CIESC Journal

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SOME CHARACTERISTICS OF PACKED COLUMN FOR CLOSE-BOILING FRACTIONATION

余国琮; 杨志才; 顾芳珍   

  1. Department of Chemical Engineering, Tianjin University
  • 收稿日期:1900-01-01 修回日期:1900-01-01 出版日期:1982-12-28 发布日期:1982-12-28
  • 通讯作者: 余国琮

SOME CHARACTERISTICS OF PACKED COLUMN FOR CLOSE-BOILING FRACTIONATION

YU Kuotsung; YANG Zhicai; GU Fangzhen   

  1. Department of Chemical Engineering, Tianjin University
  • Received:1900-01-01 Revised:1900-01-01 Online:1982-12-28 Published:1982-12-28
  • Contact: YU Kuotsung

摘要: One of the important characteristics of a close-boiling fractionating column is the requirement ofmuch longer start-up time,and consequently the search for ways to minimize such time have been receivedmuch concern and attention.The conventional method of starting up a column is under the conditionof constant vapor velocity,while in this paper,the authors propose another way of operation,i.e.start-up with stepwise lowering of vapor velocity.The mathematical models of these two methods of start-upare developed and solved to obtain the analytical solutions of exponential type to represent the unsteadyconcentration profiles.The derived equations are in agreement with the experimental data.Both theoreti-cal study and experimental work show that,when the same final concentration is reached,the start-uptime for the proposed operation is shorter than that for the conventional.

Abstract: One of the important characteristics of a close-boiling fractionating column is the requirement ofmuch longer start-up time,and consequently the search for ways to minimize such time have been receivedmuch concern and attention.The conventional method of starting up a column is under the conditionof constant vapor velocity,while in this paper,the authors propose another way of operation,i.e.start-up with stepwise lowering of vapor velocity.The mathematical models of these two methods of start-upare developed and solved to obtain the analytical solutions of exponential type to represent the unsteadyconcentration profiles.The derived equations are in agreement with the experimental data.Both theoreti-cal study and experimental work show that,when the same final concentration is reached,the start-uptime for the proposed operation is shorter than that for the conventional.