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A Novel Operation Policy for Dilute Component Separation-Quasi-batch Distillation

A Novel Operation Policy for Dilute Component Separation-Quasi-batch Distillation
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摘要 A new operation policy--quasi-batch distillation for recovering infinitesimal amounts species existing in a mixture is presented. In quasi-batch distillation operation, feed is introduced with a constant flow rate onto the feed stage of the column, and the flow rate of the distillate is the same as that of the feed, whereas the bottom product is withdrawn periodically. The behavior of quasi-batch distillation is simulated and analyzed through an example on heavy water separation. Comparing with continuous or batch distillation, the new operation policy is more reliable and efficient to achieve higher recovery of dilute component. This is especially suitable for separating small amount of precious species from large amount of raw material. A new operation policy-quasi-batch distillation for recovering infinitesimal amounts species existing in a mixture is presented. In quasi-batch distillation operation, feed is introduced with a constant flow rate onto the feed stage of the column, and the flow rate of the distillate is the same as that of the feed, whereas the bottom product is withdrawn periodically. The behavior of quasi-batch distillation is simulated and analyzed through an example on heavy water separation. Comparing with continuous or batch distillation, the new operation policy is more reliable and efficient to achieve higher recovery of dilute component. This is especially suitable for separating small amount of precious species from large amount of raw material.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2005年第3期338-342,共5页 中国化学工程学报(英文版)
基金 Supported by the National Natural Science Foundation of China (No. 20136010).
关键词 重水 蒸馏法 废水处理 同位素 原料 quasi-batch distillation, isotope separation, operation policy
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  • 1Yamanishi Toshihiko, Okuno Kenji. Control Characteristics of a Cascade Composed of Cryogenic Distillation Columns with Feedback Stream. (Dep. Fusion Eng. Res., Japan Atomic Engergy Res. Inst., Naka, Japan)JAERI-Res. 1994, 94-020.
  • 2Kinoshita Masahiro, et al. Mathematical Simulation Procedure for Single Cryogenie Distillation Column with Feedback stream Processing Six Isotope Species of Molecular Hydrogen. JAERI-M 1982. JAERI-M-82-047.

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