碳酸二甲酯
甘油
酯交换
催化作用
化学
选择性
碳酸盐
产量(工程)
生物柴油
生物柴油生产
有机化学
多相催化
浸出(土壤学)
无机化学
核化学
材料科学
环境科学
土壤科学
冶金
土壤水分
作者
Gundabathini Sandhya Rani,Adigopula Jyotsna,B.L.A. Prabhavathi Devi
标识
DOI:10.1002/slct.202202798
摘要
Abstract Glycerol, a major by‐product from biodiesel industry valorized into glycerol carbonate (GC) employing heterogeneous carbon‐based sulfated sodium (carbon‐SO 3 Na) catalyst derived from glycerol. Investigations have been conducted to study the influence of reaction parameters such as catalyst dosage, DMC/glycerol molar ratio, reaction temperature and reaction time for the production of GC in high yield with high selectivity from glycerol and dimethyl carbonate (DMC) via transesterification process. Under optimized conditions the maximum GC yield (>99 %) with 100 % selectivity was observed with catalyst dose of 1.5 wt.% (of glycerol), DMC/glycerol molar ratio of 3 : 1, reaction temperature of 80 °C in 3 h of reaction period. Further, the catalyst was easily recovered from reaction mixture and reused without any pre‐treatment. The catalyst maintained its crystalline nature with remarkable performance even after 5 cycles of reaction without any deactivation and leaching. The main advantage of the adopted carbon‐SO 3 Na catalyzed protocol for the synthesis of GC is environmentally benign due to its high yield and selectivity under mild reaction conditions. Thus, the carbon‐SO 3 Na catalyst has a wide utility as a potential heterogeneous solid base catalyst for several organic transformations.
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