A gas separation membrane resistant to organic vapor corrosion and its preparation method
A technology for gas separation membranes and organic vapors, which is applied in separation methods, semipermeable membrane separations, and dispersed particle separations. The effect of improving binding strength and separation selectivity
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Embodiment 1
[0029] Dissolve 3g of PEG400 and 1g of macromolecule PEG20000 mixed additives in N,N-dimethylformamide solvent at 40°C. After completely dissolving, add 15g of PVDF-HFP powder to the solution to prepare a casting film with a total mass of 100g solution, the dissolution temperature is maintained at 70°C, after obtaining a uniform and transparent casting solution, after standing for 16 hours for degassing, use a scraper to scrape evenly on the non-woven fabric with a scraper thickness of 150μm, stay in the air for 5s and then immerse After staying in the methanol solution for 2s, take it out immediately, then immerse in deionized water for 30s, take out the membrane, and rinse the membrane surface with clean water repeatedly for 30min to obtain a PVDF-HFP porous base membrane. Dissolve the ternary copolymerization block silicone oil (if not specified, the ternary copolymerization block silicone oil is provided by Shandong Dayi Chemical Co., Ltd. in all examples) in the solvent to...
Embodiment 2~3
[0032] Examples 2-3 investigated the influence of coating film conditions on film performance and solvent resistance, and the rest of the conditions are the same as in Example 1. The conclusions are shown in Tables 2 to 4: the membrane with PVDF-HFP as the base membrane and ternary copolymerized silicone oil as the composite layer material maintains stable separation performance and has good solvent resistance during continuous operation.
[0033] Table 1 Embodiment 2~3 film-making conditions
[0034]
[0035]
Embodiment 4
[0037]Example 4 investigates the effect of using PVDF material as the base film on the performance and solvent resistance of the composite film during long-term operation, and the rest of the conditions are the same as in Example 1. The conclusions are shown in Tables 2 to 4: During the continuous operation of the membrane with PVDF as the base membrane and ternary copolymerized silicone oil as the composite layer material, the separation factor of the membrane and the permeation rate of n-hexane are both decreasing, which shows that PVDF is in the process of long-term operation. The substrate is easily eroded by n-hexane solvent, and the pores shrink and deform under the pressure of the membrane surface, resulting in a decrease in separation performance.
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