2006Journal of Qingdao University of Science and TechnologyRequires access

Study on Controlling Method of Dynamic-accumulation in Batch Distillation

Shuang Song

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Abstract

A controlling method of total reflux by introducing temperatures of middle part and top part in batch distillation column was set up,and isopropanol and n-propanol were used to conduct the experimental study of this operation.The result indicated that the state switch of total reflux and total withdraw by controlling double-temperature in dynamic accumulation process was completely feasible.Furthermore,introducing the controlling point of middle part temperature in column could make the quantity and quality of product better that those of the method only using top part temperature,and double-temperature controlling operation was more flexible,but switching times was more than single-temperature controlling.

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What this paper is about

A controlling method of total reflux by introducing temperatures of middle part and top part in batch distillation column was set up,and isopropanol and n-propanol were used to conduct the experimental study of this operation.The result indicated that the state switch of total reflux and total withdraw by controlling double-temperature in dynamic accumulation process was completely feasible.Furthermore,introducing the controlling point of middle part temperature in column could make the quantity and quality of product better that those of the method only using top part temperature,and double-temperature controlling operation was more flexible,but switching times was more than single-temperature controlling.

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Available abstract

A controlling method of total reflux by introducing temperatures of middle part and top part in batch distillation column was set up,and isopropanol and n-propanol were used to conduct the experimental study of this operation.The result indicated that the state switch of total reflux and total withdraw by controlling double-temperature in dynamic accumulation process was completely feasible.Furthermore,introducing the controlling point of middle part temperature in column could make the quantity and quality of product better that those of the method only using top part temperature,and double-temperature controlling operation was more flexible,but switching times was more than single-temperature controlling.

Key concepts: Batch distillation, Distillation, Process (computing), Process engineering, Fractional distillation, Column (typography), Chemistry, Computer science

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