Abstract
Commercial design programs do not provide a ready-to-use process simulation of tray-by-tray heat-integrated distillation columns, so the computation of the columns using the programs is difficult due to their convergence problem. An approximate procedure for the design of the internally heat-integrated distillation column (HIDiC) is proposed here, and its performance of the design and cost evaluation is demonstrated with two example processes. The approximate design procedure eliminates the artificial heat exchangers and in-tray streams required in the design with the commercial programs, and therefore no information of the exchangers and streams is necessary except the amount of the in-tray heat transfer rate. The economic evaluation indicates that a reduction of the total annual cost of 8.1% is possible with benzene-toluene process and that 59.3% is yielded with the propylene-propane process. The results also demonstrate that the HIDiC is especially efficient for the tight separation system.
Article PDF
Similar content being viewed by others
Avoid common mistakes on your manuscript.
References
C. J. King, Separation processes, 2nd Ed., McGraw-Hill, New York (1980).
R. S. H. Mah and R. B. Wodnik, AIChE J., 23, 651 (1977).
M. Nakaiwa, K. Huang, A. Endo, T. Ohmori, T. Akiya and T. Takamatsu, Chem. Eng. Res. Des., 81, 162 (2003).
K. Kataoka, H. Noda, H. Yamaji, T. Mukaida and M. Kaneda, Proceedings of the 8 th world congress of chemical engineering, Montreal, Canada (2009).
Y. Kansha N. Tsuru, K. Sato, C. Fushimi and A. Tsutsumi, Ind. Eng. Chem. Res., 48, 7682 (2009).
J. P. Schmal, H. J. van der Kooi, A. de Rijke, Z. Olujic and P. J. Jansens, Chem. Eng. Res. Des., 84, 374 (2006).
K. Huang, W. Lui, J. Ma and S. Wang, Ind. Eng. Chem. Res., 49, 1333 (2010).
Y. Wang, K. Huang and S. Wang, Ind. Eng. Chem. Res., 49, 3349 (2010).
Y. H. Kim, Ind. Eng. Chem. Res., 50, 5733 (2011).
Y. H. Kim, Chem. Eng. Res. Des., 89, 2495 (2011).
E.A. Wolff and S. Skogestad, Ind. Eng. Chem. Res., 34, 2094 (1995).
P. B. Shah, Chem. Eng. Prog., 98, 46 (2002).
M.Y. Lee, S.Y. Jeong and Y. H. Kim, Korean J. Chem. Eng., 25, 1245 (2008).
M.Y. Lee, D.W. Choi and Y. H. Kim, Korean J. Chem. Eng., 26, 631 (2009).
K. S. Hwang, B. C. Kim and Y. H. Kim, Korean J. Chem. Eng., 27, 1056 (2010).
S. H. Lee, M. Shamsuzzoha, M. Han, Y.H. Kim and M. Lee, Korean J. Chem. Eng., 28, 348 (2011).
R. Rivero, M. Garcia and J. Urquiza, Energy, 29, 467 (2004).
M. Schaller, K. H. Hoffmann, G. Siragusa, P. Salamon and B. Andresen, Comput. Chem. Eng., 25, 1537 (2001).
G. de Koeijer and R. Rivero, Chem. Eng. Sci., 58, 1587 (2003).
Z. Olujic, L. Sun, A. de Rijke and P. J. Jansens, Energy, 31, 3083 (2006).
Z. Olujic, L. Sun, M. Gadalla, A. de Rijke and P. J. Jansens, Chem. Biochem. Eng., 22, 383 (2008).
B. Suphanit, Energy, 35, 1505 (2010).
M. Gadalla, L. Jimenez, Z. Olujic and P. J. Jansens, Comput. Chem. Eng., 31, 1346 (2007).
J.M. Douglas, Conceptual design of chemical processes, McGraw- Hill, New York (1988).
Y.H. Kim and W. L. Luyben, Chem. Eng. Comm., 128, 65 (1994).
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Kim, Y.H. Approximate design and cost evaluation of internally heat-integrated distillation columns (HIDiCs). Korean J. Chem. Eng. 29, 1004–1009 (2012). https://doi.org/10.1007/s11814-011-0288-x
Received:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s11814-011-0288-x