[1] D.B. Kaymak, W.L. Luyben, A quantitative comparison of reactive distillation with conventional multi-unit reactor/column/recycle systems for different chemical equilibrium constants, Ind. Eng. Chem. Res. 43 (2004) 2493-2507. [2] Yeong-Tarng Tang, Yi-Wei Chen, Hsiao-Ping Huang, Cheng-Ching Yu, Design of reactive distillations for acetic acid esterification, AICHE J. 51 (2005) 683-1699. [3] Shih-Bo Hung, Ming-Jer Lee, Control of different reactive distillation configurations, AICHE J. 52 (2006) 1423-1441. [4] D.B. Kaymak, W.L. Luyben, Quantitative comparison of dynamic controllability between a reactive distillation column and a conventional multi-unit process, Comput. Chem. Eng. 32 (2008) 1456-1470. [5] M.A. Al-Arfaj,W.L. Luyben, Comparison of alternative control structures for an ideal two-product reactive distillation column, Ind. Eng. Chem. Res. 39 (2000) 3298-3307. [6] M.A. Al-Arfaj, W.L. Luyben, Comparative control study of ideal and methyl acetate reactive distillation, Chem. Eng. Sci. 57 (2002) 5039-5050. [7] Yu-Cheng Cheng, Cheng-Ching Yu, Effects of feed tray locations to the design of reactive distillation and its implication to control, Chem. Eng. Sci. 60 (2005) 4661-4677. [8] G. Sunar, D.B. Kaymak, Effect of Feed Tray Location on Temperature-based Inferential Control of Double Feed Reactive Distillation Columns, Ind. Eng. Chem. Res. 48 (2009) 11071-11080. [9] Chin-Shih Chen, Cheng-Ching Yu, Effects of relative volatility ranking on design and control of reactive distillation systems with ternary decomposition reactions, Ind. Eng. Chem. Res. 47 (2008) 4830-4844. [10] I-Kuan Lai, Shih-Bo Hung, Wan-Jen Hung, Cheng-Ching Yua, Ming-Jer Lee, Hsiao- Ping Huang, Design and control of reactive distillation for ethyl and isopropyl acetates production with azeotropic feeds, Chem. Eng. Sci. 62 (2007) 878-898. [11] O. Sokolov, M.D. Hurley, T.J. Wallington, E.W. Kaiser, Kinetics and mechanism of the gas-phase reaction of Cl atoms with benzene, J. Phys. Chem. A 102 (1998) 1671-1681. [12] Zezhang Sheng, Shan Li, Mifen Cui, Study on macrokinetics of benzene chlorination boiling state, J. Nanjing Univ. Chem. Technol. 19 (9) (1997) 8-13 (in Chinese). [13] Lianghui Ding, Jihai Tang,Mifen Cui, Cuimei Bo, Qiao Xu, Optimumdesign and analysis based on independent reaction amount for distillation column with side reactors: production of benzyl chloride, Ind. Eng. Chem. Res. 50 (2011) 1143-1152. [14] B.O. Cuimei, T.A.N.G. Jihai, B.A.I. Yangjin, Q.I.A.O. Xu, D.I.N.G. Lianghui, Z.H.A.N.G. Shi, The design and control of distillation column with side reactors for chlorobenzene production, Chin. J. Chem. Eng. 20 (6) (2012) 1113-1120. [15] Yu-De Lin, Hsiao-Ping Huang, Cheng-Ching Yu, Relay feedback tests for highly nonlinear processes: reactive distillation, Ind. Eng. Chem. Res. 45 (2006) 4081-4092. [16] Cuimei Bo, Jihai Tang, Mifen Cui, Kangkang Feng, Xu Qiao, Furong Gao, Control and profile setting of reactive distillation column for benzene chloride consecutive reaction system, Ind. Eng. Chem. Res. 52 (49) (2013) 17465-17474. [17] L.Ü.Wenxiang, Z.H.U. Ying, H.U.A.N.G. Dexian, J.I.A.N.G. Yongheng, J.I.N. Yihui, A new strategy of integrated control and on-line optimization on high-purity distillation process, Chin. J. Chem. Eng. 18 (1) (2010) 66-79. |