CN105617882B - A kind of compound forward osmosis membrane of chitosan-modified stannic oxide/graphene nano and preparation method thereof - Google Patents
A kind of compound forward osmosis membrane of chitosan-modified stannic oxide/graphene nano and preparation method thereof Download PDFInfo
- Publication number
- CN105617882B CN105617882B CN201610024276.2A CN201610024276A CN105617882B CN 105617882 B CN105617882 B CN 105617882B CN 201610024276 A CN201610024276 A CN 201610024276A CN 105617882 B CN105617882 B CN 105617882B
- Authority
- CN
- China
- Prior art keywords
- chitosan
- membrane
- graphene oxide
- solution
- preparation
- 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.)
- Active
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 122
- 238000009292 forward osmosis Methods 0.000 title claims abstract description 51
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 229910021389 graphene Inorganic materials 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- 150000001875 compounds Chemical class 0.000 title 1
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical class O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 title 1
- 229920001661 Chitosan Polymers 0.000 claims abstract description 77
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims abstract description 51
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 20
- 238000000034 method Methods 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 239000000654 additive Substances 0.000 claims abstract description 12
- 230000000996 additive effect Effects 0.000 claims abstract description 10
- 239000002114 nanocomposite Substances 0.000 claims abstract description 8
- 239000000243 solution Substances 0.000 claims description 56
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 39
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 32
- 238000003756 stirring Methods 0.000 claims description 22
- 239000008367 deionised water Substances 0.000 claims description 17
- 229910021641 deionized water Inorganic materials 0.000 claims description 17
- 239000006185 dispersion Substances 0.000 claims description 15
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 claims description 13
- 239000011259 mixed solution Substances 0.000 claims description 13
- PEDCQBHIVMGVHV-UHFFFAOYSA-N glycerol group Chemical group OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 11
- 239000002994 raw material Substances 0.000 claims description 10
- 239000004695 Polyether sulfone Substances 0.000 claims description 9
- 229920006393 polyether sulfone Polymers 0.000 claims description 9
- LMDZBCPBFSXMTL-UHFFFAOYSA-N 1-Ethyl-3-(3-dimethylaminopropyl)carbodiimide Substances CCN=C=NCCCN(C)C LMDZBCPBFSXMTL-UHFFFAOYSA-N 0.000 claims description 8
- NQTADLQHYWFPDB-UHFFFAOYSA-N N-Hydroxysuccinimide Chemical compound ON1C(=O)CCC1=O NQTADLQHYWFPDB-UHFFFAOYSA-N 0.000 claims description 8
- 239000012535 impurity Substances 0.000 claims description 8
- 239000002033 PVDF binder Substances 0.000 claims description 7
- 229920002492 poly(sulfone) Polymers 0.000 claims description 7
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 235000010482 polyoxyethylene sorbitan monooleate Nutrition 0.000 claims description 5
- 229920000053 polysorbate 80 Polymers 0.000 claims description 5
- FPQQSJJWHUJYPU-UHFFFAOYSA-N 3-(dimethylamino)propyliminomethylidene-ethylazanium;chloride Chemical compound Cl.CCN=C=NCCCN(C)C FPQQSJJWHUJYPU-UHFFFAOYSA-N 0.000 claims description 4
- 230000006196 deacetylation Effects 0.000 claims description 4
- 238000003381 deacetylation reaction Methods 0.000 claims description 4
- -1 dimethylaminopropyl Chemical group 0.000 claims description 4
- 238000001132 ultrasonic dispersion Methods 0.000 claims description 3
- 239000004743 Polypropylene Substances 0.000 claims description 2
- 229920001155 polypropylene Polymers 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims 1
- DCPMPXBYPZGNDC-UHFFFAOYSA-N hydron;methanediimine;chloride Chemical compound Cl.N=C=N DCPMPXBYPZGNDC-UHFFFAOYSA-N 0.000 claims 1
- 238000002791 soaking Methods 0.000 claims 1
- 239000002131 composite material Substances 0.000 abstract description 29
- 150000003839 salts Chemical class 0.000 abstract description 21
- 229920005615 natural polymer Polymers 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- ZNZYKNKBJPZETN-WELNAUFTSA-N Dialdehyde 11678 Chemical compound N1C2=CC=CC=C2C2=C1[C@H](C[C@H](/C(=C/O)C(=O)OC)[C@@H](C=C)C=O)NCC2 ZNZYKNKBJPZETN-WELNAUFTSA-N 0.000 abstract description 2
- 239000011248 coating agent Substances 0.000 abstract description 2
- 238000000576 coating method Methods 0.000 abstract description 2
- 238000005520 cutting process Methods 0.000 abstract description 2
- 230000004907 flux Effects 0.000 description 24
- 239000010408 film Substances 0.000 description 19
- 238000010612 desalination reaction Methods 0.000 description 13
- 238000005516 engineering process Methods 0.000 description 8
- 238000011160 research Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 230000004048 modification Effects 0.000 description 7
- 238000012986 modification Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 5
- 230000035699 permeability Effects 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 238000012695 Interfacial polymerization Methods 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 235000011187 glycerol Nutrition 0.000 description 4
- 229920002521 macromolecule Polymers 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 3
- 239000013535 sea water Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 229920002284 Cellulose triacetate Polymers 0.000 description 2
- 229920002101 Chitin Polymers 0.000 description 2
- 239000004693 Polybenzimidazole Substances 0.000 description 2
- NNLVGZFZQQXQNW-ADJNRHBOSA-N [(2r,3r,4s,5r,6s)-4,5-diacetyloxy-3-[(2s,3r,4s,5r,6r)-3,4,5-triacetyloxy-6-(acetyloxymethyl)oxan-2-yl]oxy-6-[(2r,3r,4s,5r,6s)-4,5,6-triacetyloxy-2-(acetyloxymethyl)oxan-3-yl]oxyoxan-2-yl]methyl acetate Chemical compound O([C@@H]1O[C@@H]([C@H]([C@H](OC(C)=O)[C@H]1OC(C)=O)O[C@H]1[C@@H]([C@@H](OC(C)=O)[C@H](OC(C)=O)[C@@H](COC(C)=O)O1)OC(C)=O)COC(=O)C)[C@@H]1[C@@H](COC(C)=O)O[C@@H](OC(C)=O)[C@H](OC(C)=O)[C@H]1OC(C)=O NNLVGZFZQQXQNW-ADJNRHBOSA-N 0.000 description 2
- 230000003373 anti-fouling effect Effects 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000002329 infrared spectrum Methods 0.000 description 2
- 238000001728 nano-filtration Methods 0.000 description 2
- 229920002480 polybenzimidazole Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- ABFYEILPZWAIBN-UHFFFAOYSA-N 3-(iminomethylideneamino)-n,n-dimethylpropan-1-amine;hydrochloride Chemical compound Cl.CN(C)CCCN=C=N ABFYEILPZWAIBN-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 229920012266 Poly(ether sulfone) PES Polymers 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000004941 mixed matrix membrane Substances 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000000614 phase inversion technique Methods 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- 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
- B01D71/08—Polysaccharides
-
- 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
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0079—Manufacture of membranes comprising organic and inorganic components
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/445—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by forward osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/36—Hydrophilic membranes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本发明公开了一种壳聚糖修饰氧化石墨烯纳米复合正渗透膜及其制备方法,正渗透膜,由制膜液涂覆在超滤支撑底膜上制成,所述制膜液以质量百分比计由以下组分制成:壳聚糖修饰氧化石墨烯0.1%‑1.0%;壳聚糖2%‑5%;亲水添加剂0.1~0.3%;稀醋酸溶液91%‑97%;稀戊二醛溶液0.1~3%。本发明该方法操作简单,同时壳聚糖作为一种天然高分子聚合物,具有良好的亲水性和截盐性,同时复合正渗透膜制备成本低,在提高复合膜表面亲水性的同时,氧化石墨烯的独特片状结构可达到较好的截盐效果。
The invention discloses a chitosan-modified graphene oxide nanocomposite forward osmosis membrane and a preparation method thereof. The forward osmosis membrane is made by coating a membrane-making liquid on an ultrafiltration support base membrane. The percentage meter is made of the following components: chitosan modified graphene oxide 0.1%-1.0%; chitosan 2%-5%; hydrophilic additive 0.1-0.3%; dilute acetic acid solution 91%-97%; Dialdehyde solution 0.1-3%. The method of the present invention is simple to operate, and at the same time, chitosan, as a natural polymer, has good hydrophilicity and salt-cutting property, and at the same time, the preparation cost of the composite forward osmosis membrane is low, and while improving the hydrophilicity of the surface of the composite membrane, , the unique sheet-like structure of graphene oxide can achieve better salt interception effect.
Description
技术领域technical field
本发明属于膜分离技术领域,涉及一种壳聚糖修饰氧化石墨烯纳米复合正渗透膜的制备方法及产品。The invention belongs to the technical field of membrane separation, and relates to a preparation method and a product of a chitosan-modified graphene oxide nanocomposite forward osmosis membrane.
背景技术Background technique
水是生命之源,在当今世界能源紧缺,水和环境污染日益严重的形势下,海水淡化、苦咸水脱盐以及工业废水处理等方法成为获取淡水资源的主要手段。Water is the source of life. In today's world of energy shortages and increasingly serious water and environmental pollution, seawater desalination, brackish water desalination, and industrial wastewater treatment have become the main means of obtaining freshwater resources.
膜技术是一种新型分离技术,具有高效、节能、环保等优点,在海水淡化、脱盐以及食品加工、医药等方面引起了世界各国的高度重视。有研究报道表明,膜法脱盐技术占据世界水脱盐设备容量的44%。Membrane technology is a new type of separation technology, which has the advantages of high efficiency, energy saving, and environmental protection. It has attracted great attention from all over the world in seawater desalination, desalination, food processing, and medicine. Research reports have shown that membrane desalination technology accounts for 44% of the world's water desalination equipment capacity.
正渗透(FO)是一种新型膜分离技术,以膜两侧溶液渗透压差为驱动力,无需外加压力,从而达到分离、浓缩的目的,具有操作简单、能耗低、成本低等优势,主要用于海水脱盐、废水处理、食品加工、发电等方面。相比纳滤和反渗透等脱盐技术而言,正渗透技术由于其低能耗和工业污水零排放等优势,逐渐成为一种可替代性脱盐技术。Forward osmosis (FO) is a new type of membrane separation technology. It uses the osmotic pressure difference of the solution on both sides of the membrane as the driving force, without external pressure, so as to achieve the purpose of separation and concentration. It has the advantages of simple operation, low energy consumption, and low cost. Mainly used in seawater desalination, wastewater treatment, food processing, power generation, etc. Compared with desalination technologies such as nanofiltration and reverse osmosis, forward osmosis technology has gradually become an alternative desalination technology due to its advantages of low energy consumption and zero discharge of industrial sewage.
根据目前已有研究成果发现,正渗透膜材料的选择是正渗透技术的核心。理想的正渗透膜应具有以下特性:具有较薄的致密皮层,保证膜较高的截留性能并降低浓差极化;具有大孔结构的疏松支撑层,保证较高的水通量。用于正渗透膜研究较多的材料主要有:三醋酸纤维素(CTA)、聚苯并咪唑(PBI)、聚砜(PSf)、聚醚砜(PES)等。目前正渗透FO的制备主要有共混法和界面聚合法两种,共混法主要是将成膜材料如醋酸纤维、聚偏氟乙烯等与亲水纳米粒子共混以制备FO膜;界面聚合法,主要是采用亲水性物质如氧化石墨烯等改性超滤底膜,然后在超滤底膜表面进行界面聚合以制备具有超薄脱盐皮层的正渗透膜,这两种方法目前都得到了人们的广泛关注。According to the existing research results, the selection of forward osmosis membrane material is the core of forward osmosis technology. An ideal forward osmosis membrane should have the following characteristics: a thinner dense skin layer to ensure high membrane retention and reduce concentration polarization; a loose support layer with a macroporous structure to ensure higher water flux. The materials used for forward osmosis membrane research are mainly: cellulose triacetate (CTA), polybenzimidazole (PBI), polysulfone (PSf), polyethersulfone (PES) and so on. At present, the preparation of forward osmosis FO mainly includes blending method and interfacial polymerization method. The blending method is mainly to blend film-forming materials such as cellulose acetate and polyvinylidene fluoride with hydrophilic nanoparticles to prepare FO membranes; interfacial polymerization The method mainly uses hydrophilic substances such as graphene oxide to modify the ultrafiltration bottom membrane, and then performs interfacial polymerization on the surface of the ultrafiltration bottom membrane to prepare a forward osmosis membrane with an ultra-thin desalination skin layer. These two methods are currently available. received widespread attention.
近年来,由于氧化石墨烯(GO)良好的水溶性和表面活性,国内外很多学者将氧化石墨烯用于膜材料的共混改性,取得了很好的研究结果。氧化石墨烯可以有效提高超滤膜的亲水性、机械性能和盐截留率。Ganesh等人在研究中发现,在聚砜铸膜液中添加GO可以提高膜的亲水性能,同时对盐Na2SO4的截留率提高至74%(B.M.Ganesh,Arun M.Isloor,A.F.Ismail.Enhanced hydrophilicity and salt rejection study of grapheneoxide-polysulfone mixed matrix membrane.Desalination,313(2013)199-207)。Xu等人则把有机硅烷功能化的GO与聚偏氟乙烯(PVDF)进行共混制膜,所制备的超滤膜的机械强度和通量均有较大的改善,膜的表面粗糙度和抗污染性均有明显的改善(Z.W.Xu,J.G.Zhang,M.J.Shan,et al,Organosilane-functionalized graphene oxide for enhanced anti-fouling and mechanical properties of polyvinylidene fluoride ultrafiltrationmembranes,Journal of Membrane Science,458(2014)1-13)。In recent years, due to the good water solubility and surface activity of graphene oxide (GO), many scholars at home and abroad have used graphene oxide for blending and modification of membrane materials, and achieved good research results. Graphene oxide can effectively improve the hydrophilicity, mechanical properties and salt rejection of ultrafiltration membranes. In their research, Ganesh et al. found that adding GO to the polysulfone casting solution can improve the hydrophilic performance of the membrane, and at the same time increase the rejection rate of the salt Na 2 SO 4 to 74% (BMGanesh, Arun M.Isloor, AFIsmail.Enhanced Hydrophilicity and salt rejection study of graphene oxide-polysulfone mixed matrix membrane. Desalination, 313(2013) 199-207). Xu et al. blended organosilane-functionalized GO with polyvinylidene fluoride (PVDF) to form a membrane. The mechanical strength and flux of the prepared ultrafiltration membrane were greatly improved, and the surface roughness and The anti-fouling properties have been significantly improved (ZWXu, JG Zhang, MJ Shan, et al, Organosilane-functionalized graphene oxide for enhanced anti-fouling and mechanical properties of polyvinylidene fluoride ultrafiltration membranes, Journal of Membrane Science, 458(2014) 1-13).
氧化石墨烯在构建正渗透膜方面,也受到了广泛的关注。中国科技大学的徐铜文等(Y.Q.Wang,R.W.Ou,H.T.Wang,et al,Graphene oxide modified graphitic carbonnitride as a modifier for thin film composite forward osmosis membrane,Journal of Membrane Science,475(2015)281-289)将氧化石墨烯用于正渗透(FO)膜改性,采用氮化碳(CN)修饰氧化石墨烯,制备了功能性CN/rGO膜改性剂,对PES多孔支撑底膜进行了改性研究,发现改性后正渗透膜的水通量获得了很大的提高。由于膜内浓差极化会影响正渗透膜的水通量及分离性,CN/rGO有效改善了多孔支撑层的结构和亲水性,从而减小了膜内浓差极化的影响。王立国等在其专利(王立国;史新莲;李媛,等,一种高性能平板式醋酸纤维素/石墨烯共混正渗透膜;公开号CN104474919A;公开日:2015-04-01)中公开了一种高性能平板式醋酸纤维素/石墨烯共混正渗透膜,其制备方法是将醋酸纤维素、添加剂、石墨烯及二甲基甲酰胺或二甲基乙酰胺或N-甲基吡咯烷酮与丙酮混合溶剂,配制成正渗透膜铸膜液,在支撑材料上采用相转化法制备了高性能平板式醋酸纤维素/石墨烯共混正渗透膜。东华大学的李方等在其发明专利中提出了一种氨基改性氧化石墨烯复合正渗透膜的制备方法(李方;赵永军;李佳峰,等,一种氨基改性氧化石墨烯复合正渗透膜的制备方法;公开号CN103861472A;公开日:2014-06-18),其制备方法是将氧化石墨烯、二甲基甲酰胺、有机胺和二环己基碳酰亚胺混合,超声,然后在100~150℃下反应40~50h,加入无水乙醇,经静置,过滤,所得沉淀经洗涤,烘干处理后,得到氨基改性氧化石墨烯;将氨基改性氧化石墨烯和溶剂混合、超声,然后将添加剂和成膜聚合物加到上述混合液中配制成铸膜液,经脱泡后,采用相转化法制成基膜,纯水浸泡备用,然后采用界面聚合法制备了具有脱盐皮层的FO膜。本发明机械强度高、化学稳定性好,纯水渗透通量大和盐截留率高。Graphene oxide has also received extensive attention in the construction of forward osmosis membranes. Xu Tongwen from the University of Science and Technology of China (Y.Q.Wang, R.W.Ou, H.T.Wang, et al, Graphene oxide modified graphitic carbonnitride as a modifier for thin film composite forward osmosis membrane, Journal of Membrane Science, 475(2015) 281-289) oxidized Graphene is used for the modification of forward osmosis (FO) membrane, and carbon nitride (CN) is used to modify graphene oxide to prepare a functional CN/rGO membrane modifier. The water flux of the modified forward osmosis membrane has been greatly improved. Since the concentration polarization in the membrane will affect the water flux and separation of the forward osmosis membrane, CN/rGO can effectively improve the structure and hydrophilicity of the porous support layer, thereby reducing the influence of the concentration polarization in the membrane. Wang Liguo et al. disclosed in their patents (Wang Liguo; Shi Xinlian; Li Yuan, etc., a high-performance flat cellulose acetate/graphene blended forward osmosis membrane; publication number CN104474919A; publication date: 2015-04-01). A kind of high-performance flat type cellulose acetate/graphene blending forward osmosis membrane, its preparation method is that cellulose acetate, additive, graphene and dimethyl formamide or dimethyl acetamide or N-methylpyrrolidone and acetone The mixed solvent was prepared as a forward osmosis membrane casting solution, and a high-performance flat cellulose acetate/graphene blended forward osmosis membrane was prepared on a support material by a phase inversion method. Li Fang of Donghua University, etc. proposed a method for preparing an amino-modified graphene oxide composite forward osmosis membrane in their invention patent (Li Fang; Zhao Yongjun; Li Jiafeng, et al., an amino-modified graphene oxide composite forward osmosis membrane The preparation method of film; publication number CN103861472A; publication date: 2014-06-18), its preparation method is to mix graphene oxide, dimethylformamide, organic amine and dicyclohexyl carboximide, ultrasonic, and then React at 100-150°C for 40-50 hours, add absolute ethanol, stand still, filter, and the obtained precipitate is washed and dried to obtain amino-modified graphene oxide; mix amino-modified graphene oxide with a solvent, Ultrasound, then add additives and film-forming polymers to the above mixed solution to prepare a casting solution, after degassing, use the phase inversion method to make a base film, soak in pure water for later use, and then use the interfacial polymerization method to prepare a desalination skin layer FO membrane. The invention has high mechanical strength, good chemical stability, large permeation flux of pure water and high salt retention rate.
上述报道表明,GO在改善聚合物多孔基膜等方面具有明显的优势,可以大大提高膜的亲水性和抗污染性,为GO用于改善正渗透多孔支撑膜的研究提供技术支持。但上述研究中主要是将氧化石墨烯先与PES通过共混相转化法制备超滤膜材料,然后通过界面聚合来制备超薄脱盐皮层,存在制膜工艺复杂,膜的水通量不好控制等问题。此外,直接将氧化石墨烯用于膜的改性,还存在氧化石墨烯容易流失的问题,如果能对氧化石墨烯进行大分子改性,通过大分子的作用固定住氧化石墨烯,同时对氧化石墨烯进行功能化改性,也是一种很好的膜改性手段。The above reports show that GO has obvious advantages in improving polymer porous base membranes, etc., and can greatly improve the hydrophilicity and anti-fouling properties of membranes, providing technical support for the research of GO in improving porous support membranes of forward osmosis. However, in the above research, the ultrafiltration membrane material is first prepared by blending graphene oxide with PES through the phase inversion method, and then the ultra-thin desalination skin layer is prepared by interfacial polymerization. The membrane making process is complicated, and the water flux of the membrane is not easy to control, etc. question. In addition, if graphene oxide is directly used for membrane modification, there is still the problem that graphene oxide is easy to lose. If graphene oxide can be modified with macromolecules, graphene oxide can be fixed through the action of macromolecules, and at the same time Functional modification of graphene is also a good means of membrane modification.
在众多高分子中,壳聚糖(CS)是一种可生物降解、无毒、具有生物和血液相容性、可重复利用的天然高分子多糖,在自然界分布广泛,且来源丰富。它在环境、医药、食品、化工、膜分离等领域均具有很好的应用价值。作为一种天然高分子膜材料,已被广泛用于制备超滤、纳滤、反渗透膜以及智能响应性膜等。目前,关于壳聚糖膜的研究主要是提高壳聚糖膜的耐水性、渗透性、荷电性和机械性能等。Ma等(B.M.Ma,A.W.Qin,X.Li,et al,Structureand properties of chitin whisker reinforced chitosan membranes,InternationalJournal of Biological Macromolecules,64(2014)341-346)将甲壳质晶须作为添加剂改性壳聚糖膜,经改性后,壳聚糖复合膜的张力强度是纯壳聚糖膜的2.8倍。雷思宇等在其申请的专利文献(雷思宇,林大伟;一种有机硅改性壳聚糖膜的制备方法;公开号:CN105037768A;公开日:2015-11-11)中公布了一种有机硅改性壳聚糖膜的制备方法,通过环氧基聚硅氧烷与壳聚糖在醋酸溶液中反应,采用流延法制膜,所获得的改性壳聚糖膜具有优异的耐水性、耐高温低温性和透气性,膜的断裂伸长率提高30%以上,柔韧性显著提高。同时,壳聚糖修饰氧化石墨烯纳米复合材料由于具有良好的吸附性能,常用于水中重金属离子、有机染料等的吸附及脱附再生。因此,目前CS-GO主要是将其作为吸附剂用于对水溶液中有机污染物和重金属离子的吸附去除,在正渗透膜领域的研究尚未见报道。Among many polymers, chitosan (CS) is a biodegradable, non-toxic, bio- and blood-compatible, and reusable natural polymer polysaccharide, which is widely distributed in nature and has abundant sources. It has good application value in the fields of environment, medicine, food, chemical industry, membrane separation and so on. As a natural polymer membrane material, it has been widely used in the preparation of ultrafiltration, nanofiltration, reverse osmosis membranes and intelligent responsive membranes. At present, the research on chitosan membrane is mainly to improve the water resistance, permeability, chargeability and mechanical properties of chitosan membrane. Ma et al. (B.M.Ma, A.W.Qin, X.Li, et al, Structure and properties of chitin whisker reinforced chitosan membranes, International Journal of Biological Macromolecules, 64(2014) 341-346) used chitin whiskers as an additive to modify chitosan membrane, after modification, the tensile strength of the chitosan composite membrane is 2.8 times that of the pure chitosan membrane. Lei Siyu et al. published a patent document (Lei Siyu, Lin Dawei; a preparation method of organosilicon-modified chitosan film; publication number: CN105037768A; publication date: 2015-11-11) The preparation method of organosilicon modified chitosan film, through the reaction of epoxy polysiloxane and chitosan in acetic acid solution, the film is made by casting method, and the obtained modified chitosan film has excellent water resistance , high temperature and low temperature resistance and air permeability, the elongation at break of the film is increased by more than 30%, and the flexibility is significantly improved. At the same time, chitosan-modified graphene oxide nanocomposites are often used for adsorption and desorption regeneration of heavy metal ions and organic dyes in water due to their good adsorption properties. Therefore, at present, CS-GO is mainly used as an adsorbent for the adsorption and removal of organic pollutants and heavy metal ions in aqueous solution, and the research in the field of forward osmosis membrane has not been reported yet.
发明内容Contents of the invention
本发明提供了一种壳聚糖修饰氧化石墨烯纳米复合正渗透膜及其制备方法,该方法操作简单,同时壳聚糖作为一种天然高分子聚合物,具有良好的亲水性和截盐性,同时复合正渗透膜制备成本低,在提高复合膜表面亲水性的同时,氧化石墨烯的独特片状结构可达到较好的截盐效果。The invention provides a chitosan-modified graphene oxide nanocomposite forward osmosis membrane and a preparation method thereof. The method is simple to operate, and at the same time, chitosan, as a natural polymer, has good hydrophilicity and salt-cutting properties At the same time, the preparation cost of the composite forward osmosis membrane is low. While improving the hydrophilicity of the composite membrane surface, the unique sheet-like structure of graphene oxide can achieve a better salt interception effect.
一种壳聚糖修饰氧化石墨烯纳米复合正渗透膜,由制膜液涂覆在超滤支撑底膜上制成,A chitosan-modified graphene oxide nanocomposite forward osmosis membrane is made by coating the membrane-making solution on the ultrafiltration support base membrane,
所述制膜液以质量百分比计由以下组分制成:The film-making solution is made of the following components in mass percent:
壳聚糖本身是一种亲水性和荷电性很好的成膜材料,它与CS-GO具有很好的相容性,可以保证膜在应用过程中氧化石墨烯不会从膜中脱离出来,同时CS-GO对改善壳聚糖复合膜的机械性能以及渗透性和脱盐性能均具有积极的意义。Chitosan itself is a film-forming material with good hydrophilicity and chargeability, and it has good compatibility with CS-GO, which can ensure that graphene oxide will not detach from the film during the application process of the film. At the same time, CS-GO has positive significance for improving the mechanical properties, permeability and desalination performance of chitosan composite membranes.
优选地,所述壳聚糖修饰氧化石墨烯由如下方法制备:Preferably, the chitosan-modified graphene oxide is prepared by the following method:
(1)将氧化石墨烯(GO)超声分散在去离子水中,然后加入1-乙基-(3-二甲基氨基丙基)碳二亚胺盐酸盐(EDC·HCl)和N-羟基琥珀酰亚胺(NHS),继续搅拌0.5~1.5h;(1) Ultrasonic disperse graphene oxide (GO) in deionized water, then add 1-ethyl-(3-dimethylaminopropyl)carbodiimide hydrochloride (EDC·HCl) and N-hydroxy Succinimide (NHS), continue to stir for 0.5 ~ 1.5h;
(2)步骤(1)反应结束后缓慢加入壳聚糖(CS)溶液,于50~70℃反应0.5~1.5h;冷却至室温后进行后处理即得;氧化石墨烯、1-乙基-(3-二甲基氨基丙基)碳二亚胺盐酸盐、N-羟基琥珀酰亚胺和壳聚糖的质量比为1:(0.5~2.5):(0.5~1.5):(2.5~3.5)。(2) After the reaction in step (1), slowly add chitosan (CS) solution, react at 50-70°C for 0.5-1.5h; cool to room temperature and perform post-treatment; graphene oxide, 1-ethyl- The mass ratio of (3-dimethylaminopropyl) carbodiimide hydrochloride, N-hydroxysuccinimide and chitosan is 1:(0.5~2.5):(0.5~1.5):(2.5~ 3.5).
上述步骤(2)中所述的壳聚糖溶液的滴加速率控制在0.1~0.2mL/min;最优选为0.15mL/min。若滴加速度过快,会影响壳聚糖与氧化石墨烯的反应程度。壳聚糖溶液的溶剂为体积分数为1%的稀醋酸溶液,若醋酸溶液浓度过高会降低壳聚糖的溶解,壳聚糖分子量为50KDa-200KDa。The dropping rate of the chitosan solution described in the above step (2) is controlled at 0.1 to 0.2 mL/min; most preferably 0.15 mL/min. If the dropping speed is too fast, it will affect the reaction degree of chitosan and graphene oxide. The solvent of the chitosan solution is a dilute acetic acid solution with a volume fraction of 1%. If the concentration of the acetic acid solution is too high, the dissolution of the chitosan will be reduced. The molecular weight of the chitosan is 50KDa-200KDa.
上述步骤(1)中氧化石墨烯在去离子水中的超声分散时间为1.5~2.5h。进一步优选为2h。The ultrasonic dispersion time of graphene oxide in deionized water in the above step (1) is 1.5-2.5 hours. More preferably 2h.
上述步骤(2)中的反应时间进一步优选为2h。The reaction time in the above step (2) is further preferably 2h.
上述步骤(2)中的后处理步骤为:后用1%(W/V)的NaOH水溶液和去离子水洗涤数次直至pH约为7.0,40℃真空干燥即可得到。The post-treatment step in the above step (2) is: wash with 1% (W/V) NaOH aqueous solution and deionized water for several times until the pH is about 7.0, and vacuum-dry at 40° C. to obtain it.
氧化石墨烯、1-乙基-(3-二甲基氨基丙基)碳二亚胺盐酸盐、N-羟基琥珀酰亚胺和壳聚糖的质量比(GO/EDC·HCl/NHS/CS)最优选为1:2:1:3。The mass ratio of graphene oxide, 1-ethyl-(3-dimethylaminopropyl) carbodiimide hydrochloride, N-hydroxysuccinimide and chitosan (GO/EDC·HCl/NHS/ CS) is most preferably 1:2:1:3.
所述氧化石墨烯(GO)为商品化产品。The graphene oxide (GO) is a commercial product.
优选地,壳聚糖分子量为100KDa-500KDa,脱乙酰度80-95%,醋酸溶液的质量分数为1.5~2.5%。Preferably, the molecular weight of chitosan is 100KDa-500KDa, the degree of deacetylation is 80-95%, and the mass fraction of the acetic acid solution is 1.5-2.5%.
优选地,所述超滤支撑底膜为聚偏氟乙烯膜、聚醚砜膜、磺化聚醚砜膜、聚砜膜或聚丙烯超滤膜。底膜在使用前应经过浸泡、晾干后使用。Preferably, the ultrafiltration support bottom membrane is polyvinylidene fluoride membrane, polyethersulfone membrane, sulfonated polyethersulfone membrane, polysulfone membrane or polypropylene ultrafiltration membrane. The base film should be soaked and dried before use.
所述亲水添加剂为甘油或吐温80。The hydrophilic additive is glycerin or Tween 80.
戊二醛溶液的质量浓度为45%~55%,优选为50%。The mass concentration of the glutaraldehyde solution is 45%-55%, preferably 50%.
本发明中壳聚糖中氨基与氧化石墨烯中环氧基反应并与壳聚糖本体在商品化膜表面共混交联,以获得一种纳米复合正渗透膜。在氧化石墨烯与壳聚糖混合之前,经过分子量在50KDa-200KDa的壳聚糖修饰,可提高其与步骤(2)中分子量在100KDa-500KDa的壳聚糖的相容性。在本发明中,壳聚糖-氧化石墨烯(GO-CS)纳米材料可以有效提高复合层的渗透性和截盐率,而壳聚糖本体可以有效提高复合层的亲水性和荷电性,以提高正渗透复合膜的总体渗透性能和截盐率。In the present invention, amino groups in chitosan react with epoxy groups in graphene oxide and are blended and cross-linked with chitosan body on the surface of a commercial membrane to obtain a nanocomposite forward osmosis membrane. Before the graphene oxide is mixed with the chitosan, the chitosan with a molecular weight of 50KDa-200KDa is modified to improve its compatibility with the chitosan with a molecular weight of 100KDa-500KDa in step (2). In the present invention, chitosan-graphene oxide (GO-CS) nanomaterials can effectively improve the permeability and salt interception rate of the composite layer, while chitosan itself can effectively improve the hydrophilicity and chargeability of the composite layer , in order to improve the overall permeability and salt rejection rate of forward osmosis composite membrane.
与现有正渗透膜相比,本发明的正渗透膜的水通量大于12L/m2·h,且截盐性能也有很大的提高。Compared with the existing forward osmosis membrane, the water flux of the forward osmosis membrane of the present invention is greater than 12L/m 2 ·h, and the salt interception performance is also greatly improved.
本发明的制膜液,一种更有选的技术方案,以质量百分比计由以下组分制成:Membrane-making liquid of the present invention, a kind of more selected technical scheme, is made up of following component by mass percent:
在该优选组合下,正渗透膜的水通量大于15L/m2·h,反向盐通量在4.5g/m2·h以下。Under this preferred combination, the water flux of the forward osmosis membrane is greater than 15 L/m 2 ·h, and the reverse salt flux is below 4.5 g/m 2 ·h.
本发明的制膜液,最优选地,以质量百分比计由以下组分制成:Membrane-making solution of the present invention, most preferably, is made up of following components in mass percent:
在该优选组合下,正渗透膜的水通量大于20L/m2·h,反向盐通量为4.0g/m2·h以下。Under this preferred combination, the water flux of the forward osmosis membrane is greater than 20 L/m 2 ·h, and the reverse salt flux is below 4.0 g/m 2 ·h.
本发明提供一种壳聚糖修饰氧化石墨烯纳米复合正渗透膜,包括如下步骤:The invention provides a chitosan-modified graphene oxide nanocomposite forward osmosis membrane, comprising the steps of:
(1)将壳聚糖、亲水添加剂按配比溶于稀醋酸溶液中,50~70℃(优选60℃)搅拌至壳聚糖完全溶解后抽滤去除不溶性杂质,然后按配比加入经超声分散处理的壳聚糖修饰氧化石墨烯分散液,50~70℃(优选60℃)搅拌至分散均匀得混合液;(1) Dissolve chitosan and hydrophilic additives in dilute acetic acid solution according to the proportion, stir at 50-70°C (preferably 60°C) until the chitosan is completely dissolved, then remove the insoluble impurities by suction filtration, and then add according to the proportion by ultrasonic dispersion The treated chitosan-modified graphene oxide dispersion is stirred at 50 to 70°C (preferably 60°C) until uniformly dispersed to obtain a mixed liquid;
以质量百分比计原料配比为:The ratio of raw materials in terms of mass percentage is:
(2)将所得混合液真空脱泡后加入稀戊二醛溶液,混合均匀后刮制在滤支撑底膜上,室温下水平放置2-6h后40~60℃烘干,以质量百分比计,稀戊二醛二醛溶液占原料的0.1~3%;(2) Add dilute glutaraldehyde solution to the obtained mixed solution after vacuum defoaming, mix evenly and scrape it on the bottom membrane of the filter support, place it horizontally at room temperature for 2-6 hours, and then dry it at 40-60°C, in terms of mass percentage, Dilute glutaraldehyde dialdehyde solution accounts for 0.1-3% of raw materials;
(3)将烘干后的膜浸入氢氧化钠和乙醇混合溶液中0.5~1.5h,水洗、晾干即得;(3) Immerse the dried film in a mixed solution of sodium hydroxide and ethanol for 0.5 to 1.5 hours, wash it with water, and dry it in the air;
氢氧化钠和乙醇混合溶液中氢氧化钠溶液与乙醇的体积比为2:1,其中氢氧化钠溶液的质量浓度为3%,乙醇的纯度为50%。The volume ratio of sodium hydroxide solution to ethanol in the mixed solution of sodium hydroxide and ethanol is 2:1, wherein the mass concentration of sodium hydroxide solution is 3%, and the purity of ethanol is 50%.
优选地,步骤(2)中在支撑底膜上的所刮液膜的厚度为5~30μm。Preferably, the thickness of the scraped liquid film on the supporting base film in step (2) is 5-30 μm.
所述的脱泡处理可选用多种脱泡处理方式,优选的脱泡处理方式为:将CS/GO-CS溶液抽真空,静置时间30分钟,待气泡全部跑出后,将CS/GO-CS溶液取出,所述的静置时间不宜过长,静止时间过长醋酸易挥发,会影响壳聚糖的溶解,另外氧化石墨烯会产生部分沉积,最终会影响复合正渗透膜的性能。A variety of defoaming treatment methods can be selected for the defoaming treatment. The preferred defoaming treatment method is: vacuumize the CS/GO-CS solution, let it stand for 30 minutes, and after all the bubbles run out, put the CS/GO-CS solution -CS solution is taken out, and the standing time should not be too long. If the standing time is too long, acetic acid is volatile, which will affect the dissolution of chitosan. In addition, graphene oxide will produce partial deposition, which will eventually affect the performance of the composite forward osmosis membrane.
本发明工艺简单,制备成本低,满足绿色生产的要求。The invention has simple process, low preparation cost and meets the requirement of green production.
附图说明Description of drawings
图1是纯CS膜和CS/CS-GO复合FO膜的表面红外光谱(-N-H基峰是CS-GO的特征峰)Figure 1 is the surface infrared spectrum of pure CS membrane and CS/CS-GO composite FO membrane (the -N-H base peak is the characteristic peak of CS-GO)
具体实施方式Detailed ways
下述实施方式中所使用的表征方法主要有:The characterization methods used in the following embodiments mainly include:
膜表面的化学组成和结构:全反射红外光谱仪(VERTEX 70,德国)测定。Chemical composition and structure of the film surface: measured by total reflection infrared spectrometer (VERTEX 70, Germany).
膜渗透通量测定:通过实验室专用正渗透膜测试装置对正渗透膜的水通量和反向盐通量进行测定,并采用0.5mol/L Na2SO4水溶液作为驱动液。正渗透膜的水通量按照公式(1)可以计算出单位时间,单位膜有效面积通过的水通量。Membrane permeation flux measurement: The water flux and reverse salt flux of the forward osmosis membrane are measured by the laboratory-specific forward osmosis membrane test device, and 0.5mol/L Na 2 SO 4 aqueous solution is used as the driving solution. The water flux of the forward osmosis membrane can be calculated according to the formula (1) per unit time and the water flux passing through the effective area of the membrane.
式中:Jw为正渗透水通量,L/m2h;Δm为汲取液质量的增加值,kg;ρ为纯水的密度,kg/m3;S为正渗透有效面积,m2;t为时间,h。In the formula: J w is the forward osmosis water flux, L/m 2 h; Δm is the added value of the drawn liquid mass, kg; ρ is the density of pure water, kg/m 3 ; S is the effective area of forward osmosis, m 2 ; t is time, h.
膜渗透过程中反向盐通量按照公式(2)可以计算出单位时间,单位膜有效面积通过的反相盐通量。The reverse salt flux in the membrane permeation process can be calculated according to the formula (2) per unit time, and the reverse salt flux passing through the effective area of the membrane.
式中Js为反相盐通量,g/m2h;C为汲取液中盐浓度,由电导率推算可得,mol/L,V为运行t时间后汲取液体积;MNaCl为氯化钠的相对分子质量;s为正渗透有效面积,m2;t为时间,h。In the formula, J s is the reverse-phase salt flux, g/m 2 h; C is the salt concentration in the draw solution, which can be calculated from the conductivity, mol/L, and V is the volume of the draw solution after running for t time; M NaCl is the chlorine Relative molecular mass of sodium chloride; s is the effective area of forward osmosis, m 2 ; t is time, h.
下面将结合下文的实例对本发明做更详细的描述,但所述实例不构成对本发明的限制。The present invention will be described in more detail below in conjunction with the following examples, but the examples do not constitute a limitation to the present invention.
壳聚糖修饰的氧化石墨烯制备方法如下:The graphene oxide preparation method of chitosan modification is as follows:
将商品化氧化石墨烯(GO)加入到去离子水中,超声分散2h,然后加入1-乙基-(3-二甲基氨基丙基)碳二亚胺盐酸盐(EDC·HCl)和N-羟基琥珀酰亚胺(NHS),连续搅拌1h,然后将壳聚糖(CS,50KDa-200KDa,脱乙酰度80-95%,溶剂为体积分数为1%的稀醋酸溶液)溶液以0.15mL/min缓慢加入到GO分散液中,于60℃反应1h,冷却至室温后离心,各反应物质之间的质量比GO/EDC·HCl/NHS/CS=1:(0.5~2.5):(0.5~1.5):(2.5~3.5)(优选采用1:2:1:3)。然后用1%(W/V)的NaOH水溶液和去离子水洗涤数次直至pH约为7.0,40℃真空干燥即可得到壳聚糖大分子修饰的氧化石墨烯改性剂(CS-GO)。Commercially available graphene oxide (GO) was added to deionized water, ultrasonically dispersed for 2 h, and then 1-ethyl-(3-dimethylaminopropyl)carbodiimide hydrochloride (EDC·HCl) and N -Hydroxysuccinimide (NHS), continuously stirred for 1h, then chitosan (CS, 50KDa-200KDa, deacetylation degree 80-95%, solvent is 1% dilute acetic acid solution by volume fraction) solution in 0.15mL Slowly added to the GO dispersion at 60°C for 1 hour, cooled to room temperature and then centrifuged, the mass ratio between the reaction substances GO/EDC·HCl/NHS/CS=1:(0.5~2.5):(0.5 ~1.5): (2.5~3.5) (1:2:1:3 is preferred). Then wash several times with 1% (W/V) NaOH aqueous solution and deionized water until the pH is about 7.0, and vacuum-dry at 40°C to obtain the graphene oxide modifier (CS-GO) modified by chitosan macromolecules .
以下实施例中所用稀醋酸的质量浓度为2%;稀戊二醛溶液的质量浓度为50%The mass concentration of dilute acetic acid used in the following examples is 2%; The mass concentration of dilute glutaraldehyde solution is 50%
实施例1Example 1
将壳聚糖修饰的氧化石墨烯(CS-GO)加入到去离子水中,超声分散2小时,获得均匀的CS-GO分散液;将壳聚糖和亲水添加剂(甘油)按配方溶于稀醋酸中,60℃下连续搅拌6小时,抽滤,去除不溶性杂质。然后将CS-GO分散液加入到壳聚糖溶液中,继续在60℃下连续搅拌2h。Chitosan-modified graphene oxide (CS-GO) was added to deionized water, and ultrasonically dispersed for 2 hours to obtain a uniform CS-GO dispersion; chitosan and hydrophilic additive (glycerin) were dissolved in dilute In acetic acid, stir continuously at 60°C for 6 hours, and filter with suction to remove insoluble impurities. Then the CS-GO dispersion was added to the chitosan solution and continued to stir continuously at 60 °C for 2 h.
将上述CS/CS-GO溶液脱泡后,加入配方量的稀戊二醛溶液,搅拌均匀后,在聚砜超滤底膜上刮制30μm厚度的薄层液膜,将其在室温下水平放置2h,然后将其放入50℃的烘箱中烘干。烘干后的复合膜浸泡入氢氧化钠和乙醇混合溶液(混合体积比2:1,氢氧化钠溶液的质量浓度为3%,乙醇的纯度为50%)中继续处理1h,然后再用去离子水反复清洗复合膜,最后将膜晾干即可得正渗透复合膜。After defoaming the above CS/CS-GO solution, add the formulated amount of dilute glutaraldehyde solution, stir evenly, scrape a thin layer of liquid film with a thickness of 30 μm on the polysulfone ultrafiltration bottom membrane, and place it horizontally at room temperature Leave it for 2 hours, then dry it in an oven at 50°C. The dried composite film was immersed in a mixed solution of sodium hydroxide and ethanol (mixing volume ratio 2:1, the mass concentration of sodium hydroxide solution was 3%, and the purity of ethanol was 50%) to continue treatment for 1h, and then used The composite membrane is washed repeatedly with ion water, and finally the membrane is dried to obtain a forward osmosis composite membrane.
原料配方及获得的正渗透膜渗透通量和截盐性能于表1所示。The raw material formula and the permeation flux and salt interception performance of the obtained forward osmosis membrane are shown in Table 1.
实施例2Example 2
将壳聚糖修饰的氧化石墨烯(CS-GO)加入到去离子水中,超声分散2小时,获得均匀的CS-GO分散液;将壳聚糖和亲水添加剂(吐温80)按配方溶于稀醋酸中,60℃下连续搅拌8小时,抽滤,去除不溶性杂质。然后将CS-GO分散液加入到壳聚糖溶液中,继续在60℃下连续搅拌4h。Chitosan-modified graphene oxide (CS-GO) was added to deionized water, and ultrasonically dispersed for 2 hours to obtain a uniform CS-GO dispersion; chitosan and hydrophilic additive (Tween 80) were dissolved according to the formula In dilute acetic acid, stir continuously at 60°C for 8 hours, and filter with suction to remove insoluble impurities. Then the CS-GO dispersion was added to the chitosan solution and continued to stir continuously at 60 °C for 4 h.
将上述CS/CS-GO溶液脱泡后,加入配方量的稀戊二醛溶液,搅拌均匀后,在聚醚砜超滤底膜上刮制20μm厚度的薄层液膜,将其在室温下水平放置4h,然后将其放入50℃的烘箱中烘干。烘干后的复合膜浸泡入氢氧化钠和乙醇混合溶液中继续处理1h,然后再用去离子水反复清洗复合膜,最后将膜晾干即可得正渗透复合膜。After defoaming the above CS/CS-GO solution, add the formula amount of dilute glutaraldehyde solution, stir evenly, scrape a thin layer of liquid film with a thickness of 20 μm on the polyethersulfone ultrafiltration bottom membrane, and place it at room temperature Place it horizontally for 4 hours, and then dry it in an oven at 50°C. The dried composite membrane is soaked in a mixed solution of sodium hydroxide and ethanol to continue treatment for 1 hour, then the composite membrane is repeatedly washed with deionized water, and finally the membrane is dried to obtain a forward osmosis composite membrane.
原料配方及获得的正渗透膜渗透通量和截盐性能于表1所示。The raw material formula and the permeation flux and salt interception performance of the obtained forward osmosis membrane are shown in Table 1.
实施例3Example 3
将壳聚糖修饰的氧化石墨烯(CS-GO)加入到去离子水中,超声分散2小时,获得均匀的CS-GO分散液;将壳聚糖和亲水添加剂(甘油)按配方溶于稀醋酸中,60℃下连续搅拌10小时,抽滤,去除不溶性杂质。然后将CS-GO分散液加入到壳聚糖溶液中,继续在60℃下连续搅拌6h。Chitosan-modified graphene oxide (CS-GO) was added to deionized water, and ultrasonically dispersed for 2 hours to obtain a uniform CS-GO dispersion; chitosan and hydrophilic additive (glycerin) were dissolved in dilute In acetic acid, stir continuously at 60°C for 10 hours, and filter with suction to remove insoluble impurities. Then the CS-GO dispersion was added into the chitosan solution and continued to stir continuously at 60 °C for 6 h.
将上述CS/CS-GO溶液脱泡后,加入配方量的稀戊二醛溶液,搅拌均匀后,在聚醚砜超滤底膜上刮制10μm厚度的薄层液膜,将其在室温下水平放置6h,然后将其放入50℃的烘箱中烘干。烘干后的复合膜浸泡入氢氧化钠和乙醇混合溶液中继续处理1h,然后再用去离子水反复清洗复合膜,最后将膜晾干即可得正渗透复合膜。After defoaming the above CS/CS-GO solution, add the formulated amount of dilute glutaraldehyde solution, stir evenly, scrape a thin layer of liquid film with a thickness of 10 μm on the polyethersulfone ultrafiltration bottom membrane, and place it at room temperature Place it horizontally for 6 hours, and then put it into an oven at 50°C for drying. The dried composite membrane is soaked in a mixed solution of sodium hydroxide and ethanol to continue treatment for 1 hour, then the composite membrane is repeatedly washed with deionized water, and finally the membrane is dried to obtain a forward osmosis composite membrane.
原料配方及获得的正渗透膜渗透通量和截盐性能于表1所示。The raw material formula and the permeation flux and salt interception performance of the obtained forward osmosis membrane are shown in Table 1.
如此获得的正渗透膜何纯壳聚糖的红外光谱图如图1所示。The infrared spectrum of the obtained forward osmosis membrane and pure chitosan is shown in Figure 1.
实施例4Example 4
将壳聚糖修饰的氧化石墨烯(CS-GO)加入到去离子水中,超声分散2小时,获得均匀的CS-GO分散液;将壳聚糖和亲水添加剂(吐温80)按配方溶于稀醋酸中,60℃下连续搅拌12小时,抽滤,去除不溶性杂质。然后将CS-GO分散液加入到壳聚糖溶液中,继续在60℃下连续搅拌2h。Chitosan-modified graphene oxide (CS-GO) was added to deionized water, and ultrasonically dispersed for 2 hours to obtain a uniform CS-GO dispersion; chitosan and hydrophilic additive (Tween 80) were dissolved according to the formula In dilute acetic acid, stir continuously at 60°C for 12 hours, and filter with suction to remove insoluble impurities. Then the CS-GO dispersion was added to the chitosan solution and continued to stir continuously at 60 °C for 2 h.
将上述CS/CS-GO溶液脱泡后,加入配方量的稀戊二醛溶液,搅拌均匀后,在磺化聚醚砜超滤底膜上刮制5μm厚度的薄层液膜,将其在室温下水平放置4h,然后将其放入50℃的烘箱中烘干。烘干后的复合膜浸泡入氢氧化钠和乙醇混合溶液中继续处理1h,然后再用去离子水反复清洗复合膜,最后将膜晾干即可得正渗透复合膜。After defoaming the above CS/CS-GO solution, add the formula amount of dilute glutaraldehyde solution, stir evenly, scrape a thin layer of liquid film with a thickness of 5 μm on the sulfonated polyethersulfone ultrafiltration bottom membrane, and place it on the Place it horizontally at room temperature for 4 hours, and then dry it in an oven at 50°C. The dried composite membrane is soaked in a mixed solution of sodium hydroxide and ethanol to continue treatment for 1 hour, then the composite membrane is repeatedly washed with deionized water, and finally the membrane is dried to obtain a forward osmosis composite membrane.
原料配方及获得的正渗透膜渗透通量和截盐性能于表1所示。The raw material formula and the permeation flux and salt interception performance of the obtained forward osmosis membrane are shown in Table 1.
实施例5Example 5
将壳聚糖修饰的氧化石墨烯(CS-GO)加入到去离子水中,超声分散2小时,获得均匀的CS-GO分散液;将壳聚糖和亲水添加剂(甘油)按配方溶于稀醋酸中,60℃下连续搅拌6小时,抽滤,去除不溶性杂质。然后将CS-GO分散液加入到壳聚糖溶液中,继续在60℃下连续搅拌4h。Chitosan-modified graphene oxide (CS-GO) was added to deionized water, and ultrasonically dispersed for 2 hours to obtain a uniform CS-GO dispersion; chitosan and hydrophilic additive (glycerin) were dissolved in dilute In acetic acid, stir continuously at 60°C for 6 hours, and filter with suction to remove insoluble impurities. Then the CS-GO dispersion was added to the chitosan solution and continued to stir continuously at 60 °C for 4 h.
将上述CS/CS-GO溶液脱泡后,加入配方量的稀戊二醛溶液,搅拌均匀后,在磺化聚醚砜超滤底膜上刮制5μm厚度的薄层液膜,将其在室温下水平放置2h,然后将其放入50℃的烘箱中烘干。烘干后的复合膜浸泡入氢氧化钠和乙醇混合溶液中继续处理1h,然后再用去离子水反复清洗复合膜,最后将膜晾干即可得正渗透复合膜。After defoaming the above CS/CS-GO solution, add the formula amount of dilute glutaraldehyde solution, stir evenly, scrape a thin layer of liquid film with a thickness of 5 μm on the sulfonated polyethersulfone ultrafiltration bottom membrane, and place it on the Place it horizontally at room temperature for 2 hours, and then dry it in an oven at 50°C. The dried composite membrane is soaked in a mixed solution of sodium hydroxide and ethanol to continue treatment for 1 hour, then the composite membrane is repeatedly washed with deionized water, and finally the membrane is dried to obtain a forward osmosis composite membrane.
原料配方及获得的正渗透膜渗透通量和截盐性能于表1所示。The raw material formula and the permeation flux and salt interception performance of the obtained forward osmosis membrane are shown in Table 1.
实施例6Example 6
将壳聚糖修饰的氧化石墨烯(CS-GO)加入到去离子水中,超声分散2小时,获得均匀的CS-GO分散液;将壳聚糖和亲水添加剂(吐温80)按配方溶于稀醋酸中,60℃下连续搅拌6小时,抽滤,去除不溶性杂质。然后将CS-GO分散液加入到壳聚糖溶液中,继续在60℃下连续搅拌4h。Chitosan-modified graphene oxide (CS-GO) was added to deionized water, and ultrasonically dispersed for 2 hours to obtain a uniform CS-GO dispersion; chitosan and hydrophilic additive (Tween 80) were dissolved according to the formula In dilute acetic acid, stir continuously at 60°C for 6 hours, and filter with suction to remove insoluble impurities. Then the CS-GO dispersion was added to the chitosan solution and continued to stir continuously at 60 °C for 4 h.
将上述CS/CS-GO溶液脱泡后,加入配方量的稀戊二醛溶液,搅拌均匀后,在聚偏氟乙烯超滤底膜上刮制10μm厚度的薄层液膜,将其在室温下水平放置2h,然后将其放入50℃的烘箱中烘干。烘干后的复合膜浸泡入氢氧化钠和乙醇混合溶液中继续处理1h,然后再用去离子水反复清洗复合膜,最后将膜晾干即可得正渗透复合膜。After defoaming the above CS/CS-GO solution, add the formula amount of dilute glutaraldehyde solution, stir evenly, scrape a thin layer of liquid film with a thickness of 10 μm on the polyvinylidene fluoride ultrafiltration bottom membrane, and place it at room temperature Place it horizontally for 2 hours, and then dry it in an oven at 50°C. The dried composite membrane is soaked in a mixed solution of sodium hydroxide and ethanol to continue treatment for 1 hour, then the composite membrane is repeatedly washed with deionized water, and finally the membrane is dried to obtain a forward osmosis composite membrane.
原料配方及获得的正渗透膜渗透通量和截盐性能于表1所示。The raw material formula and the permeation flux and salt interception performance of the obtained forward osmosis membrane are shown in Table 1.
表1实施例中正渗透膜制膜液成分以及膜性能Forward osmosis membrane membrane-making liquid composition and membrane performance in the embodiment of table 1
由表1的结果可知,本发明的正渗透膜水通量基本都能达到12L/m2·h以上,通过对制膜液配方的优选可达到20L/m2·h左右;反向盐通量在6g/m2·h以内,通过对制膜液配方的优选可在4g/m2·h左右。From the results in Table 1, it can be seen that the water flux of the forward osmosis membrane of the present invention can basically reach more than 12L/m 2 ·h, and can reach about 20L/m 2 ·h by optimizing the formula of the membrane-making liquid; The amount is within 6g/m 2 ·h, and can be around 4g/m 2 ·h by optimizing the formulation of the film-forming solution.
以上所述仅为本发明专利的具体实施案例,但本发明专利的技术特征并不局限于此,任何相关领域的技术人员在本发明专利的领域内,所作的变化或修饰皆涵盖在本发明专利的专利范围之中。The above is only a specific implementation case of the patent of the present invention, but the technical features of the patent of the present invention are not limited thereto, and any changes or modifications made by those skilled in the relevant field within the field of the patent of the present invention are covered by the present invention within the scope of the patent.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610024276.2A CN105617882B (en) | 2016-01-14 | 2016-01-14 | A kind of compound forward osmosis membrane of chitosan-modified stannic oxide/graphene nano and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610024276.2A CN105617882B (en) | 2016-01-14 | 2016-01-14 | A kind of compound forward osmosis membrane of chitosan-modified stannic oxide/graphene nano and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105617882A CN105617882A (en) | 2016-06-01 |
CN105617882B true CN105617882B (en) | 2018-10-26 |
Family
ID=56033459
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610024276.2A Active CN105617882B (en) | 2016-01-14 | 2016-01-14 | A kind of compound forward osmosis membrane of chitosan-modified stannic oxide/graphene nano and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105617882B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US12140355B2 (en) | 2021-11-29 | 2024-11-12 | Via Separations, Inc. | Heat exchanger integration with membrane system for evaporator pre-concentration |
US12357950B2 (en) | 2019-05-15 | 2025-07-15 | Via Separations, Inc. | Durable graphene oxide membranes |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105903359A (en) * | 2016-06-06 | 2016-08-31 | 西北大学 | Chitosan functionalized graphene oxide/polyvinylidene fluoride hybrid ultrafiltration membrane and preparation method thereof |
CN106268322A (en) * | 2016-09-14 | 2017-01-04 | 南京理工大学 | A kind of LBL self-assembly graphene oxide/n-trimethyl chitosan chloride Positively charged composite nanofiltration membrane and preparation method thereof |
CN106801040A (en) * | 2017-02-02 | 2017-06-06 | 复旦大学 | Hydrophilic graphene film material of antibody modification and preparation method thereof and the application in cell capture |
CN107540883B (en) * | 2017-09-08 | 2020-05-12 | 东华大学 | A kind of preparation method of carboxymethyl chitosan/graphene oxide/poly(N-isopropylacrylamide) nanocomposite hydrogel |
CN108295812B (en) * | 2018-03-14 | 2021-02-12 | 河南城建学院 | Graphene oxide composite membrane for selectively removing metal ions in water, and preparation method and application thereof |
CN108927116A (en) * | 2018-07-20 | 2018-12-04 | 大连医科大学 | A kind of preparation method for the stannic oxide/graphene nano material that phenyl boric acid functionalization is chitosan-modified |
CN112477333B (en) * | 2020-11-30 | 2023-11-10 | 浙江鑫海纺织有限公司 | Gel type wave-absorbing fabric and preparation method thereof |
CN112604507B (en) * | 2020-12-07 | 2022-08-05 | 四川华造宏材科技有限公司 | Preparation method of high-flux dye separation nanofiltration membrane |
CN112717719B (en) * | 2020-12-25 | 2023-03-17 | 自然资源部天津海水淡化与综合利用研究所 | Method for preparing graphene oxide composite nanofiltration membrane by spraying method |
CN113019142A (en) * | 2021-04-02 | 2021-06-25 | 河北工业大学 | Post-treatment modification method of polyamide composite nanofiltration membrane |
CN115475539B (en) * | 2022-08-22 | 2023-10-24 | 北方民族大学 | MnO2 nanowire modified PVDF membrane and its preparation method and application |
WO2024173691A1 (en) * | 2023-02-15 | 2024-08-22 | Via Separations, Inc. | Graphene oxide membranes comprising sulfonated support |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103464013A (en) * | 2013-07-25 | 2013-12-25 | 烟台绿水赋膜材料有限公司 | High-performance hybrid separation membrane and preparation method thereof |
CN103736400A (en) * | 2014-01-06 | 2014-04-23 | 中国海洋大学 | Preparation method of graphene oxide composite nano filter membrane |
CN104028111A (en) * | 2013-03-08 | 2014-09-10 | 北京师范大学 | Method for preparing sandwich graphene oxide separation membrane |
CN104474919A (en) * | 2014-12-15 | 2015-04-01 | 济南大学 | High-performance flat-type cellulose acetate/graphene blend forward osmosis membrane |
CN105032207A (en) * | 2015-08-05 | 2015-11-11 | 中国科学院宁波材料技术与工程研究所 | Preparation method of graphene oxide base forward-osmosis membrane |
CN105148741A (en) * | 2015-08-14 | 2015-12-16 | 浙江大学 | Preparation method of inorganic nano-hybrided and positively-charged polyelectrolyte complex pervaporation membrane |
-
2016
- 2016-01-14 CN CN201610024276.2A patent/CN105617882B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104028111A (en) * | 2013-03-08 | 2014-09-10 | 北京师范大学 | Method for preparing sandwich graphene oxide separation membrane |
CN103464013A (en) * | 2013-07-25 | 2013-12-25 | 烟台绿水赋膜材料有限公司 | High-performance hybrid separation membrane and preparation method thereof |
CN103736400A (en) * | 2014-01-06 | 2014-04-23 | 中国海洋大学 | Preparation method of graphene oxide composite nano filter membrane |
CN104474919A (en) * | 2014-12-15 | 2015-04-01 | 济南大学 | High-performance flat-type cellulose acetate/graphene blend forward osmosis membrane |
CN105032207A (en) * | 2015-08-05 | 2015-11-11 | 中国科学院宁波材料技术与工程研究所 | Preparation method of graphene oxide base forward-osmosis membrane |
CN105148741A (en) * | 2015-08-14 | 2015-12-16 | 浙江大学 | Preparation method of inorganic nano-hybrided and positively-charged polyelectrolyte complex pervaporation membrane |
Non-Patent Citations (3)
Title |
---|
Graphene oxide cross-linked chitosan nanocomposite membrane;Lu Shao et al.;《Applied Surface Science》;20130502;第280卷;第989-992页 * |
Green fabrication of chitosan films reinforced with parallel aligned graphene oxide;Yongzheng Pan et al.;《Carbohydrate Polymers》;20101030(第83期);第1909-1914页 * |
改性氧化石墨烯/聚醚砜杂化荷正电纳滤膜的制备及表征;余亮等;《高等学校化学学报》;20140531;第35卷(第5期);第1100-1101页 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US12357950B2 (en) | 2019-05-15 | 2025-07-15 | Via Separations, Inc. | Durable graphene oxide membranes |
US12140355B2 (en) | 2021-11-29 | 2024-11-12 | Via Separations, Inc. | Heat exchanger integration with membrane system for evaporator pre-concentration |
Also Published As
Publication number | Publication date |
---|---|
CN105617882A (en) | 2016-06-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105617882B (en) | A kind of compound forward osmosis membrane of chitosan-modified stannic oxide/graphene nano and preparation method thereof | |
CN107469651B (en) | A kind of preparation method and application of high-throughput cross-linked polyimide solvent-resistant nanofiltration membrane | |
CN103861468B (en) | Compound nanofiltration membrane for dye desalination and treatment of waste water during dye desalination, as well as preparation method of compound nanofiltration membrane | |
CN102580560B (en) | Method for preparing nano-material-doped polymer film | |
CN100544809C (en) | A method for hydrophilic modification of polyvinylidene fluoride membrane | |
CN104174299B (en) | High flux forward osmosis membrane based on ultra-thin supporting layer and preparation method thereof | |
CN103394293B (en) | A kind of preparation method of hydrophilia polyvinylidene fluoride hollow fiber membrane | |
CN108409981A (en) | A kind of preparation method of modified metal organic frame and composite nanometer filtering film | |
CN103087342B (en) | Graphene oxide/PVDF (polyvinylidene fluoride) blended cation exchange membrane and preparation method thereof | |
CN102961975B (en) | Preparation method of hydrophilic hollow vinylidene fluoride fiber film | |
CN102614788A (en) | Preparation method for polyether sulfone/graphene oxide composite ultrafiltration membrane | |
CN102755841A (en) | Preparation method and product of hydrophobic PVDF (Polyvinylidene Fluoride) microporous membrane with beta crystalline phase structure | |
CN104107638B (en) | Forward osmosis membrane and preparation method thereof | |
CN102626593B (en) | Formula of acid and alkali-resistant and anti-pollution ultrafiltration membrane and preparation method thereof | |
CN104147943A (en) | Preparation method and application of high-molecular forward osmosis membrane | |
CN101274220A (en) | Preparation method of polyaniline nanofiber blended composite film | |
CN104117291A (en) | TiO2/C hybrid aerogel modified polyvinylidene fluoride membrane and preparation method thereof | |
CN113797763B (en) | Cellulose gel layer modified loose nanofiltration membrane for high-flux dye separation and preparation method and application thereof | |
CN105597552A (en) | Forward osmosis membrane with high water flux and high salt rejection rate and method for preparing forward osmosis membrane with one-step method | |
CN105126647A (en) | Preparation method for efficient oil-water separation composite ultrafiltration membrane | |
CN102626595A (en) | Formula for industrial high-strength anti-pollution ultrafiltration flat plate membrane and preparation method thereof | |
CN112604507B (en) | Preparation method of high-flux dye separation nanofiltration membrane | |
CN105797596B (en) | A kind of preparation method of filter membrane for Water warfare | |
CN117181004A (en) | Hydrophilic anti-pollution MXene/PVDF composite membrane and preparation method and application thereof | |
CN103406031A (en) | Low-resistance high-flux soiling resistant type water treatment membrane and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20200605 Address after: 405400 Zhaojia group, Puli Industrial New District, Zhaojia street, Kaizhou District, Chongqing Patentee after: CHONGQING HAITONG ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: No. n817, floor 3, xingguangyingjing, No. 117, Shuiyin Road, Yuexiu District, Guangzhou City, Guangdong Province Patentee before: Zhiyueyun (Guangzhou) Digital Information Technology Co.,Ltd. Effective date of registration: 20200605 Address after: No. n817, floor 3, xingguangyingjing, No. 117, Shuiyin Road, Yuexiu District, Guangzhou City, Guangdong Province Patentee after: Zhiyueyun (Guangzhou) Digital Information Technology Co.,Ltd. Address before: Hangzhou City, Zhejiang province 310018 Xiasha Higher Education Park is 18 street. Patentee before: ZHEJIANG GONGSHANG University |