CN105603637A - Efficient electrostatic spinning oil-water separation fiber membrane - Google Patents
Efficient electrostatic spinning oil-water separation fiber membrane Download PDFInfo
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- CN105603637A CN105603637A CN201610040433.9A CN201610040433A CN105603637A CN 105603637 A CN105603637 A CN 105603637A CN 201610040433 A CN201610040433 A CN 201610040433A CN 105603637 A CN105603637 A CN 105603637A
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- 239000012528 membrane Substances 0.000 title claims abstract description 66
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 239000000835 fiber Substances 0.000 title claims abstract description 20
- 238000010041 electrostatic spinning Methods 0.000 title claims abstract 10
- 238000000926 separation method Methods 0.000 title abstract description 48
- 229920002301 cellulose acetate Polymers 0.000 claims abstract description 36
- 239000004642 Polyimide Substances 0.000 claims abstract description 34
- 229920001721 polyimide Polymers 0.000 claims abstract description 34
- 239000002121 nanofiber Substances 0.000 claims abstract description 27
- 238000001523 electrospinning Methods 0.000 claims abstract description 22
- 238000002360 preparation method Methods 0.000 claims abstract description 21
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229920005575 poly(amic acid) Polymers 0.000 claims abstract description 17
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 12
- 238000002474 experimental method Methods 0.000 claims abstract description 11
- CMLFRMDBDNHMRA-UHFFFAOYSA-N 2h-1,2-benzoxazine Chemical compound C1=CC=C2C=CNOC2=C1 CMLFRMDBDNHMRA-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000000178 monomer Substances 0.000 claims abstract description 10
- 238000011065 in-situ storage Methods 0.000 claims abstract description 8
- 239000002105 nanoparticle Substances 0.000 claims abstract description 6
- 239000000243 solution Substances 0.000 claims description 26
- DKPFZGUDAPQIHT-UHFFFAOYSA-N Butyl acetate Natural products CCCCOC(C)=O DKPFZGUDAPQIHT-UHFFFAOYSA-N 0.000 claims description 12
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 claims description 12
- 239000011259 mixed solution Substances 0.000 claims description 12
- 235000019198 oils Nutrition 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 10
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 8
- 238000012360 testing method Methods 0.000 claims description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 230000005686 electrostatic field Effects 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- 238000009987 spinning Methods 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
- CBCKQZAAMUWICA-UHFFFAOYSA-N 1,4-phenylenediamine Chemical compound NC1=CC=C(N)C=C1 CBCKQZAAMUWICA-UHFFFAOYSA-N 0.000 claims description 4
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 4
- 229910052731 fluorine Inorganic materials 0.000 claims description 4
- 239000011737 fluorine Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 3
- 238000005520 cutting process Methods 0.000 claims description 3
- 239000000376 reactant Substances 0.000 claims description 3
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 claims description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 2
- 229930040373 Paraformaldehyde Natural products 0.000 claims description 2
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims description 2
- 229960000907 methylthioninium chloride Drugs 0.000 claims description 2
- 235000019476 oil-water mixture Nutrition 0.000 claims description 2
- 229920002866 paraformaldehyde Polymers 0.000 claims description 2
- 239000003921 oil Substances 0.000 claims 17
- 229910052681 coesite Inorganic materials 0.000 claims 5
- 229910052906 cristobalite Inorganic materials 0.000 claims 5
- 229910052682 stishovite Inorganic materials 0.000 claims 5
- 229910052905 tridymite Inorganic materials 0.000 claims 5
- PXKLMJQFEQBVLD-UHFFFAOYSA-N Bisphenol F Natural products C1=CC(O)=CC=C1CC1=CC=C(O)C=C1 PXKLMJQFEQBVLD-UHFFFAOYSA-N 0.000 claims 2
- 239000004952 Polyamide Substances 0.000 claims 2
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 claims 2
- 230000018044 dehydration Effects 0.000 claims 2
- 238000006297 dehydration reaction Methods 0.000 claims 2
- 150000002466 imines Chemical class 0.000 claims 2
- 238000007654 immersion Methods 0.000 claims 2
- 239000006101 laboratory sample Substances 0.000 claims 2
- 238000002156 mixing Methods 0.000 claims 2
- 229920002647 polyamide Polymers 0.000 claims 2
- 235000012239 silicon dioxide Nutrition 0.000 claims 2
- 230000002194 synthesizing effect Effects 0.000 claims 2
- 238000013019 agitation Methods 0.000 claims 1
- WKDNYTOXBCRNPV-UHFFFAOYSA-N bpda Chemical compound C1=C2C(=O)OC(=O)C2=CC(C=2C=C3C(=O)OC(C3=CC=2)=O)=C1 WKDNYTOXBCRNPV-UHFFFAOYSA-N 0.000 claims 1
- LLDLZZVYXXUTJN-UHFFFAOYSA-N bromobenzene hydrate Chemical compound O.Brc1ccccc1 LLDLZZVYXXUTJN-UHFFFAOYSA-N 0.000 claims 1
- FIMJSWFMQJGVAM-UHFFFAOYSA-N chloroform;hydrate Chemical compound O.ClC(Cl)Cl FIMJSWFMQJGVAM-UHFFFAOYSA-N 0.000 claims 1
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 claims 1
- 239000000975 dye Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 239000012466 permeate Substances 0.000 claims 1
- 238000010186 staining Methods 0.000 claims 1
- 125000006158 tetracarboxylic acid group Chemical group 0.000 claims 1
- PRDUHXPVDHDGKN-UHFFFAOYSA-N tetrachloromethane;hydrate Chemical compound O.ClC(Cl)(Cl)Cl PRDUHXPVDHDGKN-UHFFFAOYSA-N 0.000 claims 1
- 238000001291 vacuum drying Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 3
- 239000010865 sewage Substances 0.000 abstract description 2
- 238000012986 modification Methods 0.000 abstract 1
- 230000004048 modification Effects 0.000 abstract 1
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 9
- 229910004298 SiO 2 Inorganic materials 0.000 description 9
- 230000003075 superhydrophobic effect Effects 0.000 description 8
- 238000010586 diagram Methods 0.000 description 5
- 239000003513 alkali Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004154 testing of material Methods 0.000 description 2
- JVERADGGGBYHNP-UHFFFAOYSA-N 5-phenylbenzene-1,2,3,4-tetracarboxylic acid Chemical compound OC(=O)C1=C(C(O)=O)C(C(=O)O)=CC(C=2C=CC=CC=2)=C1C(O)=O JVERADGGGBYHNP-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- ZFVMWEVVKGLCIJ-UHFFFAOYSA-N bisphenol AF Chemical compound C1=CC(O)=CC=C1C(C(F)(F)F)(C(F)(F)F)C1=CC=C(O)C=C1 ZFVMWEVVKGLCIJ-UHFFFAOYSA-N 0.000 description 1
- BRDOFYPYQFDHOQ-UHFFFAOYSA-N butyl acetate;hexanoic acid Chemical compound CCCCCC(O)=O.CCCCOC(C)=O BRDOFYPYQFDHOQ-UHFFFAOYSA-N 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 229940050176 methyl chloride Drugs 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920001610 polycaprolactone Polymers 0.000 description 1
- 239000004632 polycaprolactone Substances 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Classifications
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
- D04H1/42—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
- D04H1/425—Cellulose series
- D04H1/4258—Regenerated cellulose series
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
-
- 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
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/0007—Electro-spinning
- D01D5/0015—Electro-spinning characterised by the initial state of the material
- D01D5/003—Electro-spinning characterised by the initial state of the material the material being a polymer solution or dispersion
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
- D04H1/42—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
- D04H1/4326—Condensation or reaction polymers
- D04H1/4334—Polyamides
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
- D04H1/42—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
- D04H1/4382—Stretched reticular film fibres; Composite fibres; Mixed fibres; Ultrafine fibres; Fibres for artificial leather
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/70—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres characterised by the method of forming fleeces or layers, e.g. reorientation of fibres
- D04H1/72—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres characterised by the method of forming fleeces or layers, e.g. reorientation of fibres the fibres being randomly arranged
- D04H1/728—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres characterised by the method of forming fleeces or layers, e.g. reorientation of fibres the fibres being randomly arranged by electro-spinning
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Analytical Chemistry (AREA)
- Physics & Mathematics (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Thermal Sciences (AREA)
- Dispersion Chemistry (AREA)
- Mechanical Engineering (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Artificial Filaments (AREA)
Abstract
Description
技术领域technical field
本发明涉及的是一种高效的静电纺丝油水分离纤维膜的制备方法,特别是一种用于重力驱使油水分离的高效的超疏水和超亲油静电纺丝油水分离纤维膜的制备方法。The invention relates to a method for preparing an efficient electrospinning oil-water separation fiber membrane, in particular a method for preparing an efficient superhydrophobic and super-oleophilic electrospinning oil-water separation fiber membrane for gravity-driven oil-water separation.
背景技术Background technique
通过静电纺丝,已经报道出了许多关于纳米纤维膜的文献例如聚苯乙烯,聚己内酯,聚甲基丙烯酸甲酯,聚氨酯以及无机二氧化硅纤维等。但这些纤维都存在分离速度慢、分离效率低、稳定性差、强度差、容易产生二次污染的缺点。而且分离速度慢、分离效率低,强度差这一最大的障碍,严重限制了它们在实际中的应用。By electrospinning, many literatures on nanofibrous membranes such as polystyrene, polycaprolactone, polymethyl methacrylate, polyurethane, and inorganic silica fibers have been reported. However, these fibers have the disadvantages of slow separation speed, low separation efficiency, poor stability, poor strength, and easy to produce secondary pollution. Moreover, the biggest obstacle of slow separation speed, low separation efficiency and poor strength seriously limits their practical application.
发明内容Contents of the invention
本发明提出的是一种用于重力驱使油水分离的高效的超疏水和超亲油静电纺丝油水分离纤维膜的制备方法,其目的旨在克服现有技术所存有的上述缺陷,采用CA和PAA为原料,通过高压同轴静电纺丝技术以高分子量的聚PAA为芯,CA为壳,在经过程序升温对PAA进行亚胺化得到具有生物可降解性、成本低廉、显著的分离通量、分离效率和机械强度的CA-PI纳米纤维膜;通过对纤维膜表面修饰,得到功能性的纤维膜材料;而且,这种高效的超疏水超亲油膜材料在油水分离、污水处理以及深海石油泄漏中具有广阔的应用前景。The present invention proposes a method for preparing an efficient superhydrophobic and superoleophilic electrospun oil-water separation fiber membrane for gravity-driven oil-water separation. Its purpose is to overcome the above-mentioned defects in the prior art. CA and PAA is used as the raw material, and high-molecular-weight poly-PAA is used as the core through high-pressure coaxial electrospinning technology, and CA is used as the shell, and PAA is imidized after temperature programming to obtain biodegradable, low-cost, and significant separation flux. CA-PI nanofiber membranes with high separation efficiency and mechanical strength; functional fiber membrane materials are obtained by modifying the surface of fiber membranes; moreover, this highly efficient super-hydrophobic and super-oleophilic membrane material is used in oil-water separation, sewage treatment and deep-sea petroleum It has broad application prospects in leakage.
本发明的技术解决方案:高效的超疏水和超亲油油水分离纳米纤维膜的制备方法,包括如下工艺步骤:Technical solution of the present invention: the preparation method of highly efficient superhydrophobic and superoleophilic oil-water separation nanofibrous membrane comprises the following process steps:
(1)合成聚酰胺酸(PAA)(1) Synthetic polyamic acid (PAA)
(2)电纺PAA纳米纤维膜以及亚胺化为聚酰亚胺(PI)膜;(2) Electrospun PAA nanofiber membrane and imidization into polyimide (PI) membrane;
(3)制备醋酸纤维素(CA)纳米纤维膜;(3) preparing cellulose acetate (CA) nanofiber membrane;
(4)同轴电纺CA-PAA并亚胺化为CA-PI;(4) Coaxial electrospinning of CA-PAA and imidization into CA-PI;
(5)合成苯并噁嗪单体(BAF-tfa);(5) Synthesis of benzoxazine monomer (BAF-tfa);
(6)BAF-tfa以及BAF-tfa/二氧化硅纳米粒子(SiO2NPs)原位固化CA、PI、CA-PI纳米纤维膜;(6) BAF-tfa and BAF-tfa/silica nanoparticles (SiO 2 NPs) in situ curing CA, PI, CA-PI nanofibrous membranes;
(7)接触角实验(7) Contact angle experiment
(8)油水分离实验。(8) Oil-water separation experiment.
本发明的积极效果Positive effect of the present invention
a.具有高的分离流量和分离效率,流量达到2270Lm-2h-1,分离效率达到99%以上,相比市场上买的油水分离膜流量提高了3-4倍,也具有更高的分离效率。a. It has high separation flow rate and separation efficiency, the flow rate reaches 2270Lm -2 h -1 , and the separation efficiency reaches over 99%. Compared with the oil-water separation membrane bought in the market, the flow rate is increased by 3-4 times, and it also has higher separation efficiency efficiency.
b.具有高的强度,拉伸强度达到200MPa以上,相比常用的CA纳米纤维膜的拉伸强度6.65MPa,提高了30多倍;b. It has high strength, the tensile strength reaches more than 200MPa, which is more than 30 times higher than the commonly used CA nanofiber membrane's tensile strength of 6.65MPa;
c.只经过BAF-tfa改性的CA-PI纳米纤维膜与水的最大接触角只能达到137°,并不具有超疏水和超亲油的性质;而经过BAF-tfa改性后CA-PI纳米纤维膜与水的最大接触角可达161°,油的接触角可达到0°,具有超疏水和超亲油的性质,可用于油水分离过程。c. The maximum contact angle of CA-PI nanofiber membranes modified by BAF-tfa with water can only reach 137°, which does not have superhydrophobic and superoleophilic properties; while CA-PI modified by BAF-tfa The maximum contact angle of PI nanofiber membrane with water can reach 161°, and the contact angle of oil can reach 0°. It has super hydrophobic and super lipophilic properties and can be used in oil-water separation process.
d.具有耐酸碱、耐高温的性质,在不同的pH、和高温下仍旧能够保持超疏水的性质。d. It has the properties of acid and alkali resistance and high temperature resistance, and can still maintain superhydrophobic properties under different pH and high temperature.
e.具有可持久使用性,存放300天后,接触角下降低于5%,经过十次循环使用,流量仍旧能够达到2000Lm-2h-1左右,分离效率达到98.5%。e. It can be used for a long time. After 300 days of storage, the contact angle drops below 5%. After ten cycles of use, the flow rate can still reach about 2000Lm -2 h -1 and the separation efficiency can reach 98.5%.
附图说明Description of drawings
图1是电纺PAA纳米纤维膜装置的结构示意图。Figure 1 is a schematic diagram of the structure of the electrospun PAA nanofiber membrane device.
图2是同轴电纺CA-PI纳米纤维膜的过程示意图。Figure 2 is a schematic diagram of the process of coaxial electrospinning CA-PI nanofibrous membranes.
图3是在室温下放置300天F-PBZ-1/PI和F-PBZ-1/CA-PI与水的接触角变化图。Fig. 3 is a graph showing the change of contact angle between F-PBZ-1/PI and F-PBZ-1/CA-PI and water after 300 days at room temperature.
图4是不同pH和温度下,F-PBZ-1/SNP-4/CA-PI与水的接触角变化图.Fig. 4 is a diagram of the contact angle variation between F-PBZ-1/SNP-4/CA-PI and water at different pH and temperature.
图5是不同浓度的BAF-tfa以及BAF-tfa/SiO2NPs原位固化后CA、PI、CA-PI流量和分离效率图。Fig. 5 is a graph of CA, PI, CA-PI flux and separation efficiency after in-situ curing of different concentrations of BAF-tfa and BAF-tfa/SiO 2 NPs.
图6是不同种类的油水混合物流量和分离效率图;循环使用10次F-PBZ-1/SNP-4/CA-PI流量和分离效率变化图以及BAF-tfa/SiO2NPs原位固化不同厚度的CA-PI后的流量和分离效率图。Figure 6 is a diagram of the flow and separation efficiency of different types of oil-water mixtures; 10 cycles of F-PBZ-1/SNP-4/CA-PI flow and separation efficiency changes and BAF-tfa/SiO 2 NPs in-situ solidification with different thicknesses Flow and separation efficiency graphs after CA-PI.
图7是不同厚度的CA-PI的孔隙率变化图。Fig. 7 is a diagram of porosity variation of CA-PI with different thicknesses.
具体实施方式detailed description
高效的超疏水和超亲油油水分离纳米纤维膜的制备方法的制备方法,包括如下工艺步骤:The preparation method of the preparation method of the efficient superhydrophobic and superoleophilic oil-water separation nanofiber membrane comprises the following process steps:
(1)合成PAA;(1) synthesis of PAA;
在装有机械搅拌器、温度计、氮气导出入管的干燥四口烧瓶中加入联苯四甲酸二酐(BPDA)和对苯二胺(PDA)分别2.9422和1.0814g(摩尔比1∶1)混合均匀;在强烈的机械搅拌下,加入40mlDMAc,在-15℃-5℃下反应24h小时后,随后结束反应,得到PAA。Add biphenyltetracarboxylic dianhydride (BPDA) and p-phenylenediamine (PDA) respectively 2.9422g and 1.0814g (molar ratio 1:1) into a dry four-necked flask equipped with a mechanical stirrer, a thermometer, and a nitrogen gas inlet and outlet tube, and mix well ; Under strong mechanical stirring, add 40ml of DMAc, react at -15°C-5°C for 24 hours, and then terminate the reaction to obtain PAA.
(2)电纺PAA纳米纤维膜以及亚胺化为聚酰亚胺(PI)膜:(2) Electrospun PAA nanofiber membrane and imidization into polyimide (PI) membrane:
用1-5%(wt)PAA的DMAc溶液,在电压为30Kv(+20,-10KV)的高压静电场中纺丝,注射器针尖到飞轮的接收距离为10-15cm,飞轮的转速为1000-2000转/min,电纺的速度为0.5-1ml/h,纺丝成聚酰胺酸(PAA)纳米纤维膜,如图1所示。将电纺好的PAA纳米纤维膜按照程序升温150℃/1h,200℃/1h,250℃/1h,300℃/1h,350℃/30mim的方法在管式炉中进行亚胺化得到PI膜;之后用深圳新三思的万能材料试验机(CMT-8500型)对PI膜的应力一应变在室温下进行测试,测试其应力-应变。Use 1-5% (wt) PAA DMAc solution to spin in a high-voltage electrostatic field with a voltage of 30Kv (+20, -10KV), the receiving distance from the needle tip of the syringe to the flywheel is 10-15cm, and the speed of the flywheel is 1000- 2000 revolutions/min, the speed of electrospinning is 0.5-1ml/h, and the polyamic acid (PAA) nanofiber membrane is spun into, as shown in Figure 1. The electrospun PAA nanofiber membrane was imidized in a tube furnace according to the temperature program of 150°C/1h, 200°C/1h, 250°C/1h, 300°C/1h, 350°C/30mim to obtain a PI film Afterwards, the stress-strain of the PI film was tested at room temperature with the universal material testing machine (CMT-8500 type) of Shenzhen Xinsansi, and the stress-strain was tested.
(3)CA纳米纤维膜的制备,(3) Preparation of CA nanofiber membrane,
CA纳米纤维膜的制备:用5-10%(wt)的二氯甲烷与丙酮(2/1(V/V))的混合溶液,在高压静电场中纺丝,注射器针尖到滚筒的距离为10-15cm,电纺速度为0.5-1ml/h,纺丝成CA纳米纤维膜,电纺装置同电纺PAA膜的装置,得到的纳米纤维膜用深圳新三思的万能材料试验机(CMT-8500型)在室温下进行测试应力-应变。The preparation of CA nanofiber film: with the mixed solution of the dichloromethane of 5-10% (wt) and acetone (2/1 (V/V)), spinning in the high-voltage electrostatic field, the distance from the needle point of the syringe to the cylinder is 10-15cm, the electrospinning speed is 0.5-1ml/h, and it is spun into CA nanofiber membrane. The electrospinning device is the same as that of electrospinning PAA membrane. Model 8500) for stress-strain testing at room temperature.
(4)同轴电纺CA-PAA并亚胺化为CA-PI:(4) Coaxial electrospinning of CA-PAA and imidization into CA-PI:
同轴CA-PAA纳米纤维膜的制备:是在传统的电纺装置的基础上采用同轴的针头,1-5%(wt)PAA的DMAc溶液作为芯,5-10%(wt)的二氯甲烷与丙酮2∶1(V/V)的混合溶液作为壳,在高压静电场中纺丝,高速旋转地飞轮进行接收CA-PAA纳米纤维。将电纺好的CA-PAA纳米纤维膜按照程序升温150℃/2h,200/3h,250℃/1h,260℃/1h的方法进行亚胺化得到CA-PI纳米纤维膜;得到的纳米纤维膜采用深圳新三思的万能材料试验机(CMT-8500型)在室温下进行测试应力一应变。如图2所示。The preparation of coaxial CA-PAA nanofiber film: adopt coaxial needle on the basis of traditional electrospinning device, 1-5% (wt) DMAc solution of PAA is used as core, 5-10% (wt) di A 2:1 (V/V) mixed solution of methyl chloride and acetone was used as a shell, spun in a high-voltage electrostatic field, and the flywheel rotated at high speed to receive CA-PAA nanofibers. The electrospun CA-PAA nanofiber membrane was imidized according to the temperature program of 150°C/2h, 200/3h, 250°C/1h, and 260°C/1h to obtain a CA-PI nanofiber membrane; the obtained nanofiber The film was tested for stress-strain at room temperature using a universal material testing machine (CMT-8500) from Shenzhen Xinsansi. as shown in picture 2.
(5)合成苯并噁嗪单体(5) Synthesis of benzoxazine monomer
1)将双酚AF、多聚甲醛和间三氟甲苯胺分别14.7,5.3和14.1g,依次加入装有冷凝回流管、电动搅拌机、N2导气管、温度计的四口瓶中;1) Add 14.7, 5.3 and 14.1 g of bisphenol AF, paraformaldehyde and m-trifluorotoluidine, respectively, into a four-necked flask equipped with a condensing reflux tube, an electric stirrer, N2 airway tube, and a thermometer;
2)加热直至反应物粘稠很难搅拌为止,待反应物冷却至室温,向其加入CHCl3200ml进行溶解;用质量分数2%的NaOH溶液洗涤上述溶解完全的混合溶液,待溶液分层取下层溶液。将分离出来的溶液加入50ml的CHCl3;待搅拌均匀后加入2g的无水氯化钙(CaCl2)脱水;将脱水之后的溶液干燥,得到含氟苯并噁嗪的单体粉末。(6)BAF-tfa以及BAF-tfa/二氧化硅纳米粒子(SiO2NPs)原位固化CA、PI、CA-PI纳米纤维膜;2) Heat until the reactant is viscous and difficult to stir, wait for the reactant to cool to room temperature, add CHCl 3 200ml to it for dissolving; wash the above-mentioned completely dissolved mixed solution with 2% NaOH solution by mass fraction, wait for the solution to be layered and take lower layer solution. Add 50 ml of CHCl 3 to the separated solution; add 2 g of anhydrous calcium chloride (CaCl 2 ) to dehydrate after stirring evenly; dry the dehydrated solution to obtain monomer powder containing fluorobenzoxazine. (6) BAF-tfa and BAF-tfa/silica nanoparticles (SiO 2 NPs) in situ curing CA, PI, CA-PI nanofibrous membranes;
1)称取0.001g,0.002g,0.005g,0.01g,0.05g,0.1g和0.4g的含氟苯并噁嗪BAF-tfa单体粉末,按照质量分数分别为0.01%、0.02%、0.05%、0.1%、0.5%、1.0%、4.0%溶解在乙酸丁酯(ButylAcetate)中,得到溶解完全且混合均一的透明溶液;1) Weigh 0.001g, 0.002g, 0.005g, 0.01g, 0.05g, 0.1g and 0.4g of fluorine-containing benzoxazine BAF-tfa monomer powder, according to the mass fraction of 0.01%, 0.02%, 0.05% %, 0.1%, 0.5%, 1.0%, and 4.0% were dissolved in Butyl Acetate (ButylAcetate) to obtain a completely dissolved and uniformly mixed transparent solution;
2)将制备的CA、PI、CA-PI纤维膜裁剪2×2cm宽度和长度的实验样品,并将该纤维膜浸渍在溶有含氟苯并噁嗪BAF-tfa的乙酸丁酯溶液中;2) cutting the prepared CA, PI, CA-PI fiber membranes into experimental samples with a width and length of 2×2 cm, and immersing the fiber membranes in a butyl acetate solution containing fluorobenzoxazine BAF-tfa;
3)用摄子将浸渍在混合溶液中的CA、PI、CA-PI纤维膜迅速取出,先在自然条件下晾干,然后放进真空供箱进行固化;之后冷却至室温,取出F-PBZ/CA、F-PBZ/PI、F-PBZ/CA-PI备用。3) Quickly take out the CA, PI, and CA-PI fiber membranes immersed in the mixed solution with a camera, first dry them under natural conditions, and then put them into a vacuum supply box for curing; after cooling to room temperature, take out the F-PBZ /CA, F-PBZ/PI, F-PBZ/CA-PI spare.
4)称取0.001g,0.002g,0.005g,0.01g,0.05g,0.1g和0.4g的BAF-tfa单体粉末,按照质量分数分别为0.01%、0.02%、0.05%、0.1%、0.5%、1.0%、4.0%溶解在乙酸丁酯(ButylAcetate)中;4) Weigh 0.001g, 0.002g, 0.005g, 0.01g, 0.05g, 0.1g and 0.4g of BAF-tfa monomer powder, respectively 0.01%, 0.02%, 0.05%, 0.1%, 0.5% by mass fraction %, 1.0%, 4.0% dissolved in butyl acetate (ButylAcetate);
5)并加入质量分数为0.01%、0.02%、0.05%、0.1%、0.5%、1.0%、4.0%的SiO2NPs到乙酸丁酯溶液中,得到溶解完全且混合均一的透明溶液;5) Adding SiO 2 NPs with a mass fraction of 0.01%, 0.02%, 0.05%, 0.1%, 0.5%, 1.0%, and 4.0% to the butyl acetate solution to obtain a completely dissolved and uniformly mixed transparent solution;
6)将制备的CA、PI、CA-PI纤维膜裁剪2×2cm宽度和长度的实验样品,并将该纤维膜浸渍在溶有BAF-tfa和SiO2NPs的乙酸丁酯液中;最后,用镊子将浸渍在混合溶液中的纤维膜迅速取出,先在自然条件下晾干,然后放进真空烘箱进行固化2h,之后冷却至室温,取出F-PBZ/SNP/CA、F-PBZ/SNP/PI、F-PBZ/SNP/CA-PI备用。6) Cut the prepared CA, PI, CA-PI fiber membranes into experimental samples with a width and length of 2×2cm, and soak the fiber membranes in butyl acetate solution in which BAF-tfa and SiO 2 NPs are dissolved; finally, Use tweezers to quickly take out the fiber membrane immersed in the mixed solution, first dry it under natural conditions, then put it in a vacuum oven for 2 hours, and then cool it to room temperature, take out the F-PBZ/SNP/CA, F-PBZ/SNP /PI, F-PBZ/SNP/CA-PI standby.
(7)接触角实验,(7) Contact angle experiment,
利用接触角实验仪器对不同浓度苯并噁嗪以及二氧化硅纳米粒子改性的CA、PI、CA-PI纳米纤维膜,F-PBZ/CA,F-PBZ/PI,F-PBZ/CA-PI以及F-PBZ/SNP/CA,F-PBZ/SNP/PI,F-PBZ/SNP/CA-PI复合纤维膜上述各个浓度所得到的样品的疏水性能和亲油性能的静态接触角进行研究。CA, PI, CA-PI nanofiber membranes modified with different concentrations of benzoxazine and silica nanoparticles, F-PBZ/CA, F-PBZ/PI, F-PBZ/CA- PI and F-PBZ/SNP/CA, F-PBZ/SNP/PI, and F-PBZ/SNP/CA-PI composite fiber membranes were studied for their hydrophobic and lipophilic static contact angles.
(8)油水分离实验:(8) Oil-water separation experiment:
1)分别量取10ml的二氯甲烷和水,水用亚甲基蓝染色,油(二氯甲烷)用油红染色。将200ml的油水混合溶液静置1min后,油水发生分离。被染成蓝色的水在上层,红色的油在下层,F-PBZ--1/SNP-4/CA-PI功能纤维膜被固定在两个玻璃管之间。然后,将分层的混合溶液倒入上面的玻璃管内,进行油水分离。红色的油迅速的渗透F-PBZ-1/SNP-4/CA-PI纤维膜,流到下面的烧杯中,而蓝色的水仍然留在上层的玻璃管内,并记录油水完全分离开的时间,以及测量分离前和分离后水的体积。1) Measure 10ml of dichloromethane and water respectively, the water is stained with methylene blue, and the oil (dichloromethane) is stained with oil red. After the 200ml oil-water mixed solution was left to stand for 1min, the oil-water separation occurred. The water dyed blue was in the upper layer, the red oil was in the lower layer, and the F-PBZ--1/SNP-4/CA-PI functional fiber membrane was fixed between two glass tubes. Then, pour the layered mixed solution into the upper glass tube for oil-water separation. The red oil quickly permeated the F-PBZ-1/SNP-4/CA-PI fiber membrane and flowed into the beaker below, while the blue water remained in the upper glass tube, and the time for complete separation of oil and water was recorded , and measure the volume of water before and after separation.
2)分别选择不同的油水混合物(二氯甲烷-水、溴苯-水、四氯化碳-水、三氯甲烷-水和1,2-二氯乙烷-水)20ml(1/1(V/V)),按照1)进行油水分离实验。2) Select 20ml (1/1( V/V)), carry out the oil-water separation experiment according to 1).
3)分别电纺不同厚度的CA-PAA膜并亚胺化得到CA-PI膜,在经过1wt%的BAF-tfa和4wt%SiO2NPs原位固化得到不同厚度F-PBZ-1/SNP-4/CA-PI膜。并按1)进行油水分离实验。3) CA-PAA films of different thicknesses were electrospun and imidized to obtain CA-PI films, and F-PBZ- 1 /SNP- 4/CA-PI film. And carry out the oil-water separation experiment according to 1).
4)选择F-PBZ-1/SNP-4/CA-PI膜,并按1)进行多次油水分离。4) Select F-PBZ-1/SNP-4/CA-PI membrane, and perform multiple oil-water separations according to 1).
本发明主要就是同轴电纺得到同轴CA-PI纳米纤维膜,之前做的用BAF-tfa和SiO2NPs改性的CA,其流量只能达到1800Lm-2h-1,分离效率达到96%,应力6.65MPa;BAF-tfa和SiO2NPs改性的PI,其流量和分离效率也只能达到400Lm-2h-1和95%,而我们做的时候给电纺成同轴的CA-PI纳米纤维膜,就好像在力学性能比较差的CA里面加上一根钢丝,经过高温亚胺化之后BAF-tfa和SiO2NPs改性的CA-PI膜,其流量能够达到2270Lm-2h-1,分离效率达到99.5%,提高其应变大于200MPa。而且能够耐酸耐碱,耐高温,可循环10次使用,在实际油水分离的应用中,能够大大节省油水分离的时间,节约成本。克服了现有的电纺膜在实际油水分离应用中流量低,分离效率低,力学性能差,不经久耐用,在循环使用的过程中特别容易破容易被强酸,强碱以及高温苛刻条件腐蚀的缺点。增加了现有油水分离膜的可使用次数,节约了经济成本。The main purpose of the present invention is to obtain the coaxial CA-PI nanofiber membrane by coaxial electrospinning. The flow rate of CA modified with BAF-tfa and SiO 2 NPs can only reach 1800Lm -2 h -1 , and the separation efficiency can reach 96 %, stress 6.65MPa; BAF-tfa and SiO 2 NPs modified PI, its flow rate and separation efficiency can only reach 400Lm -2 h -1 and 95%, and when we do it, we give electrospun coaxial CA -PI nanofibrous membrane is like adding a steel wire to CA with relatively poor mechanical properties. After high-temperature imidization, the CA-PI membrane modified by BAF-tfa and SiO 2 NPs can reach a flow rate of 2270Lm -2 h -1 , the separation efficiency reaches 99.5%, and the strain is increased by more than 200MPa. Moreover, it is resistant to acid and alkali, high temperature, and can be used for 10 cycles. In the actual application of oil-water separation, it can greatly save the time and cost of oil-water separation. It overcomes the problems of low flow rate, low separation efficiency, poor mechanical properties, not durable, easy to be broken in the process of recycling, and easy to be corroded by strong acid, strong alkali and high temperature harsh conditions in the actual application of oil-water separation. shortcoming. The usable times of the existing oil-water separation membrane are increased, and the economic cost is saved.
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