CN108816064A - A kind of preparation method of the chitosan nano fiber membrane of growth in situ metal-organic framework material - Google Patents
A kind of preparation method of the chitosan nano fiber membrane of growth in situ metal-organic framework material Download PDFInfo
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- 229920001661 Chitosan Polymers 0.000 title claims abstract description 188
- 239000012528 membrane Substances 0.000 title claims abstract description 135
- 239000002121 nanofiber Substances 0.000 title claims abstract description 81
- 239000012621 metal-organic framework Substances 0.000 title claims abstract description 68
- 238000002360 preparation method Methods 0.000 title claims abstract description 40
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 38
- 239000000463 material Substances 0.000 title claims abstract description 38
- 239000000835 fiber Substances 0.000 claims abstract description 73
- 239000003446 ligand Substances 0.000 claims abstract description 22
- 238000001523 electrospinning Methods 0.000 claims abstract description 16
- 239000003960 organic solvent Substances 0.000 claims abstract description 16
- 229910052751 metal Inorganic materials 0.000 claims abstract description 13
- 239000002184 metal Substances 0.000 claims abstract description 13
- 230000009920 chelation Effects 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000000243 solution Substances 0.000 claims description 59
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 51
- 239000002253 acid Substances 0.000 claims description 26
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 17
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 17
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 16
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 16
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 claims description 14
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 13
- 238000009987 spinning Methods 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 12
- 150000003839 salts Chemical class 0.000 claims description 10
- 238000002347 injection Methods 0.000 claims description 8
- 239000007924 injection Substances 0.000 claims description 8
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical group [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 claims description 8
- QMKYBPDZANOJGF-UHFFFAOYSA-N benzene-1,3,5-tricarboxylic acid Chemical compound OC(=O)C1=CC(C(O)=O)=CC(C(O)=O)=C1 QMKYBPDZANOJGF-UHFFFAOYSA-N 0.000 claims description 6
- 238000005406 washing Methods 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 5
- LXBGSDVWAMZHDD-UHFFFAOYSA-N 2-methyl-1h-imidazole Chemical compound CC1=NC=CN1 LXBGSDVWAMZHDD-UHFFFAOYSA-N 0.000 claims description 4
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 claims description 4
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 4
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 claims description 4
- OPQARKPSCNTWTJ-UHFFFAOYSA-L copper(ii) acetate Chemical compound [Cu+2].CC([O-])=O.CC([O-])=O OPQARKPSCNTWTJ-UHFFFAOYSA-L 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 4
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 claims description 4
- DUNKXUFBGCUVQW-UHFFFAOYSA-J zirconium tetrachloride Chemical compound Cl[Zr](Cl)(Cl)Cl DUNKXUFBGCUVQW-UHFFFAOYSA-J 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 3
- GPNNOCMCNFXRAO-UHFFFAOYSA-N 2-aminoterephthalic acid Chemical compound NC1=CC(C(O)=O)=CC=C1C(O)=O GPNNOCMCNFXRAO-UHFFFAOYSA-N 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 150000001768 cations Chemical class 0.000 claims description 2
- 229960000935 dehydrated alcohol Drugs 0.000 claims description 2
- 229910052747 lanthanoid Inorganic materials 0.000 claims description 2
- 150000002602 lanthanoids Chemical class 0.000 claims description 2
- 230000007935 neutral effect Effects 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 150000002891 organic anions Chemical class 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims description 2
- 238000009210 therapy by ultrasound Methods 0.000 claims description 2
- 230000007704 transition Effects 0.000 claims description 2
- 239000013522 chelant Substances 0.000 claims 1
- FEOIEZBSUVRDJZ-UHFFFAOYSA-N chromium;nitric acid Chemical compound [Cr].O[N+]([O-])=O FEOIEZBSUVRDJZ-UHFFFAOYSA-N 0.000 claims 1
- 230000005611 electricity Effects 0.000 claims 1
- 238000010041 electrostatic spinning Methods 0.000 claims 1
- 230000003068 static effect Effects 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 25
- 239000002131 composite material Substances 0.000 abstract description 12
- 239000000975 dye Substances 0.000 abstract description 5
- 238000001914 filtration Methods 0.000 abstract description 4
- 229920000642 polymer Polymers 0.000 abstract description 4
- 230000002378 acidificating effect Effects 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 36
- 229960000583 acetic acid Drugs 0.000 description 18
- 239000012362 glacial acetic acid Substances 0.000 description 18
- 238000000034 method Methods 0.000 description 15
- 239000013154 zeolitic imidazolate framework-8 Substances 0.000 description 15
- MFLKDEMTKSVIBK-UHFFFAOYSA-N zinc;2-methylimidazol-3-ide Chemical compound [Zn+2].CC1=NC=C[N-]1.CC1=NC=C[N-]1 MFLKDEMTKSVIBK-UHFFFAOYSA-N 0.000 description 15
- 239000011259 mixed solution Substances 0.000 description 12
- 229910021645 metal ion Inorganic materials 0.000 description 10
- 229940043267 rhodamine b Drugs 0.000 description 9
- 150000002500 ions Chemical group 0.000 description 7
- 239000007787 solid Substances 0.000 description 7
- PHFQLYPOURZARY-UHFFFAOYSA-N chromium trinitrate Chemical compound [Cr+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O PHFQLYPOURZARY-UHFFFAOYSA-N 0.000 description 6
- 239000013078 crystal Substances 0.000 description 6
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 6
- 238000011068 loading method Methods 0.000 description 5
- -1 polyoxyethylene Polymers 0.000 description 5
- 239000013148 Cu-BTC MOF Substances 0.000 description 4
- 239000013178 MIL-101(Cr) Substances 0.000 description 4
- 238000002835 absorbance Methods 0.000 description 4
- 229940107698 malachite green Drugs 0.000 description 4
- FDZZZRQASAIRJF-UHFFFAOYSA-M malachite green Chemical compound [Cl-].C1=CC(N(C)C)=CC=C1C(C=1C=CC=CC=1)=C1C=CC(=[N+](C)C)C=C1 FDZZZRQASAIRJF-UHFFFAOYSA-M 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 125000003277 amino group Chemical group 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000013110 organic ligand Substances 0.000 description 3
- 229920001282 polysaccharide Polymers 0.000 description 3
- 239000005017 polysaccharide Substances 0.000 description 3
- 150000004804 polysaccharides Chemical class 0.000 description 3
- 238000001878 scanning electron micrograph Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 239000010949 copper Substances 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- CXKWCBBOMKCUKX-UHFFFAOYSA-M methylene blue Chemical compound [Cl-].C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 CXKWCBBOMKCUKX-UHFFFAOYSA-M 0.000 description 2
- 229960000907 methylthioninium chloride Drugs 0.000 description 2
- 229920005615 natural polymer Polymers 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 238000013519 translation Methods 0.000 description 2
- 238000012795 verification Methods 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- GOJUJUVQIVIZAV-UHFFFAOYSA-N 2-amino-4,6-dichloropyrimidine-5-carbaldehyde Chemical group NC1=NC(Cl)=C(C=O)C(Cl)=N1 GOJUJUVQIVIZAV-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 229920002101 Chitin Polymers 0.000 description 1
- 241000907663 Siproeta stelenes Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000783 alginic acid Substances 0.000 description 1
- 229920000615 alginic acid Polymers 0.000 description 1
- 235000010443 alginic acid Nutrition 0.000 description 1
- 229960001126 alginic acid Drugs 0.000 description 1
- 150000004781 alginic acids Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 229920006317 cationic polymer Polymers 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 230000000850 deacetylating effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000012377 drug delivery Methods 0.000 description 1
- 238000000578 dry spinning Methods 0.000 description 1
- 229960004756 ethanol Drugs 0.000 description 1
- 231100000086 high toxicity Toxicity 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 125000000325 methylidene group Chemical group [H]C([H])=* 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- PYWVYCXTNDRMGF-UHFFFAOYSA-N rhodamine B Chemical compound [Cl-].C=12C=CC(=[N+](CC)CC)C=C2OC2=CC(N(CC)CC)=CC=C2C=1C1=CC=CC=C1C(O)=O PYWVYCXTNDRMGF-UHFFFAOYSA-N 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 229910001428 transition metal ion Inorganic materials 0.000 description 1
- AAAQKTZKLRYKHR-UHFFFAOYSA-N triphenylmethane Chemical compound C1=CC=CC=C1C(C=1C=CC=CC=1)C1=CC=CC=C1 AAAQKTZKLRYKHR-UHFFFAOYSA-N 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000002166 wet spinning Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/74—Natural macromolecular material or derivatives thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0006—Organic membrane manufacture by chemical reactions
-
- 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
- B01D69/08—Hollow fibre membranes
- B01D69/081—Hollow fibre membranes characterised by the fibre diameter
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/39—Electrospinning
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/308—Dyes; Colorants; Fluorescent agents
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- Chemical Kinetics & Catalysis (AREA)
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Analytical Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Manufacturing & Machinery (AREA)
- Artificial Filaments (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
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Abstract
本发明属于高分子复合材料制备的技术领域,具体的说是一种原位生长金属有机框架材料的壳聚糖纳米纤维膜的制备方法。将壳聚糖通过静电纺丝得壳聚糖纳米纤维膜;再将其在酸性环境下与MOFs材料中的金属结点螯合;鳌合后加入配体,在壳聚糖纤维表面原位生长MOFs材料,得到原位生长MOFs材料壳聚糖纳米纤维膜。本发明既解决了MOFs材料与壳聚糖复合难以均匀分散的问题,又提高了两者的结合强度,避免了MOFs材料的脱落。该复合材料具有制备工艺简单,吸附效率高,表面均匀且稳定性好等优点,能够应用于多种染料的吸附。同时,在气体过滤、有机溶剂分离以及水处理中也具有潜在的应用价值。The invention belongs to the technical field of polymer composite material preparation, and specifically relates to a preparation method of a chitosan nanofiber film grown in-situ as a metal-organic framework material. Chitosan nanofiber membrane is obtained by electrospinning chitosan; then it is chelated with metal nodes in MOFs material in an acidic environment; after chelation, ligands are added to grow in situ on the surface of chitosan fibers MOFs material, obtained in situ growth MOFs material chitosan nanofiber membrane. The invention not only solves the problem that the composite of MOFs material and chitosan is difficult to uniformly disperse, but also improves the bonding strength of the two, and avoids the falling off of the MOFs material. The composite material has the advantages of simple preparation process, high adsorption efficiency, uniform surface and good stability, and can be applied to the adsorption of various dyes. At the same time, it also has potential application value in gas filtration, organic solvent separation and water treatment.
Description
技术领域technical field
本发明属于高分子复合材料制备的技术领域,具体的说是一种原位生长金属有机框架材料的壳聚糖纳米纤维膜的制备方法。The invention belongs to the technical field of polymer composite material preparation, and specifically relates to a preparation method of a chitosan nanofiber film grown in-situ as a metal-organic framework material.
背景技术Background technique
金属有机框架(MOFs)材料是一类具有只允许特定分子进入孔隙的形状和结构的材料。由于有机配体和金属离子或团簇的排列具有明显的方向性,因而可以形成不同的框架孔隙结构。选择的有机配体或金属离子不同,MOFs材料的晶体结构也不同,通常采用过渡金属离子作为结点,如Zn,Cu,Ni,Co等,与多官能团的有机配体结合进行制备(Nature,2015,520:148-150)。Metal-organic frameworks (MOFs) materials are a class of materials with shapes and structures that only allow specific molecules to enter the pores. Due to the obvious directionality of the arrangement of organic ligands and metal ions or clusters, different framework pore structures can be formed. Depending on the selected organic ligands or metal ions, the crystal structure of MOFs materials is also different. Usually transition metal ions are used as nodes, such as Zn, Cu, Ni, Co, etc., combined with multifunctional organic ligands to prepare (Nature, 2015, 520:148-150).
MOFs材料呈固体粉末状,机械强度低,通常需要与其它易于加工成型的材料结合制备复合材料(Advanced Engineering Materials,2008,10(12):1151-1155)。其中,专利CN 107051398A公开了一种将MOFs原位生长在丝蛋白上方法,并制备得到了过滤效率高、负载量高、稳定性好的薄膜材料;专利CN 107841879A公开了一种海藻酸静电纺丝纤维表面原位生长MOFs的方法。此外,将MOFs原位生长在羧基纤维素(Cellulose,2012,19(5):1771-1779)、羧甲基纤维素(Nanoscale,2017,9(35):12850-12854)上已有报道。MOFs materials are solid powders with low mechanical strength, and usually need to be combined with other materials that are easy to process and shape to prepare composite materials (Advanced Engineering Materials, 2008, 10(12):1151-1155). Among them, patent CN 107051398A discloses a method of growing MOFs on silk protein in situ, and prepares a film material with high filtration efficiency, high load capacity and good stability; A method for in situ growth of MOFs on the surface of silk fibers. In addition, in situ growth of MOFs on carboxycellulose (Cellulose, 2012, 19(5): 1771-1779) and carboxymethylcellulose (Nanoscale, 2017, 9(35): 12850-12854) has been reported.
壳聚糖(Chitosan,CS)是由甲壳素脱乙酰基得到的碱性多糖,也是自然界中唯一的天然存在的阳离子聚合物,具有廉价、无毒、可生物降解、成膜性好等优点,近年来被公认为是未来极具发展潜力的绿色材料。但仅在组织工程、药物输送等领域应用广泛(Nanoscale,2017,9(12):4154-4161)。Chitosan (Chitosan, CS) is an alkaline polysaccharide obtained by deacetylating chitin, and it is also the only naturally occurring cationic polymer in nature. In recent years, it has been recognized as a green material with great development potential in the future. However, it is only widely used in the fields of tissue engineering and drug delivery (Nanoscale, 2017, 9(12): 4154-4161).
虽然将MOFs与纤维素、海藻酸及丝蛋白的其它天然高分子原位复合已有研究,其是通过MOFs原位生长机理是天然高分子表面的羧基所带的负电荷与金属离子表面的正电荷产生一定的静电引力,进而促进了高分子与金属离子的初始配位作用,使金属离子在纤维素表面形成晶核,配体的引入则促进了晶体的生长。但是将MOFs原位生长在壳聚糖表面制备复合材料未见报道。Although the in situ compounding of MOFs with cellulose, alginic acid and other natural polymers of silk protein has been studied, the in situ growth mechanism of MOFs is the negative charge of the carboxyl group on the surface of the natural polymer and the positive charge on the surface of the metal ion. The charge produces a certain electrostatic attraction, which in turn promotes the initial coordination between the polymer and the metal ion, making the metal ion form a crystal nucleus on the surface of the cellulose, and the introduction of the ligand promotes the growth of the crystal. However, the in situ growth of MOFs on the surface of chitosan to prepare composite materials has not been reported.
发明内容Contents of the invention
本发明的目的在于提供了一种原位生长金属有机框架材料的壳聚糖纳米纤维膜的制备方法。The object of the present invention is to provide a preparation method of a chitosan nanofiber membrane of a metal organic framework material grown in situ.
为实现上述目的,本发明采用技术方案为:In order to achieve the above object, the technical solution adopted by the present invention is:
一种原位生长金属有机框架材料(MOFs)的壳聚糖纳米纤维膜的制备方法:将壳聚糖通过静电纺丝得壳聚糖纳米纤维膜;再将其在酸性环境下与MOFs材料中的金属结点螯合;鳌合后加入配体,在壳聚糖纤维表面原位生长MOFs材料,得到原位生长MOFs材料壳聚糖纳米纤维膜。A preparation method of chitosan nanofibrous membrane of in-situ growth metal-organic framework (MOFs): chitosan is electrospun to obtain chitosan nanofiber membrane; The metal node chelation; after chelation, ligands are added to grow MOFs materials in situ on the surface of chitosan fibers to obtain in situ growth MOFs material chitosan nanofiber membranes.
进一步的说是,将壳聚糖纳米纤维膜与金属盐加入到有机溶剂中,并在体系内加入浓酸溶液;而后在速率为100r/min-300r/min的条件下搅拌0.5h-3.5h,然后静置1h-3h;静置沉淀后用有机溶剂洗涤3-5遍,洗涤后加入到碱溶液中,再加入配体搅拌均匀后经有机溶剂洗涤,干燥即可得到表面生长MOFs的壳聚糖纳米纤维膜。Furthermore, the chitosan nanofiber membrane and the metal salt are added to the organic solvent, and a concentrated acid solution is added to the system; then stirred at a rate of 100r/min-300r/min for 0.5h-3.5h , and then stand still for 1h-3h; after standing for precipitation, wash with organic solvent for 3-5 times, add to alkaline solution after washing, add ligand and stir evenly, wash with organic solvent, and dry to get the shell of MOFs grown on the surface Polysaccharide nanofiber membranes.
所述金属盐是指以主族元素、过渡元素或镧系元素为金属阳离子的水溶性盐类中的一种或几种;其用量为壳聚糖纤维膜质量的1-10倍,所述配体是指含氧或氮的含羧基有机阴离子配体中的一种或几种,或与含氮杂环有机中性配体共同使用,配体加入量为壳聚糖纤维膜质量的1-20倍,The metal salt refers to one or more of the water-soluble salts with main group elements, transition elements or lanthanides as metal cations; its consumption is 1-10 times of the chitosan fiber membrane quality, and the The ligand refers to one or more of the carboxyl-containing organic anion ligands containing oxygen or nitrogen, or used together with the nitrogen-containing heterocyclic organic neutral ligand, and the amount of the ligand added is 1% of the mass of the chitosan fiber membrane. -20 times,
优选金属盐的用量为壳聚糖纤维膜质量的3-5倍,优选配体加入量为壳聚糖纤维膜质量的2-10倍。Preferably, the amount of the metal salt is 3-5 times the mass of the chitosan fiber membrane, and the preferred addition of the ligand is 2-10 times the mass of the chitosan fiber membrane.
优选所述金属盐为硝酸锌、氯化钴、醋酸铜、硝酸铬、四氯化锆或氯化镍;所述配体为2-甲基咪唑、均苯三酸、对苯二甲酸、2-氨基对苯二甲酸或对苯二甲酸。Preferably, the metal salt is zinc nitrate, cobalt chloride, copper acetate, chromium nitrate, zirconium tetrachloride or nickel chloride; the ligand is 2-methylimidazole, trimesic acid, terephthalic acid, 2 - aminoterephthalic acid or terephthalic acid.
同时上述金属盐与配体形成MOFs材料时两者之间的用量关系可以按现有的制备方法进行,并调配。At the same time, the amount relationship between the metal salt and the ligand when forming the MOFs material can be carried out and formulated according to the existing preparation method.
所述有机溶剂是指无水甲醇和/或无水乙醇;有机溶剂与壳聚糖纤维膜的体积质量(mL/g)比为200-1000:1,优选为300-700:1;所述洗涤采用的有机溶剂为无水甲醇和/或无水乙醇;Described organic solvent refers to absolute methanol and/or absolute ethanol; The volume mass (mL/g) ratio of organic solvent and chitosan fiber film is 200-1000: 1, is preferably 300-700: 1; The organic solvent used for washing is absolute methanol and/or absolute ethanol;
所述碱溶液为浓度为0.05mol/L-0.3mol/L的氨水溶液;氨水溶液与壳聚糖纤维膜的体积质量(mL/g)比为100-2000:1,优选为500-1000:1。Described alkali solution is the ammonia solution that concentration is 0.05mol/L-0.3mol/L; The volume mass (mL/g) ratio of ammonia solution and chitosan fiber membrane is 100-2000: 1, is preferably 500-1000: 1.
所述加入配体后体系在转速为100-300r/min的条件下搅拌0.5h-5h,然后用有机溶剂洗涤3-5遍后干燥,干燥条件为30℃-50℃,5min-30min。After the ligand is added, the system is stirred for 0.5h-5h at a rotational speed of 100-300r/min, then washed with an organic solvent for 3-5 times and then dried. The drying condition is 30°C-50°C, 5min-30min.
所述壳聚糖纳米纤维是以壳聚糖为原料通过静电纺丝方式获得的直径小于200nm的纤维。其中,静电纺丝方式例如,湿法纺丝、干法纺丝等 The chitosan nanofiber is a fiber with a diameter of less than 200nm obtained by electrospinning chitosan as a raw material. Among them, the electrospinning method , for example, wet spinning, dry spinning, etc.
所述壳聚糖纳米纤维为以壳聚糖为原料通过静电纺丝的方式制备获得,将壳聚糖与聚氧化乙烯分别缓慢加入到浓酸溶液中混匀后加入水得到均匀粘稠的壳聚糖待纺溶液,而后超声处理后进行静电纺丝,剥离后即得到壳聚糖纤维;其中,酸溶液的终浓度(质量浓度)为1%-10%,壳聚糖占酸溶液质量的0.5%-5%,聚氧化乙烯占酸溶液质量的0.1%-10%。The chitosan nanofibers are prepared by electrospinning with chitosan as a raw material. Chitosan and polyethylene oxide are slowly added to a concentrated acid solution and mixed, and then water is added to obtain a uniform and viscous shell. The solution of polysaccharide to be spun is then subjected to electrospinning after ultrasonic treatment, and chitosan fibers are obtained after peeling off; wherein, the final concentration (mass concentration) of the acid solution is 1%-10%, and chitosan accounts for 1% of the acid solution quality. 0.5%-5%, polyethylene oxide accounts for 0.1%-10% of the acid solution mass.
优选的酸溶液的终浓度(质量浓度)为3%-5%,壳聚糖占酸溶液质量的1%-3%,聚氧化乙烯占酸溶液质量的0.1%-1%。The preferred final concentration (mass concentration) of the acid solution is 3%-5%, chitosan accounts for 1%-3% of the mass of the acid solution, and polyethylene oxide accounts for 0.1%-1% of the mass of the acid solution.
将溶液超声后,用注射器抽取溶液进行静电纺丝,采用锡纸作为接收板,纺丝条件为:正压为2.0KV-13.0KV,负压为-5.0KV--10.0KV,推注速度为0.02mm/min-0.15mm/min,平移速度为100mm/min-500mm/min,接收滚筒的转速为5r/min-30r/min。After ultrasonicating the solution, extract the solution with a syringe for electrospinning, using tin foil as the receiving plate, the spinning conditions are: positive pressure 2.0KV-13.0KV, negative pressure -5.0KV-10.0KV, injection speed 0.02 mm/min-0.15mm/min, the translational speed is 100mm/min-500mm/min, and the rotational speed of the receiving drum is 5r/min-30r/min.
本发明的原位生长MOFs的壳聚糖纳米纤维膜的制备具有以下优点:The preparation of the chitosan nanofibrous membrane of MOFs grown in situ of the present invention has the following advantages:
(1)在酸性条件下,分子链上的氨基对MOFs中的金属离子具有较好的螯合作用,进而为MOFs晶体提供合适、均匀的成核位点,然后引入配体时将体系调节至碱性,使金属离子与配体反应得到MOFs,进而均匀的生长在壳聚糖纳米纤维膜表面。这有效解决了MOFs较难在壳聚糖表面原位生长的问题,并且避免了MOFs与壳聚糖共混时导致的MOFs分散性差、负载率低以及二者结合牢度差的技术问题。(1) Under acidic conditions, the amino groups on the molecular chain have a good chelation effect on metal ions in MOFs, thereby providing suitable and uniform nucleation sites for MOFs crystals, and then adjusting the system to Alkaline, metal ions react with ligands to obtain MOFs, and then grow uniformly on the surface of chitosan nanofiber membrane. This effectively solves the problem that MOFs are difficult to grow in situ on the surface of chitosan, and avoids the technical problems of poor dispersion of MOFs, low loading rate and poor binding fastness of MOFs caused by blending MOFs and chitosan.
(2)本发明采用的壳聚糖纳米纤维与壳聚糖相比,具有较大的比表面积以及多孔结构,可以有效促进其表面氨基与金属离子间螯合作用,并且其孔径结构可以通过改变制备工艺进行调节,而MOFs颗粒具有介孔或微孔结构,也可以根据不同用途对不同孔径的MOFs进行筛选,这种可调节的分级多孔结构有利于MOFs-壳聚糖复合材料在吸附或过滤中应用,并能提高使用效率。(2) compared with chitosan, the chitosan nanofibers adopted by the present invention have larger specific surface area and porous structure, which can effectively promote the chelation between its surface amino groups and metal ions, and its pore structure can be changed by changing The preparation process is adjusted, and MOFs particles have a mesoporous or microporous structure, and MOFs with different pore sizes can also be screened according to different uses. This adjustable hierarchical porous structure is conducive to the adsorption or filtration of MOFs-chitosan composites. application and improve efficiency.
(3)本发明所用方法简单易行,易于大规模生产。(3) The method used in the present invention is simple and easy to implement, and is easy to produce on a large scale.
附图说明Description of drawings
图1是本发明实施例提供的原位生长MOFs的壳聚糖纤维膜制备流程图。Fig. 1 is a flowchart of preparation of chitosan fiber membranes for in-situ growth of MOFs provided by an example of the present invention.
图2是本发明实施例1制备的壳聚糖纳米纤维膜的SEM图。Fig. 2 is the SEM image of the chitosan nanofiber membrane prepared in Example 1 of the present invention.
图3是本发明实施例1制备的ZIF-8@壳聚糖纤维膜的实物图。Fig. 3 is the actual picture of the ZIF-8@chitosan fiber membrane prepared in Example 1 of the present invention.
图4是本发明实施例1制备的ZIF-8@壳聚糖纤维膜的SEM图。Fig. 4 is the SEM image of the ZIF-8@chitosan fiber membrane prepared in Example 1 of the present invention.
图5是本发明实施例1制备的ZIF-8@壳聚糖纤维膜的吸光度曲线。Fig. 5 is the absorbance curve of the ZIF-8@chitosan fiber membrane prepared in Example 1 of the present invention.
图6是本发明实施例1制备的ZIF-8@壳聚糖纤维膜吸附后罗丹明b溶液颜色的变化(左:0.1%罗丹明b溶液,右:复合膜吸附24h后的罗丹明b溶液)。Fig. 6 is the variation of rhodamine b solution color (left: 0.1% rhodamine b solution, right: rhodamine b solution after composite membrane adsorption 24h) after ZIF-8@chitosan fiber film adsorption prepared by Example 1 of the present invention ).
图7是本发明实施例2制备的ZIF-67@壳聚糖纤维膜的吸光度曲线。Fig. 7 is the absorbance curve of the ZIF-67@chitosan fiber membrane prepared in Example 2 of the present invention.
具体实施方式Detailed ways
以下通过具体实施实例进一步描述本方法的可行性,但并不意味着本发明局限于这些实例。The feasibility of the method is further described below through specific implementation examples, but it does not mean that the present invention is limited to these examples.
本发明以壳聚糖纳米纤维膜为原料,而壳聚糖分子结构中没有羧基,尽管壳聚糖分子中的氨基在酸性条件下也可以对金属离子产生一定的螯合作用,但引入配体后需要在碱性条件下才能是金属离子与配体形成MOFs晶体;进而为采用原位生长法将MOFs负载在壳聚糖纤维膜表面,制备了一种均匀多孔的壳聚糖纤维膜材料。其在不影响壳聚糖纤维性质的前提下,使MOFs材料与壳聚糖纤维膜实现牢固的结合,解决了MOFs在聚合物中容易聚集的难题。此外,MOFs负载在壳聚糖纳米纤维膜上形成可调的多孔结构具有较大的比表面积,有望作为吸附或过滤材料应用分离及气体存储等领域中。The present invention uses chitosan nanofiber membrane as raw material, and there is no carboxyl group in chitosan molecular structure, although the amino group in chitosan molecule also can produce certain chelating action to metal ion under acidic conditions, but the introduction of ligand Finally, metal ions and ligands need to be under alkaline conditions to form MOFs crystals; and then MOFs are loaded on the surface of chitosan fiber membrane by in situ growth method, and a uniform porous chitosan fiber membrane material is prepared. Under the premise of not affecting the properties of chitosan fibers, it enables MOFs materials to be firmly combined with chitosan fiber membranes, and solves the problem that MOFs are easy to aggregate in polymers. In addition, MOFs loaded on the chitosan nanofiber membrane to form an adjustable porous structure has a large specific surface area, which is expected to be used as an adsorption or filter material in the fields of separation and gas storage.
本发明既解决了MOFs材料与壳聚糖复合难以均匀分散的问题,又提高了两者的结合强度,避免了MOFs材料的脱落。该复合材料具有制备工艺简单,吸附效率高,表面均匀且稳定性好等优点,能够应用于多种染料的吸附。同时,在气体过滤、有机溶剂分离以及水处理中也具有潜在的应用价值。The invention not only solves the problem that the composite of MOFs material and chitosan is difficult to uniformly disperse, but also improves the bonding strength of the two, and avoids the falling off of the MOFs material. The composite material has the advantages of simple preparation process, high adsorption efficiency, uniform surface and good stability, and can be applied to the adsorption of various dyes. At the same time, it also has potential application value in gas filtration, organic solvent separation and water treatment.
实施例1Example 1
原位生长法制备ZIF-8@壳聚糖纳米纤维膜Preparation of ZIF-8@chitosan nanofibrous membrane by in situ growth method
1)壳聚糖纳米纤维的制备:将壳聚糖与聚氧化乙烯分别缓慢加入到冰醋酸中得混合液,其中,混合液中冰醋酸溶液终浓度(质量浓度)为3%,壳聚糖占酸溶液质量的1%,聚氧化乙烯占酸溶液质量的0.1%;加入后开启磁力搅拌器,转速为500r/min,搅拌30min后固体完全溶解;溶解后将溶液在300W的强度下超声10min后,用5mL的注射器抽取溶液进行静电纺丝,采用锡纸作为接收板,纺丝条件为:正压为2.0KV,负压为-10.0KV,推注速度为0.02mm/min,平移速度为100mm/min,接收滚筒的转速为5r/min;纺丝结束后,将锡纸取下,剪成2cm×2cm的小块,将壳聚糖纤维膜从锡纸上剥离(参见图2);1) Preparation of chitosan nanofibers: Slowly add chitosan and polyethylene oxide respectively in glacial acetic acid to obtain a mixed solution, wherein the final concentration (mass concentration) of the glacial acetic acid solution in the mixed solution is 3%, and the chitosan Accounting for 1% of the mass of the acid solution, polyethylene oxide accounts for 0.1% of the mass of the acid solution; after adding, turn on the magnetic stirrer at a speed of 500r/min, and stir for 30 minutes to completely dissolve the solid; after dissolution, ultrasonicate the solution at 300W for 10 minutes Finally, use a 5mL syringe to extract the solution for electrospinning, using tin foil as the receiving plate, the spinning conditions are: positive pressure 2.0KV, negative pressure -10.0KV, injection speed 0.02mm/min, translation speed 100mm /min, the rotating speed of receiving drum is 5r/min; After spinning finishes, tinfoil is taken off, is cut into the fritter of 2cm * 2cm, and chitosan fiber film is peeled off from tinfoil (referring to Fig. 2);
2)Zn-壳聚糖纳米纤维膜的制备:取壳聚糖纳米纤维膜与硝酸锌加入到甲醇中,然后滴加1g冰醋酸。其中,硝酸锌的用量为壳聚糖纤维膜质量的3倍,即0.15g;甲醇与壳聚糖纤维膜的体积质量(mL/g)比为300:1。体系在100r/min速度下搅拌0.5h,静置1h后,用甲醇洗涤3次,去除纤维表面未螯合的Zn2+离子,得到Zn-壳聚糖纳米纤维膜;2) Preparation of Zn-chitosan nanofiber membrane: take chitosan nanofiber membrane and zinc nitrate and add them to methanol, then add 1 g of glacial acetic acid dropwise. Among them, the dosage of zinc nitrate is 3 times of the mass of chitosan fiber membrane, that is, 0.15 g; the volume mass (mL/g) ratio of methanol to chitosan fiber membrane is 300:1. The system was stirred at a speed of 100r/min for 0.5h, and after standing for 1h, it was washed 3 times with methanol to remove unchelated Zn ions on the fiber surface to obtain a Zn-chitosan nanofiber membrane;
3)将Zn-壳聚糖纳米纤维膜加入到氨水(氨水浓度0.05mol/L,其与壳聚糖纤维膜的体积质量(mL/g)比为500:1)中,然后加入2-甲基咪唑(2-甲基咪唑0.1g,用量为壳聚糖纤维膜质量的2倍),该体系在100r/min下搅拌0.5h;然后用甲醇洗涤3遍后,在30℃下鼓风干燥5min,即可得到表面生长ZIF-8的壳聚糖纳米纤维膜。经过测试,ZIF-8@壳聚糖纳米纤维膜中ZIF-8的负载量较高(8.3%)。从SEM图中看出,ZIF-8在壳聚糖纤维中形成的晶体结构规则且分散均匀。(参见图3和4)。3) Add the Zn-chitosan nanofiber membrane to ammonia water (the concentration of ammonia water is 0.05mol/L, and the volume mass (mL/g) ratio of it to the chitosan fiber membrane is 500:1), and then add 2-formazan imidazole (2-methylimidazole 0.1g, the dosage is 2 times the mass of the chitosan fiber membrane), the system was stirred at 100r/min for 0.5h; then washed with methanol for 3 times, then air-dried at 30°C After 5 minutes, the chitosan nanofiber membrane with ZIF-8 grown on the surface can be obtained. After testing, the loading of ZIF-8 in the ZIF-8@chitosan nanofiber membrane is relatively high (8.3%). It can be seen from the SEM images that the crystal structure formed by ZIF-8 in chitosan fibers is regular and uniformly dispersed. (See Figures 3 and 4).
验证1Verification 1
ZIF-8@壳聚糖纤维复合膜用于罗丹明b的吸附Adsorption of rhodamine b by ZIF-8@chitosan fiber composite membrane
称取实例1中制备的0.05g ZIF-8@壳聚糖纤维复合膜、0.05g壳聚糖纳米纤维膜以及1mg ZIF-8,分别置于0.1%的罗丹明b-乙醇溶液中,密封。待吸附24h后,分别取上清液200μL加入比色皿中,采用紫外-可见光分光光度计法测试其在554nm处的吸光度值(图5),进而计算得出吸附后罗丹明b的浓度,图6为吸附前后罗丹明b溶液的颜色变化。经过测试,在壳聚糖纳米纤维膜、ZIF-8以及ZIF-8@壳聚糖纤维膜吸附后,罗丹明b溶液的浓度从0.1%分别下降至0.08%、0.004%以及0.008%,染料去除率分别为20%、96%、92%,即在原位生长MOFs后壳聚糖纳米纤维膜明显提高了对罗丹明b的吸附能力。Weigh 0.05g ZIF-8@chitosan fiber composite membrane, 0.05g chitosan nanofiber membrane and 1mg ZIF-8 prepared in Example 1, respectively place them in 0.1% rhodamine b-ethanol solution, and seal. After 24 hours of adsorption, 200 μL of the supernatant was added to a cuvette, and the absorbance value at 554 nm was measured by a UV-visible spectrophotometer (Figure 5), and then the concentration of rhodamine b after adsorption was calculated. Figure 6 is the color change of rhodamine b solution before and after adsorption. After testing, after adsorption of chitosan nanofiber membrane, ZIF-8 and ZIF-8@chitosan fiber membrane, the concentration of rhodamine b solution decreased from 0.1% to 0.08%, 0.004% and 0.008%, respectively. The ratios were 20%, 96%, and 92%, respectively, that is, the chitosan nanofibrous membrane significantly improved the adsorption capacity of rhodamine b after growing MOFs in situ.
实施例2Example 2
原位生长法制备ZIF-67@壳聚糖纳米纤维膜Preparation of ZIF-67@chitosan nanofiber membrane by in situ growth method
1)壳聚糖纳米纤维的制备:将壳聚糖与聚氧化乙烯分别缓慢加入到冰醋酸中得混合液,其中,混合液中冰醋酸溶液终浓度(质量浓度)为5%,壳聚糖占酸溶液质量的3%,聚氧化乙烯占酸溶液质量的1%。混合后开启磁力搅拌器,转速为700r/min,搅拌30min后固体完全溶解;溶解后将溶液在1500W的强度下超声30min后,用5mL的注射器抽取溶液进行静电纺丝,采用锡纸作为接收板,纺丝条件为:正压为5.0KV,负压为-6.0KV,推注速度为0.15mm/min,平移速度为500mm/min,接收滚筒的转速为30r/min;纺丝结束后,将锡纸取下,剪成2cm×2cm的小块,将壳聚糖纤维膜从锡纸上剥离;1) Preparation of chitosan nanofibers: Slowly add chitosan and polyoxyethylene respectively in glacial acetic acid to obtain a mixed solution, wherein the final concentration (mass concentration) of the glacial acetic acid solution in the mixed solution is 5%, and the chitosan It accounts for 3% of the mass of the acid solution, and polyethylene oxide accounts for 1% of the mass of the acid solution. After mixing, turn on the magnetic stirrer with a rotation speed of 700r/min. After stirring for 30 minutes, the solids are completely dissolved; after dissolution, the solution is ultrasonicated for 30 minutes at a strength of 1500W, and the solution is extracted with a 5mL syringe for electrospinning, and tin foil is used as a receiving plate. The spinning conditions are as follows: positive pressure is 5.0KV, negative pressure is -6.0KV, injection speed is 0.15mm/min, translational speed is 500mm/min, and the rotating speed of the receiving drum is 30r/min; Take it off, cut it into small pieces of 2cm×2cm, and peel off the chitosan fiber membrane from the tin foil;
2)Co-壳聚糖纳米纤维膜的制备:取壳聚糖纳米纤维膜0.5g与氯化钴加入到无水乙醇中,然后滴加0.05g冰醋酸。其中,氯化钴的用量为壳聚糖纤维膜质量的10倍,无水乙醇与壳聚糖纤维膜体积质量(mL/g)比700:1。体系在300r/min速度下搅拌3h,静置3h后,用无水乙醇洗涤5次,去除纤维膜表面未螯合的Co2+离子,得到Co-壳聚糖纳米纤维膜;2) Preparation of Co-chitosan nanofiber membrane: 0.5 g of chitosan nanofiber membrane and cobalt chloride were added to absolute ethanol, and then 0.05 g of glacial acetic acid was added dropwise. Wherein, the dosage of cobalt chloride is 10 times of the mass of chitosan fiber membrane, and the volume mass (mL/g) ratio of absolute ethanol to chitosan fiber membrane is 700:1. The system was stirred for 3 hours at a speed of 300 r/min, and after standing for 3 hours, it was washed 5 times with absolute ethanol to remove unchelated Co ions on the surface of the fiber membrane to obtain a Co-chitosan nanofiber membrane;
3)将Co-壳聚糖纳米纤维膜加入到氨水(氨水浓度为0.3mol/L,其与壳聚糖纤维膜体积质量(mL/g)比为1000:1)中,然后加入2-甲基咪唑(2-甲基咪唑用量为0.5g,其为壳聚糖纤维膜质量的10倍),该体系在300r/min下搅拌5h;然后用无水乙醇洗涤5遍后,在50℃下鼓风干燥30min,即可得到ZIF-67负载量为5.9%的ZIF-67@壳聚糖纳米纤维膜。3) Add the Co-chitosan nanofiber membrane to ammonia water (the concentration of ammonia water is 0.3mol/L, and the volume mass (mL/g) ratio of the chitosan fiber membrane is 1000:1), and then add 2-formazan imidazole (2-methylimidazole dosage is 0.5g, which is 10 times the mass of chitosan fiber membrane), the system was stirred at 300r/min for 5h; Blast drying for 30 minutes, the ZIF-67@chitosan nanofiber membrane with ZIF-67 loading of 5.9% can be obtained.
验证2Verification 2
ZIF-67@壳聚糖纤维膜用于孔雀石绿的吸附ZIF-67@chitosan fiber membrane for adsorption of malachite green
称取实例2中制备的0.05g ZIF-67@壳聚糖纤维膜、0.05g壳聚糖纳米纤维膜以及1mg ZIF-8,分别置于1%的孔雀石绿水溶液中,密封。缓慢搅拌,待吸附24h后,分别取上清液200μL加入比色皿中,采用紫外-可见光分光光度计法测试其在616.9nm处的吸光度值(图7),进而计算得出吸附后孔雀石绿的浓度。经过测试,ZIF-67@壳聚糖纤维膜吸附后,孔雀石绿溶液的浓度从1%下降至0.12%,去除效率为88%,二次吸附则可完全去除。由于孔雀石绿是有毒的三苯甲烷类化学物,具有高度毒性、高残留等缺点,而ZIF-67@壳聚糖纤维膜吸附这类染料的效果较好,因此,ZIF-67@壳聚糖纤维膜在水处理行业具有较大的应用前景。Weigh 0.05g ZIF-67@chitosan fiber membrane, 0.05g chitosan nanofiber membrane and 1mg ZIF-8 prepared in Example 2, respectively place them in 1% malachite green aqueous solution, and seal. Stir slowly, and after 24 hours of adsorption, take 200 μL of the supernatant and add it to a cuvette, and measure its absorbance at 616.9 nm by using a UV-visible spectrophotometer (Figure 7), and then calculate the malachite after adsorption. Concentration of green. After testing, after ZIF-67@chitosan fiber membrane is adsorbed, the concentration of malachite green solution drops from 1% to 0.12%, and the removal efficiency is 88%, which can be completely removed by secondary adsorption. Since malachite green is a toxic triphenylmethane chemical, which has the disadvantages of high toxicity and high residue, and ZIF-67@chitosan fiber membrane has a better adsorption effect on such dyes, therefore, ZIF-67@chitosan Sugar fiber membrane has a great application prospect in the water treatment industry.
实施例3Example 3
原位生长法制备HKUST-1@壳聚糖纳米纤维膜Preparation of HKUST-1@chitosan nanofiber membrane by in situ growth method
1)壳聚糖纳米纤维的制备:将壳聚糖与聚氧化乙烯分别缓慢加入到冰醋酸中得混合溶液,其中,混合溶液中冰醋酸终浓度(质量浓度)为4.5%,壳聚糖占酸溶液质量的1.5%,聚氧化乙烯占酸溶液质量的0.7%。混合后开启磁力搅拌器,转速为500r/min,搅拌30min后固体完全溶解;将溶液在700W的强度下超声30min后,用5mL的注射器抽取溶液进行静电纺丝,采用锡纸作为接收板,纺丝条件为:正压为3.0KV,负压为-9.0KV,推注速度为0.10mm/min,平移速度为400mm/min,接收滚筒的转速为10r/min;纺丝结束后,将锡纸取下,剪成2cm×2cm的小块,将壳聚糖纤维膜从锡纸上剥离;1) Preparation of chitosan nanofibers: chitosan and polyoxyethylene were slowly added respectively in glacial acetic acid to obtain a mixed solution, wherein the final concentration (mass concentration) of glacial acetic acid in the mixed solution was 4.5%, and chitosan accounted for 1.5% of the mass of the acid solution, polyethylene oxide accounts for 0.7% of the mass of the acid solution. After mixing, turn on the magnetic stirrer with a rotation speed of 500r/min. After stirring for 30min, the solids are completely dissolved; after the solution is ultrasonicated for 30min at a strength of 700W, the solution is extracted with a 5mL syringe for electrospinning, using tin foil as a receiving plate, and spinning The conditions are: the positive pressure is 3.0KV, the negative pressure is -9.0KV, the injection speed is 0.10mm/min, the translational speed is 400mm/min, the speed of the receiving drum is 10r/min; after the spinning is finished, remove the tin foil , cut into small pieces of 2cm×2cm, and peel off the chitosan fiber membrane from the tin foil;
2)Cu-壳聚糖纳米纤维膜的制备:取壳聚糖纳米纤维膜0.4g与无水醋酸铜加入到无水乙醇中,然后滴加1g冰醋酸。其中,无水醋酸铜的用量为壳聚糖纤维膜质量的8倍,无水乙醇与壳聚糖纤维膜体积质量(mL/g)比为500:1。体系在500r/min速度下搅拌2.5h,静置2h后,用甲醇洗涤5次,去除纤维表面未螯合的Cu2+离子,得到Cu-壳聚糖纳米纤维膜;2) Preparation of Cu-chitosan nanofiber membrane: 0.4 g of chitosan nanofiber membrane and anhydrous copper acetate were added to absolute ethanol, and then 1 g of glacial acetic acid was added dropwise. Among them, the dosage of anhydrous copper acetate is 8 times of the mass of chitosan fiber membrane, and the volume mass (mL/g) ratio of absolute ethanol to chitosan fiber membrane is 500:1. The system was stirred at a speed of 500r/min for 2.5h, and after standing for 2h, it was washed 5 times with methanol to remove unchelated Cu 2+ ions on the fiber surface to obtain a Cu-chitosan nanofiber membrane;
3)将Cu-壳聚糖纳米纤维膜加入到氨水(氨水浓度为0.11mol/L,其与壳聚糖纤维膜体积质量(mL/g)比为700:1)中,然后加入均苯三酸(均苯三酸用量为0.2g,其用量为壳聚糖纤维膜质量的4倍);体系在200r/min下搅拌2h;然后用甲醇洗涤5遍后,在40℃下鼓风干燥10min,即可得到负载量为6.2%的HKUST-1@壳聚糖纳米纤维膜。3) Add the Cu-chitosan nanofiber membrane to ammonia water (the concentration of ammonia water is 0.11mol/L, and the volume mass (mL/g) ratio of it to chitosan fiber membrane is 700:1), and then add trimesis acid (the amount of trimesic acid is 0.2g, which is 4 times the mass of the chitosan fiber membrane); the system was stirred at 200r/min for 2h; after washing with methanol for 5 times, it was air-dried at 40°C for 10min , the HKUST-1@chitosan nanofiber membrane with a loading of 6.2% can be obtained.
将上述获得的HKUST-1@壳聚糖纳米纤维膜对苏丹红(初始浓度2%)进行吸附,经HKUST-1@壳聚糖纳米纤维膜吸附后苏丹红的去除效率为74%,经二次吸附则可以完全去除。The HKUST-1@chitosan nanofiber membrane obtained above was adsorbed on Sudan Red (initial concentration 2%), and the removal efficiency of Sudan Red after adsorption by HKUST-1@chitosan nanofiber membrane was 74%. Secondary adsorption can be completely removed.
实施例4Example 4
原位生长法制备MIL-101(Cr)@壳聚糖纳米纤维膜Preparation of MIL-101(Cr)@chitosan nanofiber membrane by in situ growth method
1)壳聚糖纳米纤维的制备:将壳聚糖与聚氧化乙烯分别缓慢加入到冰醋酸中得混合溶液,其中,混合液中冰醋酸溶液终浓度(质量浓度)为4%,壳聚糖占酸溶液质量的2%,聚氧化乙烯占酸溶液质量的0.5%。开启磁力搅拌器,转速为400r/min,搅拌30min后固体完全溶解;将溶液在700W的强度下超声30min后,用5mL的注射器抽取溶液进行静电纺丝,采用锡纸作为接收板,纺丝条件为:正压为10.0KV,负压为-8.0KV,推注速度为0.08mm/min,平移速度为400mm/min,接收滚筒的转速为25r/min;纺丝结束后,将锡纸取下,剪成2cm×2cm的小块,将壳聚糖纤维膜从锡纸上剥离;1) Preparation of chitosan nanofibers: Slowly add chitosan and polyoxyethylene respectively in glacial acetic acid to obtain a mixed solution, wherein the final concentration (mass concentration) of the glacial acetic acid solution in the mixed solution is 4%, and the chitosan Accounting for 2% of the mass of the acid solution, polyethylene oxide accounts for 0.5% of the mass of the acid solution. Turn on the magnetic stirrer with a rotation speed of 400r/min. After stirring for 30min, the solids are completely dissolved; after ultrasonicating the solution for 30min at a strength of 700W, extract the solution with a 5mL syringe for electrospinning, using tin foil as the receiving plate, and the spinning conditions are: : The positive pressure is 10.0KV, the negative pressure is -8.0KV, the injection speed is 0.08mm/min, the translational speed is 400mm/min, and the rotating speed of the receiving drum is 25r/min; into small pieces of 2cm × 2cm, and the chitosan fiber membrane is peeled off from the tin foil;
2)Cr-壳聚糖纳米纤维膜的制备:取壳聚糖纳米纤维膜与硝酸铬0.25g加入到甲醇中,然后滴加1g冰醋酸。其中,硝酸铬的用量为壳聚糖纤维膜质量的5倍,甲醇与壳聚糖纤维膜体积质量(mL/g)比为600:1。体系在200r/min速度下搅拌1.5h,静置1h后,用甲醇洗涤3次,去除纤维膜表面未螯合的Cr2+离子,得到Cr-壳聚糖纳米纤维膜;2) Preparation of Cr-chitosan nanofiber membrane: take chitosan nanofiber membrane and 0.25 g of chromium nitrate and add them to methanol, then add 1 g of glacial acetic acid dropwise. Among them, the dosage of chromium nitrate is 5 times of the mass of chitosan fiber membrane, and the volume mass (mL/g) ratio of methanol to chitosan fiber membrane is 600:1. The system was stirred at a speed of 200r/min for 1.5h, and after standing for 1h, it was washed 3 times with methanol to remove unchelated Cr ions on the surface of the fiber membrane to obtain a Cr-chitosan nanofiber membrane;
3)将Cr-壳聚糖纳米纤维膜加入到氨水(氨水浓度0.05mol/L,其与壳聚糖纤维膜体积质量(mL/g)比为1000:1)中,然后加入对苯二甲酸(对苯二甲酸为0.4g),其用量为壳聚糖纤维膜质量的8倍,该体系在100r/min下搅拌1.5h;然后用甲醇洗涤5遍后,在30℃下鼓风干燥10min,即可得到表面生长MIL-101(Cr)的壳聚糖纳米纤维膜。3) Add the Cr-chitosan nanofiber membrane to ammonia water (the concentration of ammonia water is 0.05mol/L, and the volume mass (mL/g) ratio of the chitosan fiber membrane is 1000:1), and then add terephthalic acid (0.4g of terephthalic acid), its consumption is 8 times of chitosan fiber film quality, this system is stirred 1.5h under 100r/min; After washing 5 times with methanol, blow dry 10min at 30 ℃ , the chitosan nanofiber membrane with MIL-101(Cr) grown on the surface can be obtained.
将上述获得的负载量为8.9%的MIL-101(Cr)@壳聚糖纳米纤维膜对亚甲基蓝(初始浓度1%)进行吸附,经MIL-101(Cr)@壳聚糖纳米纤维膜吸附后亚甲基蓝的去除效率为90.1%。The MIL-101(Cr)@chitosan nanofiber membrane with a load of 8.9% obtained above was adsorbed on methylene blue (initial concentration 1%), and after being adsorbed by MIL-101(Cr)@chitosan nanofiber membrane The removal efficiency of methylene blue was 90.1%.
实施例5Example 5
原位生长法制备UiO-66-NH2@壳聚糖纳米纤维膜Preparation of UiO-66-NH 2 @chitosan nanofibrous membrane by in situ growth method
1)壳聚糖纳米纤维的制备:将壳聚糖与聚氧化乙烯分别缓慢加入到冰醋酸中得混合溶液,其中,混合溶液中冰醋酸溶液终浓度(质量浓度)为3.5%,壳聚糖占酸溶液质量的1.5%,聚氧化乙烯占酸溶液质量的0.9%。开启磁力搅拌器,转速为700r/min,搅拌30min后固体完全溶解;将溶液在700W的强度下超声30min后,用5mL的注射器抽取溶液进行静电纺丝,采用锡纸作为接收板,纺丝条件为:正压为10.0KV,负压为-8.0KV,推注速度为0.08mm/min,平移速度为400mm/min,接收滚筒的转速为15r/min;纺丝结束后,将锡纸取下,剪成2cm×2cm的小块,将壳聚糖纤维膜从锡纸上剥离;1) Preparation of chitosan nanofibers: Slowly add chitosan and polyoxyethylene respectively in glacial acetic acid to obtain a mixed solution, wherein the final concentration (mass concentration) of the glacial acetic acid solution in the mixed solution is 3.5%, and the chitosan Accounting for 1.5% of the mass of the acid solution, polyethylene oxide accounts for 0.9% of the mass of the acid solution. Turn on the magnetic stirrer with a rotation speed of 700r/min. After stirring for 30min, the solids are completely dissolved; after ultrasonicating the solution for 30min at a strength of 700W, extract the solution with a 5mL syringe for electrospinning, using tin foil as the receiving plate, and the spinning conditions are: : The positive pressure is 10.0KV, the negative pressure is -8.0KV, the injection speed is 0.08mm/min, the translational speed is 400mm/min, and the rotating speed of the receiving drum is 15r/min; into small pieces of 2cm × 2cm, and the chitosan fiber membrane is peeled off from the tin foil;
2)Zr-壳聚糖纳米纤维膜的制备:取壳聚糖纳米纤维膜与四氯化锆0.3g加入到甲醇中,然后滴加1g冰醋酸。其中,四氯化锆的用量为壳聚糖纤维膜质量的6倍,甲醇与壳聚糖纤维膜体积质量(mL/g)比为550:1。在300r/min速度下搅拌3h,静置3h后,用无水乙醇洗涤5次,去除纤维膜表面未螯合的Zr4+离子,得到Zr-壳聚糖纳米纤维膜;2) Preparation of Zr-chitosan nanofiber membrane: take chitosan nanofiber membrane and 0.3 g of zirconium tetrachloride and add them to methanol, then add 1 g of glacial acetic acid dropwise. Among them, the dosage of zirconium tetrachloride is 6 times of the mass of chitosan fiber membrane, and the ratio of methanol to chitosan fiber membrane volume mass (mL/g) is 550:1. Stir at 300r/min speed for 3h, after standing for 3h, wash 5 times with dehydrated alcohol, remove the unchelated Zr ions on the fiber membrane surface, obtain Zr-chitosan nanofibrous membrane;
3)将Zr-壳聚糖纳米纤维膜加入到氨水(氨水浓度0.3mol/L,其与壳聚糖纤维膜体积质量(mL/g)比为900:1)中,然后加入2-氨基对苯二甲酸0.35g,其用量为壳聚糖纤维膜质量的7倍,该体系在300r/min下搅拌3h;然后用无水乙醇洗涤5遍后,在50℃下鼓风干燥30min,即可得到表面生长UiO-66-NH2的壳聚糖纳米纤维膜(负载量为7.8%)。经过验证,UiO-66-NH2-壳聚糖纳米纤维膜对亚甲基橙(初始浓度1.5%)的去除效率为82%,二次吸附则可以完全去除。3) Add the Zr-chitosan nanofiber membrane to ammonia water (the concentration of ammonia water is 0.3mol/L, and the volume mass (mL/g) ratio of the chitosan fiber membrane is 900:1), and then add 2-amino p- 0.35g of phthalic acid, the amount of which is 7 times the quality of the chitosan fiber membrane, the system was stirred at 300r/min for 3h; then washed with absolute ethanol for 5 times, and then air-dried at 50°C for 30min. A chitosan nanofibrous membrane (loaded at 7.8%) with UiO-66-NH 2 grown on the surface was obtained. It has been verified that the removal efficiency of the UiO-66-NH 2 -chitosan nanofiber membrane for methylene orange (initial concentration 1.5%) is 82%, and can be completely removed by secondary adsorption.
实施例6Example 6
原位生长法制备MOFs-74(Ni)@壳聚糖纳米纤维膜Preparation of MOFs-74(Ni)@chitosan nanofibrous membrane by in situ growth method
1)壳聚糖纳米纤维的制备:将壳聚糖与聚氧化乙烯分别缓慢加入到冰醋酸中得混合液,其中,混合液中冰醋酸溶液终浓度(质量浓度)为10%,壳聚糖占酸溶液质量的5%,聚氧化乙烯占酸溶液质量的10%。开启磁力搅拌器,转速为550r/min,搅拌30min后固体完全溶解;将溶液在700W的强度下超声30min后,用5mL的注射器抽取溶液进行静电纺丝,采用锡纸作为接收板,纺丝条件为:正压为13.0KV,负压为-10.0KV,推注速度为0.15mm/min,平移速度为500mm/min,接收滚筒的转速为5r/min;纺丝结束后,将锡纸取下,剪成2cm×2cm的小块,将壳聚糖纤维膜从锡纸上剥离;1) Preparation of chitosan nanofibers: Slowly add chitosan and polyoxyethylene respectively in glacial acetic acid to obtain a mixed solution, wherein the final concentration (mass concentration) of the glacial acetic acid solution in the mixed solution is 10%, and the chitosan It accounts for 5% of the mass of the acid solution, and polyethylene oxide accounts for 10% of the mass of the acid solution. Turn on the magnetic stirrer at a speed of 550r/min, and stir for 30 minutes to dissolve the solid completely; after ultrasonicating the solution for 30 minutes at a strength of 700W, use a 5mL syringe to extract the solution for electrospinning, using tin foil as the receiving plate, and the spinning conditions are: : The positive pressure is 13.0KV, the negative pressure is -10.0KV, the injection speed is 0.15mm/min, the translation speed is 500mm/min, and the rotating speed of the receiving drum is 5r/min; after spinning, remove the tin foil, cut into small pieces of 2cm × 2cm, and the chitosan fiber membrane is peeled off from the tin foil;
2)MOFs-74(Ni)-壳聚糖纳米纤维膜的制备:取壳聚糖纳米纤维膜与氯化镍0.5g加入到无水乙醇中,然后滴加1g冰醋酸。其中,氯化镍的用量为壳聚糖纤维膜质量的10倍,无水乙醇与壳聚糖纤维膜体积质量(mL/g)比为1000:1。体系在100r/min速度下搅拌0.5h,静置1h后,用甲醇洗涤3次,去除纤维表面未螯合的Ni2+离子,得到Ni-壳聚糖纳米纤维膜;2) Preparation of MOFs-74(Ni)-chitosan nanofiber membrane: take chitosan nanofiber membrane and nickel chloride 0.5 g and add them to absolute ethanol, then add 1 g of glacial acetic acid dropwise. Wherein, the dosage of nickel chloride is 10 times of the mass of chitosan fiber membrane, and the volume mass (mL/g) ratio of absolute ethanol to chitosan fiber membrane is 1000:1. The system was stirred at a speed of 100r/min for 0.5h, and after standing for 1h, it was washed 3 times with methanol to remove unchelated Ni 2+ ions on the fiber surface to obtain a Ni-chitosan nanofiber membrane;
3)将Ni-壳聚糖纳米纤维膜加入到氨水(氨水浓度0.05mol/L,其与壳聚糖纤维膜体积质量(mL/g)比为2000:1)中,然后加入对苯二甲酸1g,其用量为壳聚糖纤维膜质量的20倍,该体系在100r/min下搅拌1h;然后用甲醇洗涤3遍后,在30℃下鼓风干燥5min,即可得到表面生长MOFs-74(Ni)的壳聚糖纳米纤维膜(负载量为2.9%)。3) Add the Ni-chitosan nanofiber membrane to ammonia water (the concentration of ammonia water is 0.05mol/L, and the volume mass (mL/g) ratio of the chitosan fiber membrane is 2000:1), and then add terephthalic acid 1g, the amount of which is 20 times the mass of chitosan fiber membrane, the system was stirred at 100r/min for 1h; then washed with methanol for 3 times, and air-dried at 30°C for 5min to obtain surface-grown MOFs-74 (Ni) chitosan nanofiber membrane (2.9% loading).
将上述所得MOFs-74(Ni)@壳聚糖纳米纤维膜对罗丹明b(初始浓度1.2%)进行吸附,经膜吸附后的去除效率为32.4%。The MOFs-74(Ni)@chitosan nanofiber membrane obtained above was adsorbed on rhodamine b (initial concentration 1.2%), and the removal efficiency after membrane adsorption was 32.4%.
综合上述实例,本发明基于静电纺丝获得壳聚糖的纳米纤维膜,采用原位生长法成功制备了MOFs@壳聚糖纳米纤维膜,实例证明了该膜对水或有机溶剂中的染料具有较好的吸附作用,吸附能力与MOFs材料相当,去除率最高可达92%。因此,该膜在染料废水处理中具有广阔的应用前景。Based on the above examples, the present invention obtains chitosan nanofiber membranes based on electrospinning, and successfully prepares MOFs@chitosan nanofiber membranes by using the in-situ growth method. Examples have proved that the membranes are effective against dyes in water or organic solvents. Better adsorption, the adsorption capacity is equivalent to that of MOFs materials, and the removal rate can reach up to 92%. Therefore, the membrane has broad application prospects in dye wastewater treatment.
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