New thermally coupled schemes for ternary distillation

The fully thermally coupled system of distillation columns for ternary separation has two, two-way connections between the columns. New, simplified (and easier to control) systems of columns for ternary separations, with a reduced number of connecting streams, are proposed. The new systems contain one one-way and one two-way connection between the columns. Depending on which connection is located on top and which phase stream (liquid or vapor) is used in the one-way connection, there are four possible configurations for these new systems. For certain feed compositions and relative volatilities of components, these new systems can replace the fully thermally coupled system of columns without any increase in energy demand. The optimum system selected from the four proposed configurations consumes no more, and frequently much less, energy than the side stripper or side rectifier configurations or than a system with a prefractionator.

[1]  Z. Fidkowski,et al.  Minimum energy requirements of thermally coupled distillation systems , 1987 .

[2]  B. Linnhoff,et al.  The design of separators in the context of overall processes , 1988 .

[3]  Arthur W. Westerberg,et al.  Temperature-heat diagrams for complex columns. 3. Underwood's method for the Petlyuk configuration , 1989 .

[4]  Zbigniew Fidkowski,et al.  Energy requirements of nonconventional distillation systems , 1990 .

[5]  Zbigniew T. Fidkowski,et al.  Thermally coupled system of distillation columns: Optimization procedure , 1986 .

[6]  Rakesh Agrawal,et al.  Synthesis of Distillation Column Configurations for a Multicomponent Separation , 1996 .

[7]  Arthur W. Westerberg,et al.  A review of process synthesis , 1981 .

[8]  Arthur W. Westerberg The synthesis of distillation-based separation systems , 1985 .

[9]  Dale F. Rudd,et al.  Synthesis in the design of chemical processes , 1973 .

[10]  Michael F. Malone Optimality Regions for Complex Column Alternatives in Distillation Systems , 1988 .

[11]  F. Petlyuk Thermodynamically Optimal Method for Separating Multicomponent Mixtures , 1965 .

[12]  Sigurd Skogestad,et al.  Operation of Integrated Three-Product (Petlyuk) Distillation Columns , 1995 .

[13]  Adrian Finn,et al.  Rapid assessment of thermally coupled side columns , 1996 .

[14]  Dale F. Rudd,et al.  Parametric studies in industrial distillation: Part I. Design comparisons , 1978 .

[15]  G. Kaibel Distillation columns with vertical partitions , 1987 .

[16]  Ignacio E. Grossmann,et al.  Simultaneous Optimization Model for Multicomponent Separation , 1994 .

[17]  Lee R. Lynd,et al.  Distillation with intermediate heat pumps and optimal sidestream return , 1986 .

[18]  V. Hlaváček,et al.  Synthesis in the design of chemical processes , 1978 .

[19]  K. S. Knaebel,et al.  Pressure swing adsorption: A theoretical study of diffusion‐induced separations , 1987 .

[20]  R. Agrawal,et al.  More operable arrangements of fully thermally coupled distillation columns , 1998 .

[21]  R. Agrawal,et al.  Are Thermally Coupled Distillation Columns Always Thermodynamically More Efficient for Ternary Distillations , 1998 .

[22]  William L. Luyben,et al.  Economics of Alternative Distillation Configurations for the Separation of Ternary Mixtures , 1978 .

[23]  J. Marek,et al.  Separation sequences in multicomponent rectification , 1959 .