聚合物共混的方法,而本发明是利用紫外辐照接枝亲水性PSMP聚合物的方法只对多孔支撑层的底部和孔的内壁进行亲水性改性,这样既保持了活性皮层的稳定性,又近一步提高了正渗透膜的透水性能。本发明首次将牺牲层联合铸造制备底部大孔支撑层的方法与紫外辐照接枝亲水性PSMP聚合物改性的方法结合起来综合提升膜的正渗透性能。本发明操作步骤简单易行,效果稳定明显,透水性好,且正渗透的分离选择性有很大提高。The hydrophilic modification of the conventional forward osmosis membrane is a method of increasing the content of the hydrophilic group in the polymer or blending with the hydrophilic polymer, and the present invention is to polymerize the hydrophilic PSMP by ultraviolet irradiation. The method of the material only hydrophilically modifies the bottom of the porous support layer and the inner wall of the pore, thereby maintaining the stability of the active skin layer and further improving the water permeability of the forward osmosis membrane. The invention combines the method of preparing the bottom macroporous support layer by the joint casting of the sacrificial layer for the first time and the method of modifying the hydrophilic PSMP polymer by the ultraviolet irradiation grafting to comprehensively improve the positive permeability of the membrane. The operation steps of the invention are simple and easy, the effect is stable and obvious, the water permeability is good, and the separation selectivity of the positive permeation is greatly improved.
本发明还提供一种正渗透膜,其中,包括聚砜支撑层和复合于所述聚砜支撑层顶部的活性皮层,所述聚砜支撑层的底部和孔内壁接枝有PSMP聚合物;所述正渗透膜采用本发明所述的方法制备得到。所述聚砜支撑层的有效孔径约为25-35纳米(如30纳米)。所述聚砜支撑层的厚度约为80-120微米(如100微米),所述活性皮层的厚度约为5-15纳米(如10纳米)。The present invention also provides a forward osmosis membrane comprising a polysulfone support layer and an active skin layer compounded on top of the polysulfone support layer, wherein the bottom of the polysulfone support layer and the inner wall of the pore are grafted with a PSMP polymer; The forward osmosis membrane is prepared by the method described in the present invention. The polysulfone support layer has an effective pore size of about 25-35 nanometers (e.g., 30 nanometers). The polysulfone support layer has a thickness of about 80-120 microns (e.g., 100 microns) and the active skin layer has a thickness of about 5-15 nanometers (e.g., 10 nanometers).
下面通过实施例对本发明进行详细说明。The invention will now be described in detail by way of examples.
本实施例正渗透膜的制备方法,包括以下步骤:The preparation method of the positive osmosis membrane of this embodiment comprises the following steps:
1、采用牺牲层联合铸造法制备底部大孔的PSf支撑层:1. Prepare the PSf support layer with large holes at the bottom by sacrificial layer joint casting method:
首先配置两种聚合物溶液,聚砜溶液:将18g聚砜(PSf)材料溶于74gN,N-二甲基乙酰胺(DMAC)溶液中,加入15g聚乙二醇(PEG400);聚醚酰亚胺溶液:将17g聚醚酰亚胺(PEI)溶于N-甲基吡咯烷酮(NMP)中。然后两溶液分别置于65℃水浴搅拌7小时,搅拌的转速380r/min。First, configure two polymer solutions, polysulfone solution: dissolve 18g polysulfone (PSf) material in 74g N, N-dimethylacetamide (DMAC) solution, add 15g polyethylene glycol (PEG400); polyether amide Imine solution: 17 g of polyetherimide (PEI) was dissolved in N-methylpyrrolidone (NMP). Then, the two solutions were respectively placed in a 65 ° C water bath and stirred for 7 hours, and the stirring speed was 380 r/min.
先将PEI溶液倒在干燥平整的玻璃板上,用100μm的刮刀刮取PEI溶液,再将PSf溶液倒在PEI上用300μm的刮刀刮取,最后将玻璃板置于纯水中1分钟,撕去PEI层得到PSf支撑层,将靠近PEI层的一面作为PSf支撑层的底部。所得到的PSf支撑层保存于去离子水中。PEI solution was first poured on a dry and flat glass plate, the PEI solution was scraped off with a 100 μm scraper, and the PSf solution was poured onto the PEI and scraped with a 300 μm scraper. Finally, the glass plate was placed in pure water for 1 minute, and torn. The PEI layer is removed from the PEI layer, and the side close to the PEI layer is used as the bottom of the PSf support layer. The resulting PSf support layer was stored in deionized water.
2、采用紫外光照接枝PSMP聚合物:2. Grafting PSMP polymer with UV light:
将PSf支撑层放入甲醇溶液中浸泡两小时,使表面杂质被清除干净。再将PSf支撑层放入0.13mol/L二苯甲酮(BP)的甲醇溶液(光引发剂)中浸泡两小时。最后取出处理好的PSf支撑层放入100mL的0.05g/mL的SMP单体溶液中,置入紫外灯箱中光照半小时接枝PSMP聚合物,PSf支撑层的底部朝向紫外灯,在顶端放置一片石英玻璃片,减小单体溶液中溶剂挥发使单体浓度变化,减少测试误差。The PSf support layer was immersed in a methanol solution for two hours to remove surface impurities. The PSf support layer was then immersed in a 0.13 mol/L benzophenone (BP) solution in methanol (photoinitiator) for two hours. Finally, the treated PSf support layer was taken out and placed in a 100 mL 0.05 g/mL SMP monomer solution, and placed in a UV light box for half an hour to graft the PSMP polymer. The bottom of the PSf support layer was directed toward the UV lamp, and a piece was placed at the top. Quartz glass flakes reduce the solvent volatilization in the monomer solution to change the monomer concentration and reduce the test error.
3、采用界面聚合的方法制备活性皮层:3. Preparation of active cortex by interfacial polymerization:
配置25mL 2wt%的间苯二胺(MPD)水溶液和25mL 0.1wt%的均苯三甲酰氯(TMC)正己烷溶液。将PSf支撑层放置在夹具上,利用滴管将MPD水溶液滴置于聚砜支撑层的上表面,直至完全覆盖,保持5分钟,将多余的MPD水溶液移除;然后再利用滴管将TMC正己烷溶液滴置于PSf支撑层的上表面,直至完全覆盖,保持2分钟,将多余的TMC正己烷溶液移除。活性皮层制备完成,并将正渗透膜储存于去离子水中。25 mL of a 2 wt% aqueous solution of m-phenylenediamine (MPD) and 25 mL of a 0.1 wt% solution of trimesoyl chloride (TMC) in n-hexane were placed. Place the PSf support layer on the fixture, drop the MPD aqueous solution on the upper surface of the polysulfone support layer with a dropper until it is completely covered, keep it for 5 minutes, remove the excess MPD aqueous solution; then use the dropper to bring the TMC to the right The alkane solution was dropped onto the upper surface of the PSf support layer until it was completely covered and held for 2 minutes to remove excess TMC n-hexane solution. The active skin layer is prepared and the forward osmosis membrane is stored in deionized water.
4、正渗透脱盐测试:4. Positive osmosis desalination test:
用正渗透装置测量正渗透膜的透水性能和对NaCl的分离选择性。原料液为纯水,汲取液分别为0.5M、1M、1.5M、2M、4M的NaCl溶液。测量正渗透膜在AL-FS(皮层对着原料液)和AL-DS(皮层对着汲取液)两个模式下的水通量和反向盐通量。反向盐通量是利用电导率仪测量原料液一定时间段的电导率变化,根据电导率与NaCl浓度的函数曲线计算出一定时间段盐的透过量。水通量是通过测量该段时间内汲取液的体积变化来确定正渗透膜的水通量。当0.5M NaCl为汲取液AL-DS模式下时水通量可高达24L/m
2·h,而反向盐通量仅有0.5g左右,表现出卓越的分离选择性。
The permeation performance of the forward osmosis membrane and the separation selectivity to NaCl were measured by a forward osmosis apparatus. The raw material liquid was pure water, and the extract liquid was 0.5 M, 1 M, 1.5 M, 2 M, 4 M NaCl solution, respectively. The water flux and reverse salt flux of the forward osmosis membrane in the two modes of AL-FS (the cortex facing the raw material liquid) and AL-DS (the cortex facing the draw liquid) were measured. The reverse salt flux is the conductivity change of the raw material liquid measured by a conductivity meter for a certain period of time, and the salt permeation amount is calculated according to the curve of the conductivity and the NaCl concentration. The water flux is determined by measuring the volume change of the draw liquid during this period of time to determine the water flux of the forward osmosis membrane. When 0.5M NaCl is in the draw AL-DS mode, the water flux can be as high as 24L/m 2 ·h, while the reverse salt flux is only about 0.5g, showing excellent separation selectivity.
5、正渗透膜的结构表征:5. Structural characterization of the forward osmosis membrane:
如图1所示,图1a为未接枝PSMP的正渗透膜皮层,图1d为未接枝PSMP的正渗透膜中靠近皮层的断面结构;图1b为已接枝PSMP的正渗透膜皮层,图1e为已接枝PSMP的正渗透膜中靠近皮层的断面结构。从图可以看出,未接枝的正渗透膜皮层相对比较粗糙,已接枝的PSMP正渗透膜的皮层相对更加光滑平整,而更稳定的皮层有助于对NaCl的截留。As shown in Fig. 1, Fig. 1a is a positive osmosis membrane skin layer of ungrafted PSMP, Fig. 1d is a cross-sectional structure of a positive osmosis membrane which is not grafted with PSMP near the cortex; Fig. 1b is a positive osmosis membrane skin layer to which PSMP has been grafted, Figure 1e is a cross-sectional structure of a positive osmosis membrane grafted with PSMP adjacent to the skin layer. It can be seen from the figure that the ungrafted forward osmosis membrane skin layer is relatively rough, the cortex of the grafted PSMP forward osmosis membrane is relatively smoother and smoother, and the more stable skin layer contributes to the retention of NaCl.
综上所述,本发明提供的一种正渗透膜及其制备方法,传统正渗透膜的亲水改性都是通过增加聚合物中亲水性基团的含量或者与亲水性聚合物共混的方法,而本发明是利用紫外辐照接枝亲水性PSMP聚合物的方法只对多孔支撑层的底部和孔的内壁进行亲水性改性,这样既保持了活性皮层的稳定性,又近一步提高了正渗透膜的透水性能。本发明首次将牺牲层联合铸造制备底部大孔支撑层的方法与紫外辐照接枝亲水性PSMP聚合物改性的方法结合起来综合提升膜的正渗透性能。本发明操作步骤简单易行,效果稳定明显,透水性好,且正渗透的分离 选择性有很大提高。In summary, the present invention provides a forward osmosis membrane and a preparation method thereof. The hydrophilic modification of a conventional forward osmosis membrane is by increasing the content of a hydrophilic group in the polymer or co-synthesizing with a hydrophilic polymer. a method of mixing, and the method of grafting a hydrophilic PSMP polymer by ultraviolet irradiation only hydrophilically modifies the bottom of the porous support layer and the inner wall of the pore, thereby maintaining the stability of the active skin layer. Further improved the water permeability of the forward osmosis membrane. The invention combines the method of preparing the bottom macroporous support layer by the joint casting of the sacrificial layer for the first time and the method of modifying the hydrophilic PSMP polymer by the ultraviolet irradiation grafting to comprehensively improve the positive permeability of the membrane. The operation steps of the invention are simple and easy, the effect is stable and obvious, the water permeability is good, and the separation selectivity of the forward osmosis is greatly improved.
应当理解的是,本发明的应用不限于上述的举例,对本领域普通技术人员来说,可以根据上述说明加以改进或变换,所有这些改进和变换都应属于本发明所附权利要求的保护范围。It is to be understood that the application of the present invention is not limited to the above-described examples, and those skilled in the art can make modifications and changes in accordance with the above description, all of which are within the scope of the appended claims.
Claims (10)
- 一种正渗透膜的制备方法,其特征在于,包括:A method for preparing a forward osmosis membrane, comprising:步骤A、分别配置聚砜溶液和聚醚酰亚胺溶液,并分别将所述聚砜溶液和聚醚酰亚胺溶液在60-80℃下搅拌6-7小时;Step A, separately configuring a polysulfone solution and a polyetherimide solution, and respectively stirring the polysulfone solution and the polyetherimide solution at 60-80 ° C for 6-7 hours;步骤B、将聚醚酰亚胺溶液在玻璃板上刮制成聚醚酰亚胺薄膜,然后将聚砜溶液在聚醚酰亚胺薄膜上刮制成聚砜薄膜;Step B, the polyetherimide solution is scraped into a polyetherimide film on a glass plate, and then the polysulfone solution is scraped on the polyetherimide film to form a polysulfone film;步骤C、撕去所述聚醚酰亚胺薄膜得到聚砜支撑层,将靠近聚醚酰亚胺薄膜的一面作为所述聚砜支撑层的底部;Step C, tearing off the polyetherimide film to obtain a polysulfone support layer, and the side close to the polyetherimide film is used as the bottom of the polysulfone support layer;步骤D、将聚砜支撑层放入二苯甲酮的甲醇溶液中浸泡1.5-2.5小时,取出所述聚砜支撑层放入SMP溶液中,所述聚砜支撑层的底部朝向紫外灯,在紫外灯照射下在所述聚砜支撑层的底部和孔内壁接枝PSMP聚合物;Step D: The polysulfone support layer is immersed in a methanol solution of benzophenone for 1.5-2.5 hours, and the polysulfone support layer is taken out and placed in an SMP solution, and the bottom of the polysulfone support layer faces the ultraviolet lamp. Grafting a PSMP polymer on the bottom of the polysulfone support layer and the inner wall of the pore under irradiation of a UV lamp;步骤E、分别配置间苯二胺水溶液和均苯三甲酰氯正己烷溶液,将步骤D得到的聚砜支撑层顶部浸泡于间苯二胺水溶液3-10分钟;然后再将得到的聚砜支撑层顶部浸泡于均苯三甲酰氯正己烷溶液1-3分钟,在聚砜支撑层顶部制备得到活性皮层。Step E: separately dissolving the aqueous solution of m-phenylenediamine and the solution of trimellitic acid chloride in n-hexane, and immersing the top of the polysulfone support layer obtained in step D in the aqueous solution of m-phenylenediamine for 3-10 minutes; and then obtaining the obtained polysulfone support layer. The top was immersed in a solution of trimesoyl chloride in hexane for 1-3 minutes to prepare an active skin layer on top of the polysulfone support layer.
- 根据权利要求1所述的正渗透膜的制备方法,其特征在于,所述步骤A中,所述聚砜溶液由N,N-二甲基乙酰胺、聚乙二醇400和聚砜配置得到。The method for preparing a forward osmosis membrane according to claim 1, wherein in the step A, the polysulfone solution is configured by N,N-dimethylacetamide, polyethylene glycol 400 and polysulfone. .
- 根据权利要求1所述的正渗透膜的制备方法,其特征在于,所述步骤A中,所述聚醚酰亚胺溶液由N-甲基吡咯烷酮和聚醚酰亚胺配置得到。The method for preparing a forward osmosis membrane according to claim 1, wherein in the step A, the polyetherimide solution is obtained by disposing N-methylpyrrolidone and a polyetherimide.
- 根据权利要求1所述的正渗透膜的制备方法,其特征在于,所述步骤D之前包括步骤:将聚砜薄膜放入甲醇溶液中浸泡1.5-2.5小时。The method for preparing a forward osmosis membrane according to claim 1, wherein the step D comprises the step of: immersing the polysulfone membrane in a methanol solution for 1.5 to 2.5 hours.
- 根据权利要求1所述的正渗透膜的制备方法,其特征在于,所述步骤D中,所述二苯甲酮的甲醇溶液中,所述二苯甲酮的浓度为0.1-0.2mol/L。The method for preparing a forward osmosis membrane according to claim 1, wherein in the step D, the concentration of the benzophenone in the methanol solution of benzophenone is 0.1-0.2 mol/L. .
- 根据权利要求1所述的正渗透膜的制备方法,其特征在于,所述步骤D中,所述紫外灯照射的时间为20-40分钟。The method for preparing a forward osmosis membrane according to claim 1, wherein in the step D, the ultraviolet lamp is irradiated for a time of 20-40 minutes.
- 根据权利要求6所述的正渗透膜的制备方法,其特征在于,所述步骤D中,所述紫外灯照射的时间为30分钟。The method of preparing a forward osmosis membrane according to claim 6, wherein in the step D, the ultraviolet lamp is irradiated for 30 minutes.
- 一种正渗透膜,其特征在于,包括聚砜支撑层和复合于所述聚砜支撑层顶部的活性皮层,所述聚砜支撑层的底部和孔内壁接枝有PSMP聚合物;所述正渗透膜采用权利要求1-7任一项所述的方法制备得到。A forward osmosis membrane comprising a polysulfone support layer and an active skin layer compounded on top of the polysulfone support layer, wherein a bottom portion of the polysulfone support layer and an inner wall of the pore are grafted with a PSMP polymer; A permeable membrane is prepared by the method of any of claims 1-7.
- 根据权利要求8所述的正渗透膜,其特征在于,所述聚砜支撑层的孔径为25-35纳米。The forward osmosis membrane according to claim 8, wherein the polysulfone support layer has a pore diameter of 25 to 35 nm.
- 根据权利要求8所述的正渗透膜,其特征在于,所述聚砜支撑层的厚度为80-120微米,所述活性皮层的厚度为5-15纳米。The forward osmosis membrane according to claim 8, wherein the polysulfone support layer has a thickness of 80 to 120 μm and the active skin layer has a thickness of 5 to 15 nm.
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