Design, optimization and controllability of an alternative process based on extractive distillation for an ethane-carbon dioxide mixture

Chemical Engineering and Processing - Process Intensification

Volumn 74, Issue , 2013, Pages 55-68

  Torres Ortega, Carlo E ^a   Segovia Hernández, Juan Gabriel ^a   Gómez Castro, Fernando I ^a   Hernández, Salvador ^a   Bonilla Petriciolet, Adrián ^b   Rong, Ben Guang ^c   Errico, Massimiliano ^d  

^a UNIVERSITY OF GUANAJUATO   (Mexico)

^b INSTITUTO TECNOLÓGICO DE AGUASCALIENTES   (Mexico)

^c UNIVERSITY OF SOUTHERN DENMARK   (Denmark)

^d UNIVERSITY OF CAGLIARI   (Italy)

Author keywords

Extractive distillation; Greenhouse gases generation; Multi objective differential evolution; Optimization; Singular value decomposition; Thermodynamic efficiency

Indexed keywords

COMPUTER SOFTWARE; CRYOGENICS; DISTILLATION; EFFICIENCY; ETHANE; EVOLUTIONARY ALGORITHMS; GREENHOUSE GASES; MULTIOBJECTIVE OPTIMIZATION; OPTIMIZATION; PARETO PRINCIPLE; SINGULAR VALUE DECOMPOSITION;

ALTERNATIVE CONFIGURATIONS; CARBON DIOXIDE REMOVAL; DIFFERENTIAL EVOLUTION; EXTRACTIVE DISTILLATION; HYDROCARBON FRACTION; MULTI-OBJECTIVE DIFFERENTIAL EVOLUTIONS; STOCHASTIC OPTIMIZATION PROCEDURES; THERMODYNAMIC EFFICIENCY;

CARBON DIOXIDE;

EID: 84890396588     PISSN: 02552701     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cep.2013.09.011     Document Type: Article

References (41)

1. BP BP Energy Outlook 2030, January, London 2012.
2. Elliot D., Quall W.R., Huang S., Chen J.J., Lee R.J., Yao J., Zhang Y. Benefits of integrating NGL extraction and LNG liquefaction technology. Proceedings AIChE 2005 Spring National Meeting Conference 2005, 1943.
3. 2 capture by aqueous monoethaloamine. AIChE 2003, 49(7):1676-1686.
4. 2 absorption system with various amine solution. Prepr. Pap. Am. Chem. Soc. Div. Fuel Chem. 2004, 49:251.
5. 2 removal by amine absorption from a gas based power plant. SIMS2007 Conference 2007, 73-81.
6. 2 process using DEA-MDEA mixtures. Chem. Eng. Res. Des. 2011, 89:1763-1773.
7. 2/EOR: from source to resource. OGJ 1983, 116-122. August 22.
8. Schaffert F.W., Ryan J.M. Koch Process System Inc., Westborough, Mass., Ryan/Holmes technology lands EOR projects. Oil Gas J. 1985, 133-136.
9. Hernández S., Jiménez A. Design of optimal thermally-coupled, distillation systems using a dynamic model. Trans. IChemE 1996, 74:357.
10. Hernández S., Jiménez A. Controllability analysis of thermally coupled distillation systems. Ind. Eng. Chem. Res. 1999, 38:3957.
11. Segovia-Hernández J.G., Hernández S., Jiménez A. A short note about energy efficiency performance of thermally coupled distillation sequences. Can. J. Chem. Eng. 2006, 84(1):139.
12. Segovia-Hernández J.G., Hernández S., Jiménez A. Analysis of dynamic properties of alternative sequences to the Petlyuk column. Comput. Chem. Eng. 2005, 29:1389.
13. Segovia-Hernández J.G., Hernández-Vargas E.A., Márquez-Muñoz J.A. Control properties of thermally coupled distillation sequences for different operating conditions. Comput. Chem. Eng. 2007, 31:867.
14. Wang S.J., Wong D.S.H. Controllability and energy efficiency of a high-purity divided wall column. Chem. Eng. Sci. 2007, 62(4):1010-1025.
15. Tamayo-Galván V.E., Segovia-Hernández J.G., Hernández S., Cabrera-Ruiz J., Alcántara-Ávila J.R. Controllability analysis of alternate schemes to complex column arrangements with thermal coupling for the separation of ternary mixtures. Comput. Chem. Eng. 2008, 32(12):3057-3066.
16. Errico M., Tola G., Rong B.G., Demurtas D., Turunen I. Energy saving and capital cost evaluation in distillation column sequences with a divided wall column. Chem. Eng. Res. Des. 2009, 48:907-920.
17. Ling H., Luyben W.L. New control structure for divided-wall columns. Ind. Eng. Chem. Res. 2009, 48:6034.
18. Ling H., Luyben W.L. Temperature control of the BTX divided-wall column. Ind. Eng. Chem. Res. 2010, 49:189.
19. Bravo-Bravo C., Segovia-Hernández J.G., Gutiérrez-Antonio C., Durán A.L., Bonilla-Petriciolet A., Briones-Ramírez A. Extractive dividing wall column: design and optimization. Ind. Eng. Chem. Res. 2010, 49:3672-3688.
20. He J., Xu B., Zhang W., Zhou C., Chen X. Experimental study and process simulation of n-butyl acetate produced by transesterification in a catalytic distillation column. Chem. Eng. Proc. 2010, 49:132.
21. Damartzis T., Seferlis P. Optimal design of staged three-phase reactive distillation columns using nonequilibrium and orthogonal collocation models. Ind. Eng. Chem. Res. 2010, 49:3275.
22. Chan H., Fair J.R. Prediction of point efficiencies in sieve trays: 1. Binary systems, 2. Multicomponent systems. Ind. Eng. Chem. Proc. Des. Dev. 1984, 23:814.
23. T.H. Chilton, P.A. Colburn, h-f., Sg. Chcm. 26 (1934), 1183.
24. Zuiderweg F.J. Sieve trays: a view on the state of the art. Chem. Eng. Sci. 1982, 37(10):1441-1464.
25. Aspen Technology Aspen Physical Property System: Physical Property Methods, USA 2007.
26. 2 Capture with MEA: Integrating the Absorption Process and Steam Cycle of an Existing Coal-Fired Power Plant 2004, Waterloo, Ontario, Canada, (Master's Thesis).
27. Xu X., Li Y. Comparison between particle swarm optimization, differential evolution and multi-parents crossover. Proceedings of the IEEE International Conference on Computational Intelligence and Security 2007, 124-127. 10.1109/cis.2007.37.
28. Panduco M.A., Brizuela C.A. A comparison of genetic algorithms particle swarm optimization and the differential evolution method for the design of scannable circular antenna arrays. Prog. Electromagnet. Res. B 2009, 13:171-186.
29. Sharma S., Rangaiah G.P. Modeling and optimization of a fermentation process integrated with cell recycling and pervaporation for multiple objectives. Ind. Eng. Chem. Res. 2012, 51:5542-5551.
30. Deb K. Multi-Objective Optimization Using Evolutionary Algorithms 2001, John Wiley & Sons, New York.
31. Turton R., Bailie R.C., Whiting W.B., Shaeiwitz J.A. Analysis, Synthesis and Design of Chemical Process 2009, Prentice Hall, USA, (appendix A). third ed.
32. Skogestad S., Morari M. The dominant time constant for distillation columns. Comput. Chem. Eng. 1987, 11(6):607-617.
33. Klema V.C., Laub A.J. The singular value decomposition: its computation and some applications. IEEE Trans. Automat. Control 1980, 25(2):164-176.
34. Segovia-Hernández J.G., Hernández S., Rico-Ramírez V., Jiménez A. A comparison of the feedback control behavior between thermally coupled and conventional distillation schemes. Comput. Chem. Eng. 2004, 28:811-819.
35. Murrieta-Dueñas R., Gutiérrez-Guerra R., G: Segovia-Hernández J., Hernández S. Analysis of control properties of intensified distillation sequences: reactive and extractive cases. Chem. Eng. Res. Des. 2011, 89:2215-2227.
36. Zavala-Guzmán A., Hernández-Escoto H., Hernández S., Segovia-Hernández J.G. Conventional proportional - integral (PI) control of dividing wall distillation columns: systematic tuning. Ind. Eng. Chem. Res. 2012, 51:10869-10880.
37. Seader J.D., Henley E.J. Separation Process Principles 2006, 27-29. John Wiley & Sons Inc., USA. 2nd ed.
38. 2 emissions and energy consumption of heat-integrated distillation systems. Environ. Sci. Technol. 2005, 39:6860-6870.
39. Natural Gas Supply Association Background 2010, www.naturalgas.org (accessed 02.05.13).
40. 2-ethane azeotrope separation. Chem. Eng. Process. 2010, 10.1016/j.cep.2011.10.001.
41. POGC (Pars Oil and Gas Company) Oil and Gas Processing Plant Design and Operation Training Course Gas Sweetening Processes 2002, www.pogc.ir (accessed 10.04.13).