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The selectivity of the catalyst has been varied by changing the reaction condition. The SHTC shows one of the best selectivity for the formation of monoacetins without using excess glycerol. It was found that the catalyst gets deactivated after recycling due to the generation of sulfonated ester on the catalyst surface. The recycled catalyst was again activated by acid treatment with subsequent hydrolysis of sulfonated esters. The catalyst has excellent potential for various bio-refinery processes [28].

Schematic illustration of glycerol acetalization with acetone.
S. N. Name of catalyst Source of catalyst Type of process Reactant Glycerol derivatives Conversion of glycerol (%) Selectivity (%) Ref.
1. TC-L carbon Rice husk Esterification Acetic acid DAG + TAG 90 90 [37]
2. TC-L carbon Rice husk Etherification TBA DTBG + TTBG 53 25 [37]
3. TAC-673 Sucrose Esterification Acetic acid TAG <99 50 [27]
4. AC-SA5 Activated carbon Acetylation Acetic acid DAG + TAG 91 62 [34]
5. PW2-AC Activated Carbon Esterification Acetic acid Diacetin 86 63 [35]
6. SHTC D-glucose Esterification Acetic acid Mono acetin 70 89 [28]
7. SO3H-C, Cellulose Acetalization Acetone Solketal 80 100 [29]
8. SO3H-carbon Glycerol Esterification Acetylation Acetic acid, Acid anhydride

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