Study of the structural characteristics of a divided wall column using the sloppy distillation arrangement

An efficient design method is proposed for determining the optimal design structure of a dividing wall column (DWC). The internal section of the DWC is divided into four separate sections and matched to the sloppy arrangement with three conventional simple columns. The light and heavy key component mole-fractions are used as the design variables in each column. The structure that gives superior energy efficiency in the shortcut sloppy case also brings superior energy efficiency in the DWC, while the optimal internal flow distribution of the DWC is different from that obtained from the sloppy configuration. Based upon an extensive simulation study, a two-step approach is proposed for the DWC design: the optimal DWC structure is first determined by applying the shortcut method to the sloppy configuration; the optimal internal flow distribution is then found from the corresponding DWC configuration. The simulation study shows that the DWC designed by the proposed method gives a near-optimal structure.

[1]  Andrew Hoadley,et al.  Identification of heat integration retrofit opportunities for crude distillation and residue cracking units , 2003 .

[2]  Sigurd Skogestad,et al.  Optimal operation of Petlyuk distillation: steady-state behavior , 1999 .

[3]  Rakesh Agrawal,et al.  A Method to Draw Fully Thermally Coupled Distillation Column Configurations for Multicomponent Distillation , 2000 .

[4]  Juan Gabriel Segovia-Hernández,et al.  Dynamic analysis of thermally coupled distillation sequences with undirectional flows for the separation of ternary mixtures , 2006 .

[5]  Moonyong Lee,et al.  Application of a thermally coupled distillation column with separated main columns to gas concentration process , 2008 .

[6]  Young Han Kim,et al.  Industrial application of an extended fully thermally coupled distillation column to BTX separation in a naphtha reforming plant , 2003 .

[7]  Gade Pandu Rangaiah,et al.  Retrofitting conventional column systems to dividing-Wall Columns , 2009 .

[8]  Masaru Nakaiwa,et al.  Design of a fully thermally coupled distillation column for hexane process using a semi-rigorous model , 2004 .

[9]  Y. H. Kim,et al.  Approximate design of fully thermally coupled distillation columns , 2002 .

[10]  Michelle A. Phipps,et al.  Experiences from using heat integration software to determine retrofit opportunities within a refinery process , 2002 .

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

[12]  E. R. Gilliland,et al.  Multicomponent Rectification Estimation of the Number of Theoretical Plates as a Function of the Reflux Ratio , 1940 .

[13]  Sigurd Skogestad,et al.  Shortcut Analysis of Optimal Operation of Petlyuk Distillation , 2004 .

[14]  En Sup Yoon,et al.  The energy saving effects of complex heat-integrated distillation configurations , 1989 .

[15]  Moonyong Lee,et al.  Approximate estimation of operational variables in fully thermally coupled distillation columns using pseudo-pinch points , 2009 .

[16]  Robin Smith,et al.  Operation and Control of Dividing Wall Distillation Columns: Part 1: Degrees of Freedom and Dynamic Simulation , 1998 .

[17]  Salvador Hernández,et al.  Design and Energy Performance of Alternative Schemes to the Petlyuk Distillation System , 2003 .

[18]  Sigurd Skogestad,et al.  Minimum Energy Consumption in Multicomponent Distillation. 2. Three-Product Petlyuk Arrangements , 2003 .

[19]  M. R. Fenske,et al.  Fractionation of Straight-Run Pennsylvania Gasoline , 1932 .

[20]  K. A. Amminudin,et al.  Design and Optimization of Fully Thermally Coupled Distillation Columns: Part 2: Application of Dividing Wall Columns in Retrofit , 2001 .

[21]  Rakesh Agrawal,et al.  New thermally coupled schemes for ternary distillation , 1999 .

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

[23]  Ki-Pung Yoo,et al.  Diagnosis of thermodynamic efficiency in heat integrated distillation , 1988 .

[24]  Young Han Kim Structural design and operation of a fully thermally coupled distillation column , 2002 .

[25]  Design of a fully thermally coupled distillation column based on dynamic simulations , 2000 .

[26]  Michael F. Malone,et al.  Approximate design and optimization of a thermally coupled distillation with prefractionation , 1988 .