1Cheng Z M, Anter A M, Yuan W K. Intensification of phase transition on multiphase reactions[J]. AIChEJ, 2001, 47(5): 1185-1192.
2Hanika J. Safe operation and control of trickle-bed reactor[J]. Chem Eng Sci, 1999, 54: 4653-4659.
3Khadilkar M R, Mills P L, Dudukovic M P. Trickle-bed reactor models for systems with a volatile liquid phase[J]. Chem Eng Sci, 1999, 54: 2421-2431.
4Kheshgi H S, Reyes S C, Hu R, et al. Phase transion and steady-state multiplicity in a trickle-bed reactor[J]. Chem Eng Sci, 1992, 47, 1771.
5Hanika J, Lukjanov B N, Kirillov V A, et al. Hydrogenation of 1,5-cyclooctadiene in a trickle bed reactor accompanied by phase transition[J]. Chem Eng Commun, 1986, 40: 183.
6程振民, 袁渭康, Anter A M, 等. 相变法苯加氢制备环己烷工艺[P]. CN: 1271711A, 2000-11-01. (Cheng Zh M, Yuan W K, Anter A M, et al. Benzene hydrogenation into cyclohexane via phase transition[P]. CN: 1271711A, 2000-11-01.)
8Cheng Z M, Anter A M, Khalifa G M, et al. An innovative reaction heat offset operation for a multiphase fixed bed reactor dealing with volatile compounds[J]. Chem Eng Sci, 2001, 56(21-22): 6025-6030.
9Jaguste D N, Bhatia S K. Partial internal wetting of catalyst particles: hysteresis effects[J]. AIChE, 1991, 37: 650.
9Yaws C L. Chemical Properties Handbook. New York: McGraw-Hill, 1999.
10Kim D H, Kim Y G. An experimental study of multiple steady states in a porous catalyst due to phase transition.Journal of Chemical Engineering of Japan, 1981,14(4):311-317.
