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Way to predict tray temperatures

Victor L. Rice

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Abstract

An analysis of distillation columns often requires data for individual tray temperatures, either specific ones or the entire profile. A common approach to obtain this temperature information is through use of a rigorous tray-by-tray distillation simulation, usually with a main-frame computer system. Unfortunately, this rigorous approach is either impractical or just too much trouble in many cases. For example, an on-line optimizing control scheme rarely has enough space (computer memory) or real time for a rigorous calculation of distillation column tray temperatures. A shorter method is presented in this article that predicts the tray temperatures of simple distillation columns. Following the theoretical discussion of the method, some examples of its use are presented.

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What this paper is about

An analysis of distillation columns often requires data for individual tray temperatures, either specific ones or the entire profile. A common approach to obtain this temperature information is through use of a rigorous tray-by-tray distillation simulation, usually with a main-frame computer system. Unfortunately, this rigorous approach is either impractical or just too much trouble in many cases. For example, an on-line optimizing control scheme rarely has enough space (computer memory) or real time for a rigorous calculation of distillation column tray temperatures. A shorter method is presented in this article that predicts the tray temperatures of simple distillation columns. Following the theoretical discussion of the method, some examples of its use are presented.

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Available abstract

An analysis of distillation columns often requires data for individual tray temperatures, either specific ones or the entire profile. A common approach to obtain this temperature information is through use of a rigorous tray-by-tray distillation simulation, usually with a main-frame computer system. Unfortunately, this rigorous approach is either impractical or just too much trouble in many cases. For example, an on-line optimizing control scheme rarely has enough space (computer memory) or real time for a rigorous calculation of distillation column tray temperatures. A shorter method is presented in this article that predicts the tray temperatures of simple distillation columns. Following the theoretical discussion of the method, some examples of its use are presented.

Key concepts: Tray, Distillation, Fractionating column, Computer science, Process engineering, Column (typography), Simple (philosophy), Frame (networking)

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