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间歇提馏塔的操作

许松林a; Jose Espinosab; Hector E. Salomoneb; Oscar A. Iribarrenb   

  1. a National Engineering Research Center for Distillation Technology, Tianjin University,
    Tianiin 300072, China
    b Institute for Development and Design INGAR, Conicet, Santa Fe, Argentina
  • 收稿日期:1900-01-01 修回日期:1900-01-01 出版日期:2001-06-28 发布日期:2001-06-28
  • 通讯作者: 许松林

Operation of a Batch Stripping Distillation Column

XU Songlina; Jose Espinosab; Hector E. Salomoneb; Oscar A. Iribarrenb   

  1. a National Engineering Research Center for Distillation Technology, Tianjin University,
    Tianiin 300072, China
    b Institute for Development and Design INGAR, Conicet, Santa Fe, Argentina
  • Received:1900-01-01 Revised:1900-01-01 Online:2001-06-28 Published:2001-06-28
  • Contact: XU Songlin

摘要: A stripping batch distillation column is preferred when the amount of the light component
in the feed is small and the products are to be recovered at high purity. The operation
modes of a batch stripping are believed to be the same as those of a rectifier. However,
the control system of a stripper is different. In this paper, we explore three different
control methods with Hysys (Hyprotech Ltd. 1997) for a batch stripper. The main difference
is the control scheme for reboiler liquid level: (a) controlled by reflux flow; (b)
controlled by reboiler heat duty; (c) controlled by bottom product flow. The main
characteristics of operating a batch stripper with different control scheme are presented
in this paper. Guidelines are provided for the startup of a batch stripper, the effects of
somecontrol tuning parameters on the column performance are discussed.

关键词: batch stripper;control;operation

Abstract: A stripping batch distillation column is preferred when the amount of the light component
in the feed is small and the products are to be recovered at high purity. The operation
modes of a batch stripping are believed to be the same as those of a rectifier. However,
the control system of a stripper is different. In this paper, we explore three different
control methods with Hysys (Hyprotech Ltd. 1997) for a batch stripper. The main difference
is the control scheme for reboiler liquid level: (a) controlled by reflux flow; (b)
controlled by reboiler heat duty; (c) controlled by bottom product flow. The main
characteristics of operating a batch stripper with different control scheme are presented
in this paper. Guidelines are provided for the startup of a batch stripper, the effects of
somecontrol tuning parameters on the column performance are discussed.

Key words: batch stripper, control, operation