Zhu Baoxing(朱宝兴), Li Laifeng(李来风), Lin Hong(林宏), Han Wei(韩伟), Tan Douping(谭都平), Zhang Feng(张峰). Industrial sideline evaluation of a new catalyst for C3 fraction liquid phase selective hydrogenation[J]. Chem. Ind. Eng. Prog.(化工进展), 2012, 31(6): 1379-1382
[2]
Zhang Shizhong(张世忠), Dai Wei(戴伟), Qi Dongsheng(齐东升), Peng Hui(彭晖), Wei Guobin(卫国宾). Industrial application of a new catalyst for C3 fraction liquid phase selective hydrogenation[J]. Chem. Ind. Eng. Prog.(化工进展), 2008, 27(3): 464-467
[3]
Cheng Guangwei(程广伟). Analysis and handling of operating fluctuation of C3 hydrogenation in ethylene plant[J]. Chem. Ind. Eng. Prog.(化工进展), 2012, 31(suppl.2): 256-259
[4]
Arganbright R P. Hydroisomerization process[P]: US, 5087780. 1992-02-11
[5]
Gao Buliang(高步良), Cheng Zhenmin(程振民), Zhang Lian(张濂), Yuan Weikang(袁渭康). Effect of the catalyst packing structure on the selective hydrogenation of C3 distillate by catalytic distillation[J]. Chem. Ind. Eng. Prog.(化工进展), 2004, 23(10): 1121-1124
[6]
Brugm A J. Fractional distillation of liquid mixtures[P]: NL, 41850. 1937
[7]
Petlyuk F B, Platonov V M. Thermodynamically optimal method for separating multi component mixtures[J]. Int. Chem. Eng., 1965, 5(3): 555-561
[8]
Fidkowski Z T, Krolikowski L. Thermally coupled system of distillation columns: optimization procedure[J]. AIChE J., 1986, 32(4): 537-546
[9]
Fidkowski Z T, Krolikowski L. Minimum energy requirement of thermally coupled distillation systems[J]. AIChE J., 1987, 33(4): 643-653
[10]
Ilkka Malinen, Juha Tanskanen. Thermally coupled side-column configurations enabling distillation boundary crossing(Ⅰ): An overview and a solving procedure[J]. Ind. Eng. Chem. Res., 2009, 48(13): 6387-6404
[11]
Ilkka Malinen, Juha Tanskanen. Thermally coupled side-column configurations enabling distillation boundary crossing(Ⅱ): Effects of intermediate heat exchangers[J]. Ind. Eng. Chem. Res., 2009, 48(13): 6372-6386
[12]
Kiss Anton A, Pragt J J. Reactive dividing-wall columns—how to get more with less resources?[J]. Chemical Engineering Communications, 2009, 196(11): 1366-1374
[13]
Fernando Israel Gomez-Casto. Feasibility study of a thermally coupled reactive distillation process for biodiesel production[J]. Chemical Engineering and Processing, 2010, 49(3): 262-269
[14]
Hernández S, Sandoval-Vergara R, Barroso-Mu？oz F O, Murrieta-Due？as R, Hernández-Escoto H, Segovia-Hernández J G, Rico-Ramirez V. Reactive dividing wall distillation columns: simulation and implementation in a pilot plant[J]. Chemical Engineering and Processing, 2009, 48(1): 250-258
[15]
Hakan Uygur, Suheyda Atalay, Tunc O Savasci. Kinetics of liquid phase selective hydrogenation of methylacetylene and propadiene in C3 streams[J]. Journal of Chemical Engineering of Japan, 1998, 31(2):178-186
[16]
Yu Zaiqun(于在群), Gao Buliang(高步良), Jia Yinghua(贾颖华). Mathematical model for selective hydrogenation of C3 streams in a catalytic distillation column[J]. Chemical Reaction Engineering and Technology(化学反应工程与工艺), 2002, 18(1): 12-17
[17]
Yu Zaiqun(于在群), Gao Buliang(高步良), Xu Jinmei(徐金梅), Zhang Jinyong(张金永). Kinetic study of C3 cut liquid-phase selective hydrogenation over supported metal catalyst[J]. Industrial Catalysis, 2002, 10(5): 11-16
[18]
Yu Zaiqun(于在群), Zhu Honglin(朱宏林). Simulation and analysis of C3 hydrogenation reactor[J]. Petrochemical Technology(石油化工), 2002, 31(5): 376-379
[19]
Wang Yufei(王宇飞), Wang Jing(王婧), Lin Dongfeng(林东风). Simulation of a novel catalytic distillation coupling process for propylene purification[J]. Petrochemical Technology(石油化工), 2012, 14(8): 880-884
[20]
Finn A J. Rapid assessment of thermally coupled side columns[J]. Gas Sep. Purif., 1996, 10(3): 169-175
