2020
DOI: 10.1016/j.seppur.2020.116926
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Separation of dimethyl carbonate/methanol azeotropic mixture by pervaporation with dealcoholized room temperature-vulcanized silicone rubber/nanosilica hybrid active layer

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Cited by 15 publications
(6 citation statements)
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“…The obvious advantage of DMC over other potential fuel additives (methyl tert-butyl ether or ethyl tert-butyl ether) consists in its slow decomposition into carbon dioxide and methanol (MeOH), which do not cause serious consequences when DMC is released into the environment [ 7 , 8 , 9 ]. Thus, DMC is fairly positioned as a “new base stone of chemical engineering” in the 21st century [ 10 ].…”
Section: Introductionmentioning
confidence: 99%
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“…The obvious advantage of DMC over other potential fuel additives (methyl tert-butyl ether or ethyl tert-butyl ether) consists in its slow decomposition into carbon dioxide and methanol (MeOH), which do not cause serious consequences when DMC is released into the environment [ 7 , 8 , 9 ]. Thus, DMC is fairly positioned as a “new base stone of chemical engineering” in the 21st century [ 10 ].…”
Section: Introductionmentioning
confidence: 99%
“…Hydrophilic polymers such as polyacrylic acid, polyvinyl alcohol [ 30 , 31 ], or chitosan [ 32 , 33 , 34 , 35 ] have been shown to be preferentially permeable toward MeOH in pervaporation of MeOH/DMC mixtures. A membrane with a silicone rubber/nanosilica hybrid active layer has been recently developed [ 10 ], which showed the preferential permeation of DMC during the pervaporation separation with inverse DMC/methanol selectivity.…”
Section: Introductionmentioning
confidence: 99%
“…The separation of alcohol-ester azeotropic systems in the chemical industry is a current challenging problem. At present, the traditional methods used for alcohol-ester separation mainly include low-temperature crystallization, azeotropic distillation, extractive distillation, adsorption, etc. These methods suffer from large capital investment, high energy consumption, low efficiency, and complicated operation.…”
Section: Introductionmentioning
confidence: 99%
“…The presence of free silicon hydroxyl groups, hydrogen-bonded silicon hydroxyl groups, and condensed silicon hydroxyl groups on the surface of SiO 2 , and their hydrophilicity and hydrophobicity, can be obtained by chemical modification. The size controllable, hydrophilic and hydrophobic properties of modified SiO 2 are suitable for the advantages in the field of pervaporation. , PDMS have unique advantages such as excellent chemical stability and good affinity for organics. It is considered to be an ideal material for pervaporation membranes. , …”
Section: Introductionmentioning
confidence: 99%
“…Notably, in these processes, because of the thermodynamic equilibrium and limited catalytic ability, excess methanol was generally used for obtaining the high efficiency. Therefore, the target product was always mixed with methanol, and the easily formed DMC/MeOH binary azeotrope (approximate methanol/DMC composition of 70%:30%) increased the complexity of DMC separation [ 14 , 15 , 16 ]. Until now, the available separation methods have included extractive distillation, liquid–liquid extraction, selective adsorption, lower temperature crystallization, and the membrane/distillation integrated process, etc.…”
Section: Introductionmentioning
confidence: 99%