Optimal Design of Multistage Flash Desalination Process Based on the Modified Genetic Algorithm (MGA)

Article Preview

Abstract:

In this paper, a rigorous mathematical model of multistage flash system (MSF) is presented based on a detailed physicochemical representation of the process, including all the fundamental elementary phenomena. In particular, Comparison to the mathematical model of reference, two integer variables, which are the number of recovery stage (NR) and the number of rejection stage (NJ), are introduced to the model. Additionally, two special variables, which are the ratio of recirculation brine water flow rate and distillation flow rate and the ratio of make-up flow rate and the distillation flow rate, are introduced to the model as the continuous variables too. Then, the MSF system is described as a mixed-integer nonlinear programming (MINLP). The objective is to minimize the total annual cost (TAC), which is mainly composed of the operating costs and investment cost. Here the modified genetic algorithm (MGA), which is characterized as mixing coding way, is adopted for the system optimization. A case study and a discussion of the results are presented.

You might also be interested in these eBooks

Info:

Periodical:

Advanced Materials Research (Volumes 233-235)

Pages:

1044-1049

Citation:

Online since:

May 2011

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2011 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] M.A. Soliman, J. Eng. Sci., 7, 2–10(1981).

Google Scholar

[2] M.A. Darwish, Desalination, 85, 59–79 (1991).

Google Scholar

[3] H.T. El-Dessouky, I., Desalination, 115,155–179 (1998).

Google Scholar

[4] Salah Al-Hengarim, Mohamed El-Bousiffi, Walid El-Mudir, desalination, 182, 73-85(2005).

DOI: 10.1016/j.desal.2005.03.010

Google Scholar

[5] Sommariva, C.; Pinciroli, D.; Sciubba, E.; Lior, N., Proceedings, IDA World Congress on Desalination and Water Reuse, San Diego, CA, Vol. 1, 65-75(1999)..

Google Scholar

[6] El-Dessouky, H.; Alatiqi, I.; Ettouney, H., Desalination, 115, 155-179( 1998).

DOI: 10.1016/s0011-9164(98)00035-6

Google Scholar

[7] Mussati, S.; Aguirre, P.; Scenna, N., Lat. Am.Appl. Res., 33, 141-147( 2003).

Google Scholar

[8] Mussati, S.; Aguirre, P.; Scenna, N., Desalination, 138, 341-347(2001).

DOI: 10.1016/s0011-9164(01)00283-1

Google Scholar

[9] Sergio F. Mussati, Pio A. Aguirre and Nicolas J. Scenna, Ind. Eng. Chem. Res., 45,7190-7203(2006)

DOI: 10.1021/ie051053y

Google Scholar

[10] M. Mazzotti, M. Rosso, A. Beltramini and M. Morbidelli, Desalination, 127, 207–218 (2000).

DOI: 10.1016/s0011-9164(00)00011-4

Google Scholar

[11] M.F. Falcetta and E. Sciubba, Desalination, 122, 263–269 (1999).

Google Scholar

[12] I. Kamal, Desalination, 114, 233–240 (1997).

Google Scholar

[13] P. Fiorini and E. Sciubba, Desalination, 182, 39–48(2005).

Google Scholar

[14] Nabil M. Abdel-Jabber, Hazim Mohameed Qiblawey, Farouq S. Mjalli, Hisham Ettouney, Desalination, 204,501-514(2007).

DOI: 10.1016/j.desal.2006.02.047

Google Scholar