Preparation method of bifunctional hollow fibrous membrane with strong acidic catalysis and pervaporation
A pervaporation, inorganic hollow fiber technology, applied in the preparation of organic compounds, catalyst activation/preparation, preparation of carboxylate, etc., can solve rare problems, reduce separation steps, improve conversion rate, save equipment and operating costs Effect
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Embodiment 1
[0027] Polyacrylonitrile (PAN), polyvinylpyrrolidone (PVP, K30) and N,N dimethylacetamide (DMAc) were dissolved in a mass ratio of 15:5:80 at 60°C for 24h, stirred and left to stand to obtain a cast film liquid. The hollow fiber membrane spinning device was self-made in the laboratory, and the spinneret used had an outer diameter of 1.5 mm and an inner diameter of 1.0 mm. Pour the casting liquid into the raw material tank and let it stand for 24 hours for defoaming. The casting liquid is filtered through a stainless steel filter before entering the spinneret to remove the tiny particles that may exist in the casting liquid. Under the action of nitrogen pressure, the casting liquid enters the spinneret, the core liquid (internal gel bath) is pumped into the spinneret by a non-pulsating precision metering pump (China, Xingda), and the casting liquid comes out of the spinneret. The material transfer of solvent and non-solvent occurs with the inner and outer gel bath, and the ho...
Embodiment 2
[0031] Dissolve PFSA in an aqueous solution of isopropanol with a mass ratio of 1:1, add nano-SiO 2 and PVA solution, PFSA, nano-SiO 2 The mass ratio to PVA is 8:2:3. Dip-coated on SHFCM-4 pervaporation hollow fiber separation membrane, dried at room temperature, treated with 5wt% hydrochloric acid, and dried at room temperature to obtain a hollow fiber membrane with dual functions of strong acid catalysis and pervaporation. The pervaporation separation column top crude ester (water: 8.91wt%, ethanol: 3.73wt%, ethyl acetate: 87.36wt%) was used to test the separation of the membrane, and the catalytic acetic acid-ethanol esterification reaction was used to test the catalytic activity of the membrane. The PFSA resin loaded on the hollow fiber membrane with the dual functions of strong acid catalysis and pervaporation is 4.0wt%, and the total permeation flux is 136g / m 2 h, the separation factor of water to ethanol is 404, without ethyl acetate permeation, the equilibrium conver...
Embodiment 3
[0033] Dissolve PFSA in an aqueous solution of isopropanol with a mass ratio of 1:1, add nano-SiO 2 and PVA solution, PFSA, nano-SiO 2 The mass ratio with PVA is 10:0:3. Dip-coated on SHFCM-4 pervaporation hollow fiber separation membrane, dried at room temperature, treated with 5wt% hydrochloric acid, and dried at room temperature to obtain a hollow fiber membrane with dual functions of strong acid catalysis and pervaporation. The pervaporation separation column top crude ester (water: 8.91wt%, ethanol: 3.73wt%, ethyl acetate: 87.36wt%) was used to test the separation of the membrane, and the catalytic acetic acid-ethanol esterification reaction was used to test the catalytic activity of the membrane. The PFSA resin loaded on the hollow fiber membrane with strong acid catalysis and pervaporation dual functions is 4.5wt%, and the total permeation flux is 117g / m 2 h, without the permeation of ethanol and ethyl acetate, the equilibrium conversion rate of ethanol in the esterif...
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