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Structural Control And Gas Separation Performance Of Nanoscale Hybrid Silica Membranes

Posted on:2020-09-16Degree:MasterType:Thesis
Country:ChinaCandidate:S H ChaiFull Text:PDF
GTID:2381330602999201Subject:Materials engineering
Abstract/Summary:PDF Full Text Request
The pore size of the microporous silica membrane prepared by silica can be precisely controlled by sol-gel method.So it is suitable for efficient separation of small molecule gases,and shows good application prospects in the fields such as hydrogen energy production,natural gas purification and CO2 capture.However,due to the rich hydroxyl groups on the surface of traditional silica membranes,the hydrolysis of Si-O-Si in the structure of silica membranes is easy to occur in the hydrothermal environment,which limits its practical application.Therefore,the use of organic-inorganic hybrid alkoxides that contain hydrophobic groups such as methyltriethoxysilane?MTES?,1,2-bis?triethoxysilyl?ethane?BTESE?,1,8-bis?triethoxysilyl?octane?BTESO?,have been proposed by several research groups for the preparation of organic-inorganic hybrid silica membranes,which not only greatly improves the hydrophobicity of silica membranes,but also provides new inspiration for the structural control of hybrid silica membranes.In this paper,organic-inorganic hybrid silica sols were synthesized by sol-gel method using BTESE and MTES as precursors.The hybrid silica membranes were prepared by hot-coating method.The effects of BTESE/MTES ratio on the structure and gas separation properties of the membranes were investigated by Fourier transform infrared spectroscopy?FTIR?,N2 sorption?BET?,scanning electron microscopy?SEM?and home-made gas permeation/separation device.The results showed that:with the increase of the proportion of MTES in the precursors,the porosity of the hybrid silica membrane increased.When BTESE/MTES=1/3,the hybrid silica membrane exhibited the largest gas permeation,the permeance of H2 and CO2 can reach 7.99×10-7 mol·m-2·s-1·Pa-1 and 3.53×10-7 mol·m-2·s-1·Pa-1,respectively.And when BTESE/MTES=1/2,the best gas separation selectivity was achieved on the membrane,the ideal selectivity of H2/N2,H2/CH4,CO2/N2 and CO2/CH4 were 64.4,73.6,28.5 and 32.6,respectively,the mixed gas separation selectivity of H2/N2 and CO2/CH4 were 19.0 and 14.6,respectively.Subsequently,the hybrid silica membranes were doped by metal-organic frameworks?MOFs?CuBDC crystals,and CuBDC/hybrid silica composite membranes were successfully prepared by dip-coating method.The effects of bulk-type and sheet CuBDC on the separation efficiency of CO2/CH4 were compared.The results showed that the CO2 permeance for composite membranes prepared by bulk-type CuBDC doping was higher than that of pristine hybrid silica membranes,and it can reach 9.39×10-7 mol·m-2·s-1·Pa-1,but the ideal selectivity of CO2/CH4 was only19.0,while the composite membranes doped with sheet CuBDC can achieve 63.5,which was much higher than that of pristine hybrid silica membranes,and the CO2permeance was 2.25×10-7 mol·m-2·s-1·Pa-1.The membrane still performed well in the mixed gas separation,the CO2/CH4 mixture selectivity can reach 33.4.
Keywords/Search Tags:hybrid silica membranes, methyltriethoxysilane, 1,2-bis(triethoxysilyl) ethane, CuBDC, gas separation
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