CN115445439A - Pervaporation membrane and preparation method and application thereof - Google Patents
Pervaporation membrane and preparation method and application thereof Download PDFInfo
- Publication number
- CN115445439A CN115445439A CN202110636406.9A CN202110636406A CN115445439A CN 115445439 A CN115445439 A CN 115445439A CN 202110636406 A CN202110636406 A CN 202110636406A CN 115445439 A CN115445439 A CN 115445439A
- Authority
- CN
- China
- Prior art keywords
- graphene oxide
- electric field
- pervaporation
- polymer matrix
- pervaporation membrane
- 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.)
- Pending
Links
- 238000005373 pervaporation Methods 0.000 title claims abstract description 82
- 239000012528 membrane Substances 0.000 title claims abstract description 65
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 102
- 229910021389 graphene Inorganic materials 0.000 claims abstract description 101
- 239000002135 nanosheet Substances 0.000 claims abstract description 96
- 230000005684 electric field Effects 0.000 claims abstract description 82
- 229920000642 polymer Polymers 0.000 claims abstract description 30
- 239000011159 matrix material Substances 0.000 claims abstract description 28
- 125000000524 functional group Chemical group 0.000 claims abstract description 8
- 239000002064 nanoplatelet Substances 0.000 claims abstract description 7
- 239000006185 dispersion Substances 0.000 claims description 55
- 239000007788 liquid Substances 0.000 claims description 37
- 238000005266 casting Methods 0.000 claims description 33
- 239000000243 solution Substances 0.000 claims description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 27
- 230000009471 action Effects 0.000 claims description 16
- 229920002284 Cellulose triacetate Polymers 0.000 claims description 14
- 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 claims description 14
- 238000003756 stirring Methods 0.000 claims description 10
- -1 polyhydroxymethylene Polymers 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 6
- 239000004695 Polyether sulfone Substances 0.000 claims description 5
- 229920006393 polyether sulfone Polymers 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 229920001661 Chitosan Polymers 0.000 claims description 4
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 claims description 4
- 239000004952 Polyamide Substances 0.000 claims description 4
- 229920002614 Polyether block amide Polymers 0.000 claims description 4
- 239000004698 Polyethylene Substances 0.000 claims description 4
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 4
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 4
- 125000003700 epoxy group Chemical group 0.000 claims description 4
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 4
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 4
- 229920002647 polyamide Polymers 0.000 claims description 4
- 229920000573 polyethylene Polymers 0.000 claims description 4
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 4
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 claims description 3
- 238000010612 desalination reaction Methods 0.000 claims description 3
- 239000000661 sodium alginate Substances 0.000 claims description 3
- 235000010413 sodium alginate Nutrition 0.000 claims description 3
- 229940005550 sodium alginate Drugs 0.000 claims description 3
- 239000012267 brine Substances 0.000 claims description 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims 2
- 230000004907 flux Effects 0.000 abstract description 22
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 48
- 239000011780 sodium chloride Substances 0.000 description 20
- 230000000052 comparative effect Effects 0.000 description 18
- 238000012360 testing method Methods 0.000 description 18
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 17
- 239000012466 permeate Substances 0.000 description 15
- 238000012546 transfer Methods 0.000 description 15
- 238000010586 diagram Methods 0.000 description 14
- 239000007864 aqueous solution Substances 0.000 description 12
- 239000002994 raw material Substances 0.000 description 12
- 239000000047 product Substances 0.000 description 9
- 150000003839 salts Chemical class 0.000 description 9
- 239000011521 glass Substances 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 6
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 6
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical group CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 6
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 6
- PBAYDYUZOSNJGU-UHFFFAOYSA-N chelidonic acid Natural products OC(=O)C1=CC(=O)C=C(C(O)=O)O1 PBAYDYUZOSNJGU-UHFFFAOYSA-N 0.000 description 6
- 239000003153 chemical reaction reagent Substances 0.000 description 6
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- IVSZLXZYQVIEFR-UHFFFAOYSA-N m-xylene Chemical group CC1=CC=CC(C)=C1 IVSZLXZYQVIEFR-UHFFFAOYSA-N 0.000 description 6
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 229960000583 acetic acid Drugs 0.000 description 3
- 239000012362 glacial acetic acid Substances 0.000 description 3
- 229940078552 o-xylene Drugs 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- JHUUPUMBZGWODW-UHFFFAOYSA-N 3,6-dihydro-1,2-dioxine Chemical compound C1OOCC=C1 JHUUPUMBZGWODW-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 235000010443 alginic acid Nutrition 0.000 description 1
- 239000000783 alginic acid Substances 0.000 description 1
- 229920000615 alginic acid Polymers 0.000 description 1
- 229960001126 alginic acid Drugs 0.000 description 1
- 150000004781 alginic acids Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000001132 ultrasonic dispersion Methods 0.000 description 1
- 238000002525 ultrasonication Methods 0.000 description 1
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
- B01D61/36—Pervaporation; Membrane distillation; Liquid permeation
- B01D61/362—Pervaporation
-
- 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
- B01D2325/00—Details relating to properties of membranes
- B01D2325/36—Hydrophilic membranes
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
技术领域technical field
本发明属于恒沸物及近沸物分离、微量水脱除、盐水淡化等分离领域,具体地,涉及一种渗透汽化膜及其制备方法、应用。The invention belongs to the field of separation of azeotrope and near-boiler, trace water removal, brine desalination, etc., and in particular relates to a pervaporation membrane and its preparation method and application.
背景技术Background technique
渗透汽化是一种以液体混合物中某组分在膜两侧的化学势梯度为传质驱动力,使组分在膜表面吸附溶解、在膜内扩散、最后在膜下游侧汽化,利用不同组分在溶解和扩散过程中的差异实现分离的一种新兴分离技术。渗透汽化具有能耗低、污染小、设备简单、操作方便等优点,可以应用到恒沸物及近沸物分离、微量水脱除、含盐水淡化等领域中,已成为化工、环保等领域的研究热点之一。Pervaporation is a mass transfer driving force based on the chemical potential gradient of a certain component in the liquid mixture on both sides of the membrane, so that the component absorbs and dissolves on the surface of the membrane, diffuses in the membrane, and finally vaporizes on the downstream side of the membrane. It is an emerging separation technology that realizes the separation by the difference in the dissolution and diffusion process. Pervaporation has the advantages of low energy consumption, low pollution, simple equipment, and convenient operation. It can be applied to the fields of azeotrope and near-boiler separation, trace water removal, and salt water desalination. One of the research hotspots.
目前,渗透汽化膜存在通量不足的问题,限制了渗透汽化技术的大规模工业化应用。At present, the pervaporation membrane has insufficient flux, which limits the large-scale industrial application of pervaporation technology.
发明内容Contents of the invention
鉴于此,本发明的目的是提供一种渗透汽化膜及其制备方法、应用,本发明的渗透汽化膜具有提高的渗透通量。In view of this, the object of the present invention is to provide a pervaporation membrane and its preparation method and application. The pervaporation membrane of the present invention has improved permeation flux.
根据本发明的一个方面,所述渗透汽化膜,包括以下组分:聚合物基体;和分散于所述聚合物基体中的氧化石墨烯纳米片,所述氧化石墨烯纳米片包含亲水性官能团;其中,所述氧化石墨烯纳米片沿膜的厚度方向取向。According to one aspect of the present invention, the pervaporation membrane includes the following components: a polymer matrix; and graphene oxide nanosheets dispersed in the polymer matrix, and the graphene oxide nanosheets contain hydrophilic functional groups ; Wherein, the graphene oxide nanosheets are oriented along the thickness direction of the film.
本发明中,通过将氧化石墨烯(Graphene Oxide,下文简写GO)纳米片掺杂入聚合物基体,并施加外部交流电场以对聚合物基体中的氧化石墨烯纳米片进行排布,使其在膜中发生取向,所制备的有机-无机杂化膜(即渗透汽化膜)具有比未施加电场条件下制备的膜具有提高的渗透通量。In the present invention, by doping graphene oxide (Graphene Oxide, hereinafter abbreviated as GO) nanosheets into the polymer matrix, and applying an external AC electric field to arrange the graphene oxide nanosheets in the polymer matrix, so that Orientation occurs in the membrane, and the prepared organic-inorganic hybrid membrane (ie, pervaporation membrane) has enhanced permeation flux than the membrane prepared without an applied electric field.
根据本发明一些实施方式,所述聚合物基体包括:聚醚酰胺、聚乙烯醇、壳聚糖、三醋酸纤维素、聚羟基甲撑、磺化聚乙烯、聚酰胺、聚醚砜、海藻酸钠、聚丙烯腈和聚甲基丙烯酸二甲氨基乙酯中的一种或多种;优选地,所述聚合物基体包括三醋酸纤维素。According to some embodiments of the present invention, the polymer matrix includes: polyetheramide, polyvinyl alcohol, chitosan, cellulose triacetate, polyhydroxymethylene, sulfonated polyethylene, polyamide, polyethersulfone, alginic acid One or more of sodium, polyacrylonitrile and polydimethylaminoethyl methacrylate; preferably, the polymer matrix includes cellulose triacetate.
根据本发明一些实施方式,所述氧化石墨烯纳米片的片径为0.05~5μm,优选为0.1~3μm,更优选为0.2~1.5μm。本发明中,术语“片径”是指氧化石墨烯纳米片的同一面上距离最远的两点之间的直线距离。According to some embodiments of the present invention, the diameter of the graphene oxide nanosheets is 0.05-5 μm, preferably 0.1-3 μm, more preferably 0.2-1.5 μm. In the present invention, the term "sheet diameter" refers to the straight-line distance between the two farthest points on the same surface of the graphene oxide nanosheet.
根据本发明一些实施方式,所述氧化石墨烯纳米片的亲水性官能团包含羧基、羟基和环氧基中的一种或多种。例如,采用购自Sigma-Aldrich的、商品号为796034的氧化石墨烯纳米片。According to some embodiments of the present invention, the hydrophilic functional groups of the graphene oxide nanosheets include one or more of carboxyl groups, hydroxyl groups and epoxy groups. For example, graphene oxide nanosheets available from Sigma-Aldrich, product number 796034, are used.
根据本发明一些实施方式,所述氧化石墨烯纳米片相对于所述渗透汽化膜的质量分数为0.05~25wt%,优选为0.5~20wt%,更优选为2.5~15wt%。According to some embodiments of the present invention, the mass fraction of the graphene oxide nanosheets relative to the pervaporation membrane is 0.05-25 wt%, preferably 0.5-20 wt%, more preferably 2.5-15 wt%.
根据本发明第二方面,还提供如上所述的渗透汽化膜的制备方法,包括以下步骤:According to the second aspect of the present invention, there is also provided a method for preparing a pervaporation membrane as described above, comprising the following steps:
步骤a)将氧化石墨烯纳米片分散于溶剂中,形成氧化石墨烯纳米片分散液,其中,所述氧化石墨烯纳米片分散液中氧化石墨烯纳米片的含量为0.001~0.7wt%,优选为0.01~0.5wt%,更优选为0.05~0.3wt%;Step a) dispersing graphene oxide nanosheets in a solvent to form a graphene oxide nanosheet dispersion, wherein the content of graphene oxide nanosheets in the graphene oxide nanosheet dispersion is 0.001 to 0.7 wt%, preferably It is 0.01~0.5wt%, more preferably 0.05~0.3wt%;
步骤b)向步骤a)中所述氧化石墨烯纳米片分散液中加入聚合物基体,搅拌溶解形成铸膜液;Step b) adding a polymer matrix to the graphene oxide nanosheet dispersion described in step a), stirring and dissolving to form a casting solution;
步骤c)将步骤b)中所述铸膜液浇铸成膜,置于电场作用中,干燥,获得电场取向的渗透汽化膜。Step c) Casting the film-casting liquid described in step b) into a film, placing it under the action of an electric field, and drying to obtain an electric-field-oriented pervaporation film.
根据本发明一些实施方式,所述步骤a)中通过超声作用来制备氧化石墨烯纳米片分散液,超声分散时间为30~60分钟;和/或其中,所述氧化石墨烯纳米片片径为0.05~5μm,优选为0.1~3μm,更优选为0.2~1.5μm;和/或所述氧化石墨烯纳米片的亲水性官能团包含羧基、羟基和环氧基中的一种或多种;和/或所述溶剂包括1,4-二氧六环、1,2-二氯乙烷、异丙醇、邻二甲苯、环己酮、间二甲苯、无水乙醇、石油醚、、四氢呋喃、冰乙酸中的一种或多种,优选为1,4-二氧六环。According to some embodiments of the present invention, the graphene oxide nanosheet dispersion is prepared by ultrasonication in the step a), and the ultrasonic dispersion time is 30 to 60 minutes; and/or wherein, the diameter of the graphene oxide nanosheet is 0.05-5 μm, preferably 0.1-3 μm, more preferably 0.2-1.5 μm; and/or the hydrophilic functional groups of the graphene oxide nanosheets include one or more of carboxyl, hydroxyl and epoxy groups; and /or the solvent includes 1,4-dioxane, 1,2-dichloroethane, isopropanol, o-xylene, cyclohexanone, m-xylene, absolute ethanol, petroleum ether, tetrahydrofuran, One or more of glacial acetic acid, preferably 1,4-dioxane.
根据本发明一些实施方式,所述步骤b)中,配制成聚合物基体浓度为0.1~15wt%,优选为0.5~10wt%,更优选为1~5wt%的铸膜液;和/或搅拌温度为40~80℃,时间为8~15小时;其中,所述聚合物基体包括聚醚酰胺、聚乙烯醇、壳聚糖、三醋酸纤维素、聚羟基甲撑、磺化聚乙烯、聚酰胺、聚醚砜、海藻酸钠、聚丙烯腈和聚甲基丙烯酸二甲氨基乙酯中的一种或多种,优选为三醋酸纤维素。According to some embodiments of the present invention, in the step b), the casting solution is prepared with a polymer matrix concentration of 0.1-15wt%, preferably 0.5-10wt%, more preferably 1-5wt%; and/or stirring temperature 40-80°C, and the time is 8-15 hours; wherein, the polymer matrix includes polyetheramide, polyvinyl alcohol, chitosan, cellulose triacetate, polyhydroxymethylene, sulfonated polyethylene, polyamide , polyethersulfone, sodium alginate, polyacrylonitrile and polydimethylaminoethyl methacrylate or one or more, preferably cellulose triacetate.
根据本发明一些实施方式,所述步骤c)中电场强度为400~5000V/cm,优选为500~3000V/cm,更优选为600~1000V/cm;和/或频率为400~1000Hz,,所述电场作用时间为10~120分钟;和/或所述干燥时间为2~24小时。According to some embodiments of the present invention, the electric field strength in step c) is 400-5000V/cm, preferably 500-3000V/cm, more preferably 600-1000V/cm; and/or the frequency is 400-1000Hz, so The electric field action time is 10-120 minutes; and/or the drying time is 2-24 hours.
根据本发明第三方面,提供如上所述的渗透汽化膜和如上所述的渗透汽化膜的制备方法所制备的渗透汽化膜,在恒沸物及近沸物分离、微量水脱除、盐水淡化等领域的应用。According to the third aspect of the present invention, the above pervaporation membrane and the pervaporation membrane prepared by the above pervaporation membrane preparation method are provided. applications in other fields.
本发明的有益效果在于:The beneficial effects of the present invention are:
本发明氧化石墨烯纳米片上存在亲水性官能团,可将其掺杂在聚合物中制备有机-无机杂化膜,氧化石墨烯纳米片之间存在的间隙以及有机相与无机相之间形成的界面都可以成为渗透物在膜内的传质通道。There are hydrophilic functional groups on the graphene oxide nanosheets of the present invention, which can be doped in polymers to prepare organic-inorganic hybrid films, gaps between graphene oxide nanosheets and gaps formed between organic and inorganic phases. The interface can become the mass transfer channel of the permeate in the membrane.
进一步地,本发明通过施加外部交流电场,对聚合物基体中的氧化石墨烯纳米片进行排布,使得GO纳米片在膜中发生取向,缩短渗透物分子在膜中的传质途径,提高渗透汽化膜的渗透通量。Furthermore, the present invention arranges the graphene oxide nanosheets in the polymer matrix by applying an external AC electric field, so that the GO nanosheets are oriented in the membrane, shortening the mass transfer pathway of the permeate molecules in the membrane, and improving the permeability. The permeate flux of vaporized membranes.
附图说明Description of drawings
图1A为根据本发明实施例1制得的氧化石墨烯纳米片在1,4-二氧六环中的分散液在电场作用下0秒、60秒、90秒、120秒以及150秒时显微镜观察图。Fig. 1A is a micrograph of the dispersion of graphene oxide nanosheets in 1,4-dioxane prepared according to Example 1 of the present invention under the action of an electric field at 0 seconds, 60 seconds, 90 seconds, 120 seconds and 150 seconds Observe the diagram.
图1B为根据本发明实施例2制得的氧化石墨烯纳米片在1,2-二氯乙烷中的分散液在电场作用下0秒以及150秒时显微镜观察图。FIG. 1B is a microscope observation diagram of the dispersion of graphene oxide nanosheets in 1,2-dichloroethane prepared according to Example 2 of the present invention under the action of an electric field for 0 seconds and 150 seconds.
图1C为根据本发明实施例2制得的氧化石墨烯纳米片在异丙醇中的分散液在电场作用下0秒以及150秒时显微镜观察图。1C is a microscopic observation diagram of the dispersion of graphene oxide nanosheets in isopropanol prepared according to Example 2 of the present invention under the action of an electric field for 0 seconds and 150 seconds.
图1D为根据本发明实施例2制得的氧化石墨烯纳米片在邻二甲苯中的分散液在电场作用下0秒以及150秒时显微镜观察图。FIG. 1D is a microscope observation diagram of the dispersion of graphene oxide nanosheets in o-xylene prepared according to Example 2 of the present invention under the action of an electric field for 0 seconds and 150 seconds.
图1E为根据本发明实施例2制得的氧化石墨烯纳米片在环己酮中的分散液在电场作用下0秒以及150秒时显微镜观察图。FIG. 1E is a microscope observation diagram of the dispersion of graphene oxide nanosheets in cyclohexanone prepared according to Example 2 of the present invention under the action of an electric field for 0 seconds and 150 seconds.
图1F为根据本发明实施例2制得的氧化石墨烯纳米片在间二甲苯中的分散液在电场作用下0秒以及150秒时显微镜观察图。FIG. 1F is a microscope observation diagram of the dispersion of graphene oxide nanosheets in m-xylene prepared according to Example 2 of the present invention under the action of an electric field for 0 seconds and 150 seconds.
图1G为根据本发明实施例2制得的氧化石墨烯纳米片在无水乙醇中的分散液在电场作用下0秒以及150秒时显微镜观察图。FIG. 1G is a microscope observation diagram of the dispersion of graphene oxide nanosheets in absolute ethanol prepared according to Example 2 of the present invention under the action of an electric field for 0 seconds and 150 seconds.
图1H为根据本发明实施例2制得的氧化石墨烯纳米片在石油醚中的分散液在电场作用下0秒以及150秒时显微镜观察图。FIG. 1H is a microscope observation diagram of the dispersion of graphene oxide nanosheets in petroleum ether prepared according to Example 2 of the present invention at 0 seconds and 150 seconds under the action of an electric field.
图1I为根据本发明实施例2制得的氧化石墨烯纳米片在四氢呋喃中的分散液在电场作用下0秒以及150秒时显微镜观察图。FIG. 1I is a microscope observation diagram of the dispersion of graphene oxide nanosheets in tetrahydrofuran prepared according to Example 2 of the present invention at 0 seconds and 150 seconds under the action of an electric field.
图1J为根据本发明实施例2制得的氧化石墨烯纳米片在冰乙酸中的分散液在电场作用下0秒以及150秒时显微镜观察图。FIG. 1J is a microscope observation diagram of the dispersion of graphene oxide nanosheets in glacial acetic acid prepared according to Example 2 of the present invention under the action of an electric field for 0 seconds and 150 seconds.
图1K为根据本发明示例性实施例中观察渗透汽化膜的显微镜装置示意图。FIG. 1K is a schematic diagram of a microscope device for observing a pervaporation membrane according to an exemplary embodiment of the present invention.
图2为根据本发明示例性实施例的渗透汽化膜的制备方法流程图。Fig. 2 is a flowchart of a method for preparing a pervaporation membrane according to an exemplary embodiment of the present invention.
图3为根据本发明示例性实施例的渗透汽化膜在实施电场取向作用的示意图。Fig. 3 is a schematic diagram of a pervaporation membrane performing electric field orientation according to an exemplary embodiment of the present invention.
图4为根据本发明示例性实施例的渗透汽化膜性能与电场取向作用电场强度的关系变化图。Fig. 4 is a graph showing the relationship between the performance of the pervaporation membrane and the electric field strength of the electric field orientation according to an exemplary embodiment of the present invention.
附图标记说明Explanation of reference signs
101 显微镜101 Microscope
103 电极板103 electrode plate
105 高压脉冲电源105 High voltage pulse power supply
107 玻璃槽107 glass tank
109 氧化石墨烯纳米片分散液109 Graphene oxide nanosheet dispersion
301 电源301 power supply
303 无尘箱303 Dust-free box
305 电极板305 electrode plate
307 垫板307 backing plate
309 铸膜液309 Casting solution
311 玻璃板311 glass plate
具体实施方式detailed description
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
氧化石墨烯纳米片极化率各向异性,受外电场作用时,外电场在其平面上会产生一个诱导偶极矩。外电场与偶极矩的相互作用会产生一个转矩,该转矩作用于氧化石墨烯纳米片,使偶极子转向并与外场方向对齐,从而使得氧化石墨烯纳米片平行于电场方向。因此,在采用含有GO的聚合物溶液制备膜的过程中,在膜两侧施加电场方向与膜片垂直的外电场,可以实现聚合物中氧化石墨烯纳米片沿膜的厚度方向取向。The polarizability of graphene oxide nanosheets is anisotropic, and when subjected to an external electric field, the external electric field will generate an induced dipole moment on its plane. The interaction of the external electric field with the dipole moment produces a torque that acts on the GO nanosheets, turning the dipoles and aligning them with the direction of the external field so that the GO nanosheets are parallel to the direction of the electric field. Therefore, in the process of preparing the membrane using a polymer solution containing GO, an external electric field with the direction of the electric field perpendicular to the membrane sheet is applied on both sides of the membrane, and the graphene oxide nanosheets in the polymer can be oriented along the thickness direction of the membrane.
[1]Besharat F,Manteghian M,Gallone G,et al.Electric field inducedalignment of graphene oxide nanoplatelets in polyethersulfone matrix[J].Nanotechnology,2020,31(15):155701(16pp).[1] Besharat F, Manteghian M, Gallone G, et al. Electric field induced alignment of graphene oxide nanoplatelets in polyethersulfone matrix [J]. Nanotechnology, 2020, 31(15): 155701(16pp).
需要说明的是,本发明各实施例中所用试剂,均为可以通过市购获得的常规产品,试剂均为分析纯或化学纯。It should be noted that the reagents used in each embodiment of the present invention are commercially available conventional products, and the reagents are all analytical or chemical pure.
实施例1Example 1
实施例1所用氧化石墨烯纳米片分散液的制备过程包括将氧化石墨烯纳米片(商品号为796034;生产厂家Sigma-Aldrich;分子量4239.48g/mol,片径均值为0.8μm)加入到1,4-二氧六环(Dioxane,生产厂家天津市科密欧化学试剂有限公司,分析纯)中,制成分散液中氧化石墨烯纳米片的含量为0.02wt%的氧化石墨烯纳米片分散液,将氧化石墨烯纳米片分散液超声分散1h。The preparation process of the graphene oxide nanosheet dispersion used in Example 1 includes adding graphene oxide nanosheets (product number is 796034; manufacturer Sigma-Aldrich; molecular weight 4239.48g/mol, and the average value of sheet diameter is 0.8 μm) to 1, In 4-dioxane (Dioxane, manufacturer Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure), the content of graphene oxide nanosheets in the dispersion is made into a graphene oxide nanosheet dispersion of 0.02wt%. , ultrasonically disperse the graphene oxide nanosheet dispersion for 1 h.
图1A为根据本发明实施例1制得的氧化石墨烯纳米片的1,4-二氧六环分散液在电场作用下0秒、60秒、90秒、120秒以及150秒时显微镜观察图。Figure 1A is a microscope observation diagram of the 1,4-dioxane dispersion of graphene oxide nanosheets prepared according to Example 1 of the present invention under the action of an electric field at 0 seconds, 60 seconds, 90 seconds, 120 seconds and 150 seconds .
在本实施例中,图1A观察环境为氧化石墨烯纳米片分散液浓度为0.02wt%,电场强度为1000V/cm,频率为1000Hz,所用观察装置如图1K显微镜装置示意图所示。In this embodiment, the observation environment in Figure 1A is that the concentration of the graphene oxide nanosheet dispersion is 0.02wt%, the electric field strength is 1000V/cm, and the frequency is 1000Hz, and the observation device used is shown in Figure 1K.
在本实施例中,在电场的作条件下,随电场作用时间延长,氧化石墨烯纳米片在溶剂中取向更加明显。In this embodiment, under the condition of the electric field, the orientation of the graphene oxide nanosheets in the solvent is more obvious as the time of the electric field is prolonged.
实施例2Example 2
实施例2所用氧化石墨烯纳米片分散液的制备过程包括将氧化石墨烯纳米片(商品号为796034;生产厂家Sigma-Aldrich;分子量4239.48g/mol,片径均值为0.8μm)分别加入到1,2-二氯乙烷(生产厂家天津市科密欧化学试剂有限公司,分析纯)、异丙醇(生产厂家天津市风船化学试剂科技有限公司,分析纯)、邻二甲苯(生产厂家天津市科密欧化学试剂有限公司,分析纯)、间二甲苯(生产厂家天津市科密欧化学试剂有限公司,分析纯)、环己酮(生产厂家天津市科密欧化学试剂有限公司,分析纯)、无水乙醇(生产厂家天津市科密欧化学试剂有限公司,分析纯)、石油醚(生产厂家天津市风船化学试剂科技有限公司,分析纯)、四氢呋喃(生产厂家天津市风船化学试剂科技有限公司,分析纯)、冰乙酸(生产厂家天津市风船化学试剂科技有限公司,分析纯)中,制成分散液中氧化石墨烯纳米片的含量为0.02wt%的氧化石墨烯纳米片分散液,将氧化石墨烯纳米片分散液超声分散1h。The preparation process of the graphene oxide nanosheet dispersion used in Example 2 includes adding graphene oxide nanosheets (the product number is 796034; manufacturer Sigma-Aldrich; molecular weight 4239.48g/mol, average sheet diameter is 0.8 μm) to 1 , 2-dichloroethane (manufacturer Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure), isopropanol (manufacturer Tianjin Fengchuan Chemical Reagent Technology Co., Ltd., analytically pure), o-xylene (manufacturer Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure), m-xylene (produced by Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure), cyclohexanone (produced by Tianjin Kemiou Chemical Reagent Co., Ltd., Analytical pure), absolute ethanol (produced by Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure), petroleum ether (produced by Tianjin Fengchuan Chemical Reagent Technology Co., Ltd., analytically pure), tetrahydrofuran (produced by Tianjin Fengchuan Chuan Chemical Reagent Technology Co., Ltd., analytically pure), glacial acetic acid (manufacturer Tianjin Fengchuan Chemical Reagent Technology Co., Ltd., analytically pure), make the graphite oxide whose content of graphene oxide nanosheets in the dispersion is 0.02wt%. Graphene oxide nanosheet dispersion, ultrasonically disperse the graphene oxide nanosheet dispersion for 1 h.
图1B~图1J为根据本发明实施例2制得的氧化石墨烯纳米片分散液在电场作用下0秒以及150秒时显微镜观察图。1B to 1J are microscopic observations of the graphene oxide nanosheet dispersion prepared according to Example 2 of the present invention under the action of an electric field for 0 seconds and 150 seconds.
在本实施例中,图1B~图1J观察环境为氧化石墨烯纳米片分散液浓度为0.02wt%,电场强度为1000V/cm,频率为1000Hz,所用观察装置如图1K显微镜装置示意图所示。In this embodiment, the observation environment in Figures 1B to 1J is that the concentration of the graphene oxide nanosheet dispersion is 0.02wt%, the electric field strength is 1000V/cm, and the frequency is 1000Hz. The observation device used is shown in the schematic diagram of the microscope device in Figure 1K.
在本实施例中,在电场的作条件下,随电场作用时间延长,氧化石墨烯纳米片在溶剂中取向更加明显。In this embodiment, under the condition of the electric field, the orientation of the graphene oxide nanosheets in the solvent is more obvious as the time of the electric field is prolonged.
实施例3Example 3
图2为根据本发明示例性实施例的渗透汽化膜的制备方法流程图。Fig. 2 is a flowchart of a method for preparing a pervaporation membrane according to an exemplary embodiment of the present invention.
参见图2,在本实施例步骤S201中,将0.05g的氧化石墨烯纳米片(商品号为796034;生产厂家Sigma-Aldrich;分子量4239.48g/mol,片径均值为0.8μm)与97.95g的1,4-二氧六环(Dioxane,生产厂家天津市科密欧化学试剂有限公司,分析纯)共混,制成分散液中氧化石墨烯纳米片的含量为0.05wt%的氧化石墨烯纳米片分散液,将氧化石墨烯纳米片分散液超声分散1h。随后转入S203中。Referring to Fig. 2, in step S201 of the present embodiment, 0.05g of graphene oxide nanosheets (product number is 796034; manufacturer Sigma-Aldrich; molecular weight 4239.48g/mol, average sheet diameter is 0.8μm) and 97.95g of 1,4-dioxane (Dioxane, produced by Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure) is blended to make a graphene oxide nanosheet whose content of graphene oxide nanosheets in the dispersion is 0.05wt%. Sheet dispersion liquid, the graphene oxide nanosheet dispersion liquid was ultrasonically dispersed for 1 h. Then transfer to S203.
在步骤S203中,将氧化石墨烯纳米片分散液中加入聚合物基体为2g三醋酸纤维素(分析纯;生产厂家ACROS;分子量966.845g/mol),搅拌溶解形成铸膜液,在80℃的水浴中搅拌溶解8小时,得到GO/CTA=0.025的铸膜液。随后转入S205中。In step S203, 2 g of cellulose triacetate (analytical pure; manufacturer ACROS; molecular weight 966.845 g/mol) is added to the graphene oxide nanosheet dispersion liquid as a polymer matrix, stirred and dissolved to form a casting solution, and the Stir and dissolve in a water bath for 8 hours to obtain a casting solution with GO/CTA=0.025. Then transfer to S205.
在步骤S205中,将铸膜液在玻璃板上刮制成膜,放入高压交流电场中,电场强度为1000V/cm,频率为1000Hz,电场作用装置如图3所示。施加电场50分钟后停止,自然干燥24小时,以蒸发溶剂形成固化的膜。获得本实施例的渗透汽化膜。In step S205, the film-casting solution was scraped on a glass plate to form a film, and placed in a high-voltage AC electric field with an electric field strength of 1000 V/cm and a frequency of 1000 Hz. The electric field application device is shown in FIG. 3 . After 50 minutes of application of the electric field, stop, and let it dry naturally for 24 hours to evaporate the solvent to form a cured film. The pervaporation membrane of this example was obtained.
本实施例所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in this example include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
本实施例渗透汽化实验结果为:水通量为8.10kg/(m2·h),NaCl的盐截留率为99.9%。The results of the pervaporation experiment in this embodiment are: the water flux is 8.10 kg/(m 2 ·h), and the salt rejection rate of NaCl is 99.9%.
实施例4Example 4
同理于实施例3,参见图2,在本实施例步骤S201中,将0.1g的氧化石墨烯纳米片(商品号为796034;生产厂家Sigma-Aldrich;分子量4239.48g/mol,片径均值为0.8μm)与97.9g的1,4-二氧六环(Dioxane,生产厂家天津市科密欧化学试剂有限公司,分析纯)共混,制成分散液中氧化石墨烯纳米片的含量为0.1wt%的氧化石墨烯纳米片分散液,将氧化石墨烯纳米片分散液超声分散1h。随后转入S203中。In the same way as in Example 3, referring to Fig. 2, in step S201 of the present embodiment, 0.1g of graphene oxide nanosheets (product number is 796034; manufacturer Sigma-Aldrich; molecular weight 4239.48g/mol, average sheet diameter is 0.8 μm) and 97.9g of 1,4-dioxane (Dioxane, manufacturer Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure) blended to make the content of graphene oxide nanosheets in the dispersion liquid is 0.1 wt% graphene oxide nanosheet dispersion liquid, and ultrasonically disperse the graphene oxide nanosheet dispersion liquid for 1 h. Then transfer to S203.
在步骤S203中,将氧化石墨烯纳米片分散液中加入聚合物基体为2g三醋酸纤维素(分析纯;生产厂家ACROS;分子量966.845g/mol),搅拌溶解形成铸膜液,在80℃的水浴中搅拌溶解8小时,得到GO/CTA=0.05的铸膜液。随后转入S205中。In step S203, 2 g of cellulose triacetate (analytical pure; manufacturer ACROS; molecular weight 966.845 g/mol) is added to the graphene oxide nanosheet dispersion liquid as a polymer matrix, stirred and dissolved to form a casting solution, and the Stir and dissolve in a water bath for 8 hours to obtain a casting solution with GO/CTA=0.05. Then transfer to S205.
在步骤S205中,将铸膜液在玻璃板上刮制成膜,放入高压交流电场中,电场强度为600-1000V/cm(每间隔100V/cm制备一个试样,故本实施例中共5个试样),频率为1000Hz,电场作用装置如图3所示。施加电场50分钟后停止,干燥24小时。获得本实施例的渗透汽化膜。In step S205, the film-casting solution is scraped on a glass plate to form a film, and placed in a high-voltage AC electric field with an electric field strength of 600-1000V/cm (a sample is prepared at an interval of 100V/cm, so there are 5 samples in total in this embodiment) samples), the frequency is 1000 Hz, and the electric field device is shown in Figure 3. The electric field was stopped after 50 minutes of application and dried for 24 hours. The pervaporation membrane of this example was obtained.
本实施例所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in this example include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
本实施例渗透汽化实验结果为:The results of the pervaporation experiment in this embodiment are:
电场强度为600V/cm试样:水通量为7.63kg/(m2·h),NaCl的盐截留率为99.9%;The electric field strength is 600V/cm sample: the water flux is 7.63kg/(m 2 ·h), and the salt rejection rate of NaCl is 99.9%;
电场强度为700V/cm试样:水通量为7.76kg/(m2·h),NaCl的盐截留率为99.9%;The electric field strength is 700V/cm sample: the water flux is 7.76kg/(m 2 ·h), and the salt rejection rate of NaCl is 99.9%;
电场强度为800V/cm试样:水通量为7.93kg/(m2·h),NaCl的盐截留率为99.9%;The electric field strength is 800V/cm sample: the water flux is 7.93kg/(m 2 ·h), and the salt rejection rate of NaCl is 99.9%;
电场强度为900V/cm试样:水通量为8.12kg/(m2·h),NaCl的盐截留率为99.9%;The electric field strength is 900V/cm sample: the water flux is 8.12kg/(m 2 h), and the salt rejection rate of NaCl is 99.9%;
电场强度为1000V/cm试样:水通量为8.59kg/(m2·h),NaCl的盐截留率为99.9%。The electric field intensity is 1000V/cm sample: the water flux is 8.59kg/(m 2 ·h), and the salt rejection rate of NaCl is 99.9%.
本实施例证明,电场强度越高,GO取向程度越高,水通量提升的更多,如图4所示。This example proves that the higher the electric field intensity is, the higher the orientation degree of GO is, and the water flux is improved more, as shown in Fig. 4 .
实施例5Example 5
同理于上述实施例3,参见图2,在本实施例步骤S201中,将0.15g的氧化石墨烯纳米片(商品号为796034;生产厂家Sigma-Aldrich;分子量4239.48g/mol,片径均值为0.8μm)与97.85g的1,4-二氧六环(Dioxane,生产厂家天津市科密欧化学试剂有限公司,分析纯)共混,制成分散液中氧化石墨烯纳米片的含量为0.15wt%的氧化石墨烯纳米片分散液,将氧化石墨烯纳米片分散液超声分散1h。随后转入S203中。In the same way as above-mentioned embodiment 3, referring to Fig. 2, in step S201 of the present embodiment, the graphene oxide nanosheet of 0.15g (commercial number is 796034; manufacturer Sigma-Aldrich; molecular weight 4239.48g/mol, sheet diameter mean value 0.8 μm) and 97.85g of 1,4-dioxane (Dioxane, manufacturer Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure) blends to make the content of graphene oxide nanosheets in the dispersion liquid is 0.15wt% graphene oxide nanosheet dispersion, and ultrasonically disperse the graphene oxide nanosheet dispersion for 1 hour. Then transfer to S203.
在步骤S203中,将氧化石墨烯纳米片分散液中加入聚合物基体为2g三醋酸纤维素(分析纯;生产厂家ACROS;分子量966.845g/mol),搅拌溶解形成铸膜液,在80℃的水浴中搅拌溶解8小时,得到GO/CTA=0.075的铸膜液。随后转入S205中。In step S203, 2 g of cellulose triacetate (analytical pure; manufacturer ACROS; molecular weight 966.845 g/mol) is added to the graphene oxide nanosheet dispersion liquid as a polymer matrix, stirred and dissolved to form a casting solution, and the Stir and dissolve in a water bath for 8 hours to obtain a casting solution with GO/CTA=0.075. Then transfer to S205.
在步骤S205中,将铸膜液在玻璃板上刮制成膜,放入高压交流电场中,电场强度为1000V/cm,频率为1000Hz,电场作用装置如图3所示。施加电场50分钟后停止,干燥24小时。获得本实施例的渗透汽化膜。In step S205, the film-casting solution was scraped on a glass plate to form a film, and placed in a high-voltage AC electric field with an electric field strength of 1000 V/cm and a frequency of 1000 Hz. The electric field application device is shown in FIG. 3 . The electric field was stopped after 50 minutes of application and dried for 24 hours. The pervaporation membrane of this example was obtained.
本实施例所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in this example include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
本实施例渗透汽化实验结果为:水通量为9.06kg/(m2·h),NaCl的盐截留率为99.9%。The results of the pervaporation experiment in this embodiment are: the water flux is 9.06 kg/(m 2 ·h), and the NaCl salt rejection rate is 99.9%.
实施例6Example 6
参见图2,在本实施例步骤S201中,将0.2g的氧化石墨烯纳米片(商品号为796034;生产厂家Sigma-Aldrich;分子量4239.48g/mol,片径均值为0.8μm)与97.8g的1,4-二氧六环(Dioxane,生产厂家天津市科密欧化学试剂有限公司,分析纯)共混,制成分散液中氧化石墨烯纳米片的含量为0.2wt%的氧化石墨烯纳米片分散液,将氧化石墨烯纳米片分散液超声分散1h。随后转入S203中。Referring to Fig. 2, in step S201 of the present embodiment, 0.2g of graphene oxide nanosheets (product number is 796034; manufacturer Sigma-Aldrich; molecular weight 4239.48g/mol, average sheet diameter is 0.8μm) and 97.8g of 1,4-dioxane (Dioxane, produced by Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure) is blended to make a graphene oxide nanosheet whose content of graphene oxide nanosheets in the dispersion is 0.2wt%. Sheet dispersion liquid, the graphene oxide nanosheet dispersion liquid was ultrasonically dispersed for 1 h. Then transfer to S203.
在步骤S203中,将氧化石墨烯纳米片分散液中加入聚合物基体为2g三醋酸纤维素(分析纯;生产厂家ACROS;分子量966.845g/mol),搅拌溶解形成铸膜液,在80℃的水浴中搅拌溶解8小时,得到GO/CTA=0.1的铸膜液。随后转入S205中。In step S203, 2 g of cellulose triacetate (analytical pure; manufacturer ACROS; molecular weight 966.845 g/mol) is added to the graphene oxide nanosheet dispersion liquid as a polymer matrix, stirred and dissolved to form a casting solution, and the Stir and dissolve in a water bath for 8 hours to obtain a casting solution with GO/CTA=0.1. Then transfer to S205.
在步骤S205中,将铸膜液在玻璃板上刮制成膜,放入高压交流电场中,电场强度为1000V/cm,频率为1000Hz,电场作用装置如图3所示。施加电场50分钟后停止,干燥24小时。获得本实施例的渗透汽化膜。In step S205, the film-casting solution was scraped on a glass plate to form a film, and placed in a high-voltage AC electric field with an electric field strength of 1000 V/cm and a frequency of 1000 Hz. The electric field application device is shown in FIG. 3 . The electric field was stopped after 50 minutes of application and dried for 24 hours. The pervaporation membrane of this example was obtained.
本实施例所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in this example include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
本实施例渗透汽化实验结果为:水通量为9.07kg/(m2·h),NaCl的盐截留率为99.9%。The results of the pervaporation experiment in this embodiment are: the water flux is 9.07 kg/(m 2 ·h), and the salt rejection rate of NaCl is 99.9%.
实施例7Example 7
参见图2,在本实施例步骤S201中,将0.25g的氧化石墨烯纳米片(商品号为796034;生产厂家Sigma-Aldrich;分子量4239.48g/mol,片径均值为0.8μm)与97.75g的1,4-二氧六环(Dioxane,生产厂家天津市科密欧化学试剂有限公司,分析纯)共混,制成分散液中氧化石墨烯纳米片的含量为0.25wt%的氧化石墨烯纳米片分散液,将氧化石墨烯纳米片分散液超声分散1h。随后转入S203中。Referring to Fig. 2, in step S201 of the present embodiment, 0.25g of graphene oxide nanosheets (product number is 796034; manufacturer Sigma-Aldrich; molecular weight 4239.48g/mol, average sheet diameter is 0.8μm) and 97.75g of 1,4-Dioxane (Dioxane, produced by Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure) is blended to make a graphene oxide nanosheet whose content of graphene oxide nanosheets in the dispersion is 0.25wt%. Sheet dispersion liquid, the graphene oxide nanosheet dispersion liquid was ultrasonically dispersed for 1 h. Then transfer to S203.
在步骤S203中,将氧化石墨烯纳米片分散液中加入聚合物基体为2g三醋酸纤维素(分析纯;生产厂家ACROS;分子量966.845g/mol),搅拌溶解形成铸膜液,在80℃的水浴中搅拌溶解8小时,得到GO/CTA=0.125的铸膜液。随后转入S205中。In step S203, 2 g of cellulose triacetate (analytical pure; manufacturer ACROS; molecular weight 966.845 g/mol) is added to the graphene oxide nanosheet dispersion liquid as a polymer matrix, stirred and dissolved to form a casting solution, and the Stir and dissolve in a water bath for 8 hours to obtain a casting solution with GO/CTA=0.125. Then transfer to S205.
在步骤S205中,将铸膜液在玻璃板上刮制成膜,放入高压交流电场中,电场强度为1000V/cm,频率为1000Hz,电场作用装置如图3所示。施加电场50分钟后停止,干燥24小时。获得本实施例的渗透汽化膜。In step S205, the film-casting solution was scraped on a glass plate to form a film, and placed in a high-voltage AC electric field with an electric field strength of 1000 V/cm and a frequency of 1000 Hz. The electric field application device is shown in FIG. 3 . The electric field was stopped after 50 minutes of application and dried for 24 hours. The pervaporation membrane of this example was obtained.
本实施例所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in this example include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
本实施例渗透汽化实验结果为:水通量为9.11kg/(m2·h),NaCl的盐截留率为99.9%。The results of the pervaporation experiment in this embodiment are: the water flux is 9.11 kg/(m 2 ·h), and the NaCl salt rejection rate is 99.9%.
实施例8Example 8
参见图2,在本实施例步骤S201中,将0.3g的氧化石墨烯纳米片(商品号为796034;生产厂家Sigma-Aldrich;分子量4239.48g/mol,片径均值为0.8μm)与97.7g的1,4-二氧六环(Dioxane,生产厂家天津市科密欧化学试剂有限公司,分析纯)共混,制成分散液中氧化石墨烯纳米片的含量为0.3wt%的氧化石墨烯纳米片分散液,将氧化石墨烯纳米片分散液超声分散1h。随后转入S203中。Referring to Fig. 2, in step S201 of the present embodiment, 0.3g of graphene oxide nanosheets (product number is 796034; manufacturer Sigma-Aldrich; molecular weight 4239.48g/mol, mean value of sheet diameter is 0.8μm) and 97.7g of 1,4-Dioxane (Dioxane, produced by Tianjin Kemiou Chemical Reagent Co., Ltd., analytically pure) is blended to make a graphene oxide nanosheet whose content of graphene oxide nanosheets in the dispersion is 0.3wt%. Sheet dispersion liquid, the graphene oxide nanosheet dispersion liquid was ultrasonically dispersed for 1 h. Then transfer to S203.
在步骤S203中,将氧化石墨烯纳米片分散液中加入聚合物基体为2g三醋酸纤维素(分析纯;生产厂家ACROS;分子量966.845g/mol),搅拌溶解形成铸膜液,在80℃的水浴中搅拌溶解8小时,得到GO/CTA=0.15的铸膜液。随后转入S205中。In step S203, 2 g of cellulose triacetate (analytical pure; manufacturer ACROS; molecular weight 966.845 g/mol) is added to the graphene oxide nanosheet dispersion liquid as a polymer matrix, stirred and dissolved to form a casting solution, and the Stir and dissolve in a water bath for 8 hours to obtain a casting solution with GO/CTA=0.15. Then transfer to S205.
在步骤S205中,将铸膜液在玻璃板上刮制成膜,放入高压交流电场中,电场强度为1000V/cm,频率为1000Hz,电场作用装置如图3所示。施加电场50分钟后停止,干燥24小时。获得本实施例的渗透汽化膜。In step S205, the film-casting solution was scraped on a glass plate to form a film, and placed in a high-voltage AC electric field with an electric field strength of 1000 V/cm and a frequency of 1000 Hz. The electric field application device is shown in FIG. 3 . The electric field was stopped after 50 minutes of application and dried for 24 hours. The pervaporation membrane of this example was obtained.
本实施例所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in this example include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
本实施例渗透汽化实验结果为:水通量为9.23kg/(m2·h),NaCl的盐截留率为99.9%。The results of the pervaporation experiment in this embodiment are: the water flux is 9.23 kg/(m 2 ·h), and the NaCl salt rejection rate is 99.9%.
对比例1Comparative example 1
同理于实施例3中制备的铸膜液,将其在无电场环境下干燥24小时,获得未经电场取向的渗透汽化膜。In the same way as the casting solution prepared in Example 3, it was dried for 24 hours in an environment without an electric field to obtain a pervaporation film without electric field orientation.
对比例1所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in Comparative Example 1 include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
对比例1渗透汽化实验结果为:水通量为7.07kg/(m2·h),NaCl的盐截留率为99.9%。The pervaporation test results of Comparative Example 1 are: the water flux is 7.07 kg/(m 2 ·h), and the NaCl salt rejection rate is 99.9%.
对比例2Comparative example 2
同理于实施例4中制备的铸膜液,将其在无电场环境下干燥24小时,获得未经电场取向的渗透汽化膜。In the same way as the casting solution prepared in Example 4, it was dried for 24 hours in an environment without an electric field to obtain a pervaporation film without electric field orientation.
对比例2所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in Comparative Example 2 include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
对比例2渗透汽化实验结果为:水通量为7.24kg/(m2·h),NaCl的盐截留率为99.9%。The pervaporation test results of Comparative Example 2 are: the water flux is 7.24 kg/(m 2 ·h), and the salt rejection rate of NaCl is 99.9%.
对比例3Comparative example 3
同理于实施例5中制备的铸膜液,将其在无电场环境下干燥24小时,获得未经电场取向的渗透汽化膜。In the same way as the casting solution prepared in Example 5, it was dried for 24 hours in an environment without an electric field to obtain a pervaporation film without electric field orientation.
对比例3所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in Comparative Example 3 include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
对比例3渗透汽化实验结果为:水通量为7.36kg/(m2·h),NaCl的盐截留率为99.9%。The pervaporation test results of Comparative Example 3 are: the water flux is 7.36 kg/(m 2 ·h), and the NaCl salt rejection rate is 99.9%.
对比例4Comparative example 4
同理于实施例6中制备的铸膜液,将其在无电场环境下干燥24小时,获得未经电场取向的渗透汽化膜。In the same way as the casting solution prepared in Example 6, it was dried for 24 hours in an environment without an electric field to obtain a pervaporation film without electric field orientation.
对比例4所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in Comparative Example 4 include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
对比例4渗透汽化实验结果为:水通量为7.69kg/(m2·h),NaCl的盐截留率为99.9%。The pervaporation test results of Comparative Example 4 are: the water flux is 7.69 kg/(m 2 ·h), and the NaCl salt rejection rate is 99.9%.
对比例5Comparative example 5
同理于实施例7中制备的铸膜液,将其在无电场环境下干燥24小时,获得未经电场取向的渗透汽化膜。In the same way as the casting solution prepared in Example 7, it was dried for 24 hours in an environment without an electric field to obtain a pervaporation film without electric field orientation.
对比例5所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in Comparative Example 5 include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
对比例5渗透汽化实验结果为:水通量为7.95kg/(m2·h),NaCl的盐截留率为99.9%。The pervaporation test results of Comparative Example 5 are: the water flux is 7.95 kg/(m 2 ·h), and the NaCl salt rejection rate is 99.9%.
对比例6Comparative example 6
同理于实施例8中制备的铸膜液,将其在无电场环境下干燥24小时,获得未经电场取向的渗透汽化膜。In the same way as the casting solution prepared in Example 8, it was dried for 24 hours in an environment without an electric field to obtain a pervaporation film without electric field orientation.
对比例6所获得的渗透汽化膜进行渗透汽化实验条件包括:原料液为35g/L NaCl水溶液,流速1000mL/min,温度为50℃,渗透侧绝对压力0kPa。The pervaporation test conditions for the pervaporation membrane obtained in Comparative Example 6 include: the raw material liquid is 35g/L NaCl aqueous solution, the flow rate is 1000mL/min, the temperature is 50°C, and the absolute pressure on the permeate side is 0kPa.
对比例6渗透汽化实验结果为:水通量为8.53kg/(m2·h),NaCl的盐截留率为99.9%。The pervaporation test results of Comparative Example 6 are: the water flux is 8.53 kg/(m 2 ·h), and the NaCl salt rejection rate is 99.9%.
以上所述的仅是本发明的优选实例。应当指出对于本领域的普通技术人员来说,在本发明所提供的技术启示下,作为本领域的公知常识,还可以做出其它等同变型和改进,也应视为本发明的保护范围。What has been described above are only preferred examples of the present invention. It should be pointed out that for those skilled in the art, under the technical inspiration provided by the present invention, as common knowledge in the field, other equivalent modifications and improvements can also be made, which should also be regarded as the protection scope of the present invention.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110636406.9A CN115445439A (en) | 2021-06-08 | 2021-06-08 | Pervaporation membrane and preparation method and application thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110636406.9A CN115445439A (en) | 2021-06-08 | 2021-06-08 | Pervaporation membrane and preparation method and application thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
CN115445439A true CN115445439A (en) | 2022-12-09 |
Family
ID=84294669
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110636406.9A Pending CN115445439A (en) | 2021-06-08 | 2021-06-08 | Pervaporation membrane and preparation method and application thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115445439A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101983758A (en) * | 2010-10-21 | 2011-03-09 | 中国科学院苏州纳米技术与纳米仿生研究所 | Polymer/inorganic nanometer composite separation membrane and preparation method thereof |
CN104998560A (en) * | 2015-09-02 | 2015-10-28 | 中国海洋大学 | Preparation method of composite membrane containing oxidized graphene |
CN108404682A (en) * | 2018-03-12 | 2018-08-17 | 黄启洋 | A kind of graphene oxide film and preparation method thereof, preparation facilities and application |
CN108479423A (en) * | 2018-05-31 | 2018-09-04 | 大连理工大学 | A graphene oxide@polyvinyl alcohol mixed matrix pervaporation membrane and its preparation method |
CN112495195A (en) * | 2020-11-06 | 2021-03-16 | 大连理工大学 | A kind of preparation method and application method of graphene oxide/carbon nanotube asymmetric separation membrane |
-
2021
- 2021-06-08 CN CN202110636406.9A patent/CN115445439A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101983758A (en) * | 2010-10-21 | 2011-03-09 | 中国科学院苏州纳米技术与纳米仿生研究所 | Polymer/inorganic nanometer composite separation membrane and preparation method thereof |
CN104998560A (en) * | 2015-09-02 | 2015-10-28 | 中国海洋大学 | Preparation method of composite membrane containing oxidized graphene |
CN108404682A (en) * | 2018-03-12 | 2018-08-17 | 黄启洋 | A kind of graphene oxide film and preparation method thereof, preparation facilities and application |
CN108479423A (en) * | 2018-05-31 | 2018-09-04 | 大连理工大学 | A graphene oxide@polyvinyl alcohol mixed matrix pervaporation membrane and its preparation method |
CN112495195A (en) * | 2020-11-06 | 2021-03-16 | 大连理工大学 | A kind of preparation method and application method of graphene oxide/carbon nanotube asymmetric separation membrane |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Yang et al. | Preparation of graphene oxide modified poly (m-phenylene isophthalamide) nanofiltration membrane with improved water flux and antifouling property | |
Wang et al. | Mussel-inspired hybrid coatings that transform membrane hydrophobicity into high hydrophilicity and underwater superoleophobicity for oil-in-water emulsion separation | |
CN102794113B (en) | Super hydrophobic-supper lipophilic polymer porous film, preparation method and application thereof | |
CN105617882B (en) | A kind of compound forward osmosis membrane of chitosan-modified stannic oxide/graphene nano and preparation method thereof | |
CN111346523B (en) | Multifunctional bio-based composite microporous membrane and preparation method thereof | |
CN101249387B (en) | There is the high flux of laminar hole structure, withstand voltage milipore filter and preparation method thereof | |
CN107638816A (en) | Preparation method of dopamine-assisted dispersion graphene oxide-modified polyvinylidene fluoride ultrafiltration membrane | |
CN104211962A (en) | High dielectric polyimide composite material and preparation method thereof | |
CN108570155A (en) | Polyvinylidene fluoride film, method for forming the same, and method for purifying brine | |
CN1294181C (en) | Method for preparing poly(2,5-benzimidazole) | |
CN102343225A (en) | Preparation method of polyaniline (PANI) composite ultrafiltration membrane | |
Xie et al. | Conductive and stable polyphenylene/CNT composite membrane for electrically enhanced membrane fouling mitigation | |
Du et al. | Electric-field-assisted formation of cellulose triacetate/edge-oxidized graphene oxide mixed-matrix membranes for pervaporation desalination | |
CN108993165A (en) | A kind of layered inorganic material organic solvent nanofiltration composite membrane and preparation method thereof | |
CN115445439A (en) | Pervaporation membrane and preparation method and application thereof | |
CN110790967A (en) | Aramid nanofiber/polyvinyl alcohol/gold/conductive polyaniline composite film material and preparation method thereof | |
CN104289118A (en) | In situ polymerization method for controlling polyvinylidene fluoride ultrafiltration membrane structure | |
CN110152503A (en) | A kind of preparation method of graphene oxide and self-contained microporous polymer composite solvent-resistant nanofiltration membrane | |
CN102357347A (en) | Preparation method of modified polyacrylonitrile film | |
CN103120902A (en) | Preparation method of carbon nanotube nanosilica co-modified polyvinyl alcohol composite ultra-filtration membrane | |
CN105013331B (en) | Method for preparing PDMS/PVDF blend pervaporation membrane by using membrane casting solution | |
CN109173745B (en) | A kind of hollow fiber ultrafiltration membrane and preparation method thereof | |
CN110665372A (en) | Porous membrane for permeation separation of small molecules, preparation method and application thereof | |
CN112717709B (en) | Preparation method of high-flux and high-stability two-dimensional mica-doped ultrafiltration membrane | |
CN114713295B (en) | Monovalent selective cation exchange membrane and preparation method and application thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20221209 |