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- W2393511351 abstract "The aim of this work is to simulate and examine a batch extractive distillation process for purification of dimethyl carbonate(DMC) from the DMC-MEOH azeotropic system.The extractive solvent ethylene carbonate(EC) was used,which was also one of the reagents to synthesize DMC.The results of simulation were compared with examination in the following fields: reflux ratio,temperature of solvent,flow rate of solvent etc.The products could be separated under the following operation condition: reflux ratio in extractive distillation 0.8—1.2,reflux ratio in the distillation of EC-DMC 2— 2.5;optimum temperature of solvent 65 ℃,flux rate of solvent to the azeotrope 1.85—1.95.The obtained results could be possibly used as the theoretical and practical basis for industrial equipment." @default.
- W2393511351 created "2016-06-24" @default.
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- W2393511351 date "2008-01-01" @default.
- W2393511351 modified "2023-09-23" @default.
- W2393511351 title "Batch separation of dimethyl carbonate-methanol azeotrope" @default.
- W2393511351 hasPublicationYear "2008" @default.
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