1 Wang, L.J., Li, X., Zhang, H.J., “Thermodynamic analysis and azeotropic distillation simulation for aceticacid-water-butylacetate system”, Journal of Chemical Industry and Engineering, 56 (7),1260-1266 (2005).(in Chinese) 2 Geng, J., Wu, Y., T., Liu, Q.L., Zhang, Z.B., “The vapor-liquid equilibrium of acetic acid-water system and its simulation of the distillation process”, Journal of Nanjing University, 36 (4), 491-496 (2000). (in Chinese) 3 Kannan, A., Joshi, M.R., Reddy, G.R., Shah, D.M., “Multiple-steady states identification in homogeneous azeotropic distillation using a process simulator”, Industrial and Engineering Chemistry Research,44, 4386-4399 (2005). 4 Rovaglio, M.R., Doherty, M.F., “Dynamics of heterogeneous azeotropic distillation columns”, AIChE, 36 (1), 39-52(1990). 5 Widagdo, S., Seider, W.D., Sebastian, D.H., “Dynamic analysis of heterogeneous azeotropic distillation”, AIChE, 38 (8), 1229-1242 (1992). 6 Chien, I.L., Wang, C.J., Wong, D.S.H., “Dynamics and control of a heterogeneous azeotropic distillation column: Conventional control approzch”, Industrial and Engineering Chemistry Research, 38 (2),468-478 (1999). 7 Chien, I.L., Wang, C.J., Wong, K.S.H., Lee, C.H., Cheng, S.H., Shih, R.F., Liu, W.T., “Experimental investigation of conventional control strategies for a heterogeneous azeotropic distillation column”, Journal of Process Control, 10 (4), 333-340 (2000). 8 Chien, I.L., Zeng, K.L., Chao, H.Y., Liu, J.H., “Design and control of actic acid hydration system via heterogeneous azeotropic distillation”, Chemical Engineering Science, 59 (21), 4547-4567 (2004). 9 Rovaglio, M., Faravelli, T., Biardi, G., Gaffuri, P., Soccol, S., “The key role of entrainer inventory for operation and control of heterogeneous azeotropic distillation column towers”, Computers and Chemical Engineering, 17 (5), 535-547 (1993). 10 Pham, H.N., Doherty, M.F., “Design and synthesis of heterogeneous azeotropic distillations (III) Column sequences”, Chemical Engineering Science, 45 (7), 1845-1854 (1990). 11 Tanaka, S., Yamada, J., “Graphical calculation method for minimum reflux ratio in azeotropic distillation”, Journal of Chemical Engineering of Japan, 5, 20-26 (1972). 12 Siirola, J.J., “An industrial perspective on process synthesis”, AIChE Symp., 91 (304), 222-233 (1995). 13 Wasylkiewicz, S.K., Kobylka, L.C., Castillo, F.J.L., “Optimal design of complex azeotropic distillation columns”, Chemical Engineering Journal, 79 (3), 219-227 (2000). 14 Luyben, M.L., Tyreus, B.D., “An industrial design/control study for the vinyl acetate monomer process”, Computers & Chemical Engineering, 22 (7), 867-877 (1998). 15 Kurooka, T., Yamashita, Y., Nishitani, H., “Multivariable control of a distillation column by exact input-output linearization”, The Symposium of Chemical Engineers, 26 (3), 406-416(2000). (in Japanese) 16 Kurooka, T., Yamashita, Y., Nishitani, H., Hashimoto, Y., Yoshida, M., Numata, M., “Dynamic simulation and nonlinear control system design of a heterogeneous azeotropic distillation column”, Computers and Chemical Engineering, 24 (2), 887-892 (2000). 17 Gaubert, M.A., Gerbaud, V., Joulia, X., Peyrigain, P.S., Pons, M., “Analysis and multiple steady states of an industrial heterogeneous azeotropic distillation”, Industrial and Engineering Chemistry Research, 40 (13), 2914-2924 (2001). 18 Chien, I.L., Chen, W.H., Chang, T.S., “Operation and decoupling control of a heterogeneous azeotropic distillation column”, Computers and Chemical Engineering, 24, 893-899 (2004). 19 Chien, I.L., Kuo, C.L., “Investigating the need of a pre-concentrator column for acetic acid dehydration system via heterogeneous azeotropic distillation”, Chemical Engineering Science, 61, 569-585 (2006). 20 Arifin, S., Chen, I.L., “Combined preconcentrator/recovery column design for isopropyl alcohol dehydration process”, Industrial and Engineering Chemistry Research, 46 (8), 2535-2543 (2007). 21 Lee, H.Y., Huang, H.P., Chien, I.L., “Design and control of an acetic acid dehydration column with p-xylene or m-xylene feed impurity (2) Bifurcation analysis and control”, Industrial and Engineering Chemistry Research, 47 (9), 3046-3059 (2008). 22 Xu, Y., Zhu, Q.X., “Research and implementation of decreasing the acetic acid consumption in purified terephthalic acid solvent system”, Chinese Journal of Chemical Engineering, 16 (4), 650-655 (2008). 23 Fu, J.Q., Phase Equilibrium and Simulation Calculation of Distillation for Special System, China Petrochemical Press, Beijing, 106 (2001). (in Chinese) |