[1] Rathore, R.N.S., van Wormer, K.A., Powers, G.J., "Synthesis strategies for multicomponent separation systems withenergy integration", AIChE J., 20, 491 (1974a). [2] Andrecovich, M.J., Westerberg, A.W., "An MILP formulation for heat integrated distillation sequence synthesis",AIChE J., 31, 1461 (1985b). [3] Floudas, C.A., Paules, G.E., "A mixed integrated nonlinear programming formulation for the synthesis of heat integrated distillation sequences", Computer chem. Engng.,12, 531 (1988). [4] Wang, K.F., Qian, Y., "Synthesis and optimization of heatintegrated distillation systems using an improved geneticalgorithm", Computer Chem. Engng., 23, 125 (1998). [5] Petlyuk, F.B., Platonov, C.M., Slavinskii, D.M., "Thermodynamically optimal method for separating multicomponent mixtures", International Chemical Engineering, 5,555 (1965). [6] Carlberg, N.A., Westerberg, A.W., "Temperature heat diagrams for complex columns (2) Underwood’s method forside strippers and enrichers", Ind. Engng. Chem. Res., 28,1379 (1989). [7] Glinos, K., Malone, M.F., "Optimality regions for complexcolumn alternatives in distillation systems", Ind. Engng.Chem. Res., 66, 229-240 (1988). [8] Floquet, P., Pibouleau, L., Domenech, S., "Separation sequenecs synthesis: How to use simulated annealing procedure?", Computer Chem. Engng., 18, 1141 (1994). [9] Chen, Z.Z., Yuan, X.G., Chen, L., "Synthesis of heat integrated complex column distillation system via SA basedmethod", Computer and Applied Chemistry, 14 (Sup.), 189 (1997). (in Chinese) [10] Metropolis, N., Rosenbluth, A., Rosenbluth, M., Teller, A.,Teller, E., "Equation of state calculations by fast computingmachines", Journal of Chemical Physics, 21, 1087-1092 (1953). [11] Kirkpatrick, S., Gelatt, C.D., Vecchi, M.P., "Optimizationby simulated annealing", Science, 220, 671-680 (1983). [12] Chen, Z.Z., Yuan, X.G., Zhong, Z.J., "Synthesis of heatintegrated nonsharp distillation sequence", Computer andApplied Chemistry, 14 (4), 247 (1997). (in Chinese) [13] Agrawal, R., "Synthesis of distillation column configurations for a mulitcomponent separation", Ind. Engng.Chem. Res., 35, 1059-1071 (1996). [14] Rong, B.G., Kraslawski, A., Nystrom, L., "Design andsynthesis of multicomponent thermally coupled distillation flowsheets", Computer Chem. Engng., 25, 807-820(2001). [15] Horowitz, E., Sahni, S., Mehta, D., Fundamentals of DataStructures in C++", W. H. Freeman, New York (1995). [16] Guthrie, K.M., "Capital cost estimating", Chem. Engng.,24, 114-135 (1969). [17] Douglas, J.M., "Conceptual Design of Chemical Processes",McGraw-Hill, New York (1988). [18] Yuan, X.G., Chen, Z.Z., "A hybrid global optimizationmethod for design of batch chemical processes", ComputerChem. Engng., 21, (Sup.), 8685-S690 (1997). [19] Cardoso, M.F., Salcedo, R.L., de Azevedo, S.F., "A simulated annealing approach to the solution of MINLP problems", Computer Chem. Engng., 21, 1349-1364 (1997). [20] Seader, J.D., Westerberg, A.W., "A combined heuristic andevolutionary strategy for synthesis of simple separation sequences", AIChE J, 23, 951 (1977). [21] Mezsey, P., Fonyo, Z., "A new bounding strategy for synthesizing distillation schemes with energy integration", Computer Chem. Engng., 10, 545-550 (1986).
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