Global minimization of total exergy loss of multicomponent distillation configurations

Jiang, Zheyu; Chen, Zewei; Huff, Joshua; Shenvi, Anirudh A.; Tawarmalani, Mohit; Agrawal, Rakesh

doi:10.1002/aic.16737

Title: Global minimization of total exergy loss of multicomponent distillation configurations

Journal Article · 07 August 2019 · AIChE Journal

DOI: https://doi.org/10.1002/aic.16737 · OSTI ID:1547572

Jiang, Zheyu ^[1]; Chen, Zewei ^[1]; Huff, Joshua ^[1]; Shenvi, Anirudh A. ^[1]; Tawarmalani, Mohit ^[2];

^[1]

Davidson School of Chemical Engineering Purdue University West Lafayette Indiana
Krannert School of Management Purdue University West Lafayette Indiana

Abstract The operating cost of a multicomponent distillation system comprises two major aspects: the overall heat duty requirement and the temperature levels at which the heat duties are generated and rejected. The second aspect, often measured by the thermodynamic efficiency of the distillation system, can be quantified by its total exergy loss. In this article, we introduce a global optimization framework for determining the minimum total exergy loss required to distill any ideal or near‐ideal multicomponent mixture using a sequence of columns. Desired configurations identified by this new framework tend to use milder‐temperature reboilers and condensers and are thus attractive for applications such as heat pump assisted distillation. Through a case study of shale gas separations, we demonstrate the effectiveness of this framework and present various useful physical insights for designing energy efficient distillation systems.

View Accepted Manuscript (Publisher)

Cite

Export

Save

Sponsoring Organization:: USDOE

Grant/Contract Number:: EE0005768

OSTI ID:: 1547572

Journal Information:: AIChE Journal, Journal Name: AIChE Journal Journal Issue: 11 Vol. 65; ISSN 0001-1541

Publisher:: Wiley Blackwell (John Wiley & Sons)Copyright Statement

Country of Publication:: United States

Language:: English

References (39)

A matrix method for multicomponent distillation sequences Shah, Vishesh H.; Agrawal, Rakesh AIChE Journal, Vol. 56, Issue 7 https://doi.org/10.1002/aic.12118	journal	November 2009
A synthesis method for multicomponent distillation sequences with fewer columns Shenvi, Anirudh A.; Shah, Vishesh H.; Zeller, Jeremy A. AIChE Journal, Vol. 58, Issue 8 https://doi.org/10.1002/aic.12752	journal	September 2011
On separation efficiency Cussler, E. L.; Dutta, Binay K. AIChE Journal, Vol. 58, Issue 12 https://doi.org/10.1002/aic.13779	journal	March 2012
Global optimization of multicomponent distillation configurations: 1. Need for a reliable global optimization algorithm Nallasivam, Ulaganathan; Shah, Vishesh H.; Shenvi, Anirudh A. AIChE Journal, Vol. 59, Issue 3 https://doi.org/10.1002/aic.13875	journal	July 2012
Global optimization of multicomponent distillation configurations: 2. Enumeration based global minimization algorithm Nallasivam, Ulaganathan; Shah, Vishesh H.; Shenvi, Anirudh A. AIChE Journal, Vol. 62, Issue 6 https://doi.org/10.1002/aic.15204	journal	February 2016
A systematic method to synthesize all dividing wall columns for n -component separation: Part II Madenoor Ramapriya, Gautham; Tawarmalani, Mohit; Agrawal, Rakesh AIChE Journal, Vol. 64, Issue 2 https://doi.org/10.1002/aic.15963	journal	September 2017
A systematic method to synthesize all dividing wall columns for n -component separation-Part I Madenoor Ramapriya, Gautham; Tawarmalani, Mohit; Agrawal, Rakesh AIChE Journal, Vol. 64, Issue 2 https://doi.org/10.1002/aic.15964	journal	September 2017
Minimum energy of multicomponent distillation systems using minimum additional heat and mass integration sections Jiang, Zheyu; Madenoor Ramapriya, Gautham; Tawarmalani, Mohit AIChE Journal, Vol. 64, Issue 9 https://doi.org/10.1002/aic.16189	journal	May 2018
Systematic synthesis of separation schemes Thompson, Roger W.; King, C. Judson AIChE Journal, Vol. 18, Issue 5 https://doi.org/10.1002/aic.690180510	journal	September 1972
Improving distillation column design using thermodynamic availability analysis Fitzmorris, R. E.; Mah, R. S. H. AIChE Journal, Vol. 26, Issue 2 https://doi.org/10.1002/aic.690260209	journal	March 1980
Shortcut evaluation ofΔT andQΔT for the synthesis of heat integrated distillation sequences Glinos, K.; Malone, M. F.; Douglas, J. M. AIChE Journal, Vol. 31, Issue 6 https://doi.org/10.1002/aic.690310622	journal	June 1985
Graphic exergy analysis of processes in distillation column by energy-utilization diagrams Taprap, Ruchira; Ishida, Masaru AIChE Journal, Vol. 42, Issue 6 https://doi.org/10.1002/aic.690420615	journal	June 1996
Optimal thermodynamic feed conditions for distillation of ideal binary mixtures Agrawal, Rakesh; Herron, D. Michael AIChE Journal, Vol. 43, Issue 11 https://doi.org/10.1002/aic.690431111	journal	November 1997
Improved direct and indirect systems of columns for ternary distillation Agrawal, Rakesh; Fidkowski, Zbigniew T. AIChE Journal, Vol. 44, Issue 4 https://doi.org/10.1002/aic.690440407	journal	April 1998
Efficient use of an intermediate reboiler or condenser in a binary distillation Agrawal, Rakesh; Herron, D. Michael AIChE Journal, Vol. 44, Issue 6 https://doi.org/10.1002/aic.690440608	journal	June 1998
Intermediate reboiler and condenser arrangement for binary distillation columns Agrawal, Rakesh; Herron, D. Michael AIChE Journal, Vol. 44, Issue 6 https://doi.org/10.1002/aic.690440609	journal	June 1998
New thermally coupled schemes for ternary distillation Agrawal, Rakesh; Fidkowski, Zbigniew T. AIChE Journal, Vol. 45, Issue 3 https://doi.org/10.1002/aic.690450306	journal	March 1999
Synthesis of multicomponent distillation column configurations Agrawal, Rakesh AIChE Journal, Vol. 49, Issue 2 https://doi.org/10.1002/aic.690490210	journal	February 2003
Convexification and Global Optimization in Continuous and Mixed-Integer Nonlinear Programming Tawarmalani, Mohit; Sahinidis, Nikolaos V. Nonconvex Optimization and Its Applications https://doi.org/10.1007/978-1-4757-3532-1	book	January 2002
A polyhedral branch-and-cut approach to global optimization Tawarmalani, Mohit; Sahinidis, Nikolaos V. Mathematical Programming, Vol. 103, Issue 2 https://doi.org/10.1007/s10107-005-0581-8	journal	May 2005
Net work consumption in distillation—short-cut evaluation and applications to synthesis Glinos, K.; Malone, M. F. Computers & Chemical Engineering, Vol. 13, Issue 3 https://doi.org/10.1016/0098-1354(89)85007-0	journal	March 1989
Efficient cryogenic nitrogen generators: An exergy analysis Agrawal, R.; Woodward, D. W. Gas Separation & Purification, Vol. 5, Issue 3 https://doi.org/10.1016/0950-4214(91)80012-T	journal	September 1991
Process intensification in multicomponent distillation: A review of recent advancements Jiang, Zheyu; Agrawal, Rakesh Chemical Engineering Research and Design, Vol. 147 https://doi.org/10.1016/j.cherd.2019.04.023	journal	July 2019
Design of distillation sequences: from conventional to fully thermally coupled distillation systems Caballero, José A.; Grossmann, Ignacio E. Computers & Chemical Engineering, Vol. 28, Issue 11 https://doi.org/10.1016/j.compchemeng.2004.04.010	journal	October 2004
Synthesis of distillation configurations: I. Characteristics of a good search space Giridhar, Arun; Agrawal, Rakesh Computers & Chemical Engineering, Vol. 34, Issue 1 https://doi.org/10.1016/j.compchemeng.2009.05.003	journal	January 2010
Synthesis of distillation configurations. II: A search formulation for basic configurations Giridhar, Arun; Agrawal, Rakesh Computers & Chemical Engineering, Vol. 34, Issue 1 https://doi.org/10.1016/j.compchemeng.2009.05.004	journal	January 2010
Global optimization of multicomponent distillation configurations: Global minimization of total cost for multicomponent mixture separations Jiang, Zheyu; Mathew, Tony Joseph; Zhang, Haibo Computers & Chemical Engineering, Vol. 126 https://doi.org/10.1016/j.compchemeng.2019.04.009	journal	July 2019
Short-Cut Methods versus Rigorous Methods for Performance-Evaluation of Distillation Configurations Ramapriya, Gautham Madenoor; Selvarajah, Ajiththaa; Jimenez Cucaita, Luis Eduardo Industrial & Engineering Chemistry Research, Vol. 57, Issue 22 https://doi.org/10.1021/acs.iecr.7b05214	journal	May 2018
Two-feed distillation. Same-composition feeds with different enthalpies Wankat, Phillip C.; Kessler, David P. Industrial & Engineering Chemistry Research, Vol. 32, Issue 12 https://doi.org/10.1021/ie00024a015	journal	December 1993
Generalized Disjunctive Programming Model for the Optimal Synthesis of Thermally Linked Distillation Columns Caballero, José A.; Grossmann, Ignacio E. Industrial & Engineering Chemistry Research, Vol. 40, Issue 10 https://doi.org/10.1021/ie000761a	journal	May 2001
Minimum Energy Consumption in Multicomponent Distillation. 3. More Than Three Products and Generalized Petlyuk Arrangements Halvorsen, Ivar J.; Skogestad, Sigurd Industrial & Engineering Chemistry Research, Vol. 42, Issue 3 https://doi.org/10.1021/ie0108651	journal	February 2003
Thermodynamic Analysis of Thermally Coupled Distillation Sequences Flores, Olga A.; Cárdenas, J. Carlos; Hernández, Salvador Industrial & Engineering Chemistry Research, Vol. 42, Issue 23 https://doi.org/10.1021/ie034011n	journal	November 2003
Are All Thermal Coupling Links between Multicomponent Distillation Columns Useful from an Energy Perspective? Shah, Vishesh H.; Agrawal, Rakesh Industrial & Engineering Chemistry Research, Vol. 50, Issue 3 https://doi.org/10.1021/ie101768c	journal	February 2011
Shale Gas Processing Integrated with Ethylene Production: Novel Process Designs, Exergy Analysis, and Techno-Economic Analysis He, Chang; You, Fengqi Industrial & Engineering Chemistry Research, Vol. 53, Issue 28 https://doi.org/10.1021/ie5012245	journal	July 2014
Synthesis of Distillation Column Sequences for Nonsharp Separations Ivakpour, Javad; Kasiri, Norollah Industrial & Engineering Chemistry Research, Vol. 48, Issue 18 https://doi.org/10.1021/ie802013r	journal	September 2009
Synthesis of Distillation Column Configurations for a Multicomponent Separation Agrawal, Rakesh Industrial & Engineering Chemistry Research, Vol. 35, Issue 4 https://doi.org/10.1021/ie950323h	journal	January 1996
Are Thermally Coupled Distillation Columns Always Thermodynamically More Efficient for Ternary Distillations? Agrawal, Rakesh; Fidkowski, Zbigniew T. Industrial & Engineering Chemistry Research, Vol. 37, Issue 8 https://doi.org/10.1021/ie980062m	journal	August 1998
Thermodynamically Efficient Systems for Ternary Distillation Agrawal, Rakesh; Fidkowski, Zbigniew T. Industrial & Engineering Chemistry Research, Vol. 38, Issue 5 https://doi.org/10.1021/ie980531k	journal	May 1999
Thermodynamic Analysis of Separation Systems Demirel, Yaşar Separation Science and Technology, Vol. 39, Issue 16 https://doi.org/10.1081/SS-200041152	journal	January 2004

Similar Records

Global optimization of multicomponent distillation configurations: Global minimization of total cost for multicomponent mixture separations

Journal Article · 2019 · Computers and Chemical Engineering · OSTI ID:1511698

Jiang, Zheyu; Mathew, Tony Joseph; Zhang, Haibo; +4 more

Process Intensification in Multicomponent Distillation: A Review of Recent Advancements

Journal Article · 2019 · Chemical Engineering Research and Design · OSTI ID:1511532

Jiang, Zheyu; Agrawal, Rakesh

Global optimization of multicomponent distillation configurations: 2. Enumeration based global minimization algorithm

Journal Article · 2016 · AIChE Journal · OSTI ID:1238668

Nallasivam, Ulaganathan; Shah, Vishesh H.; Shenvi, Anirudh A.; +3 more

Title: Global minimization of total exergy loss of multicomponent distillation configurations

Citation Formats

References (39)

Similar Records

Related Subjects