| [ 1 ] 李大东. 加氢处理工艺与工程[ M ]. 北京:中国石化出版社,2004.
[ 2 ] Shin S S. Mobil’S OTGAINTM process for gasoline quality attai-
nment [ C ]. NPRA Annual Meeting, 1999.
[ 3 ] 涂先红,方向晨,赵乐平. FCC汽油加氢脱硫降烯烃技术进展[ J ]. 当代化工,2006,35( 2 ):114 - 116.
[ 4 ] Ojeda J A, Ramirez J, Krishna R. Hydrodesulphurization of gasoils: Advantages of counter-Current gas-Liquid contacting [ J ]. Com-
puter Aided Chemical Engineering, 2002( 10 ): 277 - 282.
[ 5 ] Trambouze P. Countercurrent two-phase flow fixed bed catalytic reactors[ J ]. Chemical Engineering Science, 1990, 45( 8 ): 2 269 - 2 275.
[ 6 ] JAKOBSSON K, HASANEN A, AITTAMAA J. MODELLING OF A COUNTERCURRENT HYDROGENATION PROCESS[ J ]. Chemical Engineering Research and Design, 2004( 82 ): 203 - 207.
[ 7 ] 宋永一,沈美庆,方向晨,等. 柴油逆流加氢超深度脱硫脱芳烃技术的研究和开发[ J ]. 石油炼制与化工,2006,37( 4 ):1 - 5.
[ 8 ] Fabia′n S. Mederos, Jorge Ancheyta. Mathematical modeling and simulation of hydrotreating reactors: Cocurrent versus countercur-
rent operations[ J ]. Applied Catalysis A: General, 2007 ( 332 ): 8 - 21.
[ 9 ] 李大东. 加氢处理工艺与工程[ M ]. 北京:中国石化出版社,2004.
[ 10 ] Van Hasselt B W, Lindenbergh D J, Calis H P, et al. The three-
levels-of-porosity reactor. A novel reactor for countercurrent trickle-flow processes [ J ]. Chemical Engineering science, 1997
( 52 ): 3 901 - 3 907.
[ 11 ] Van Hasselt B W, Calis H P, Sie S T, et al. Gas-liquid mass transfer characteristics of the three-levels-of-porosity reactor [ J ]. Chemical Engineering Science, 2001( 56 ): 531 - 536.
[ 12 ] Higler A P, Krishna R, Ellenberger J, et al. Counter-current ope-ration of a structured catalytically packed-bed reactor:Liquid phase mixing and mass transfer[ J ]. Chemical Engineering Science, 1999( 54 ): 5 145 - 5 152.
[ 13 ] Lebens P J M, vander Meijden R, Edvinsson R K,et al. Hydrody - namics of gas-liquid countercurrent flow in internally finned monolithic structures [ J ]. Chemical Engineering Science, 1997 ( 52 ): 3 893 - 3 899.
[ 14 ] Lebens P J M, Kapteijn F, Sie S T, etal. Potentials of inter-nally finned monoliths as a packing for multifunctional reactors[ J ]. Chemical Engineering Science, 1999( 54 ): 1 359 - 1 365.
[ 15 ] van Hasselt B W, Lebens P J M, Calis H P A, et al. A numerical comparison of alternative three-phase reactors with a conventional trickle-bed reactor. The advantages of countercurrent flow for hydrodesulfurization[ J ]. Chemical Engineering Science, 1999( 54 ): 4 791 - 4 799.
[ 16 ] 方向晨,程振民,穆 斌,等. 四叶形催化载体材料的流体力学性质[ J ]. 高校化学工程学报,2006,20( 2 ):292 - 295.
[ 17 ] Han M H, Lin H F, Yuan Y H. Pressure drop for two phase counter
-current flow in a packed column with a novel internal[ J ]. Chemical Engineering Journal, 2003( 94 ): 179 - 187.
[ 18 ] Breijer A J, John Nijenhuis, Ruud van Ommen J. Prevention of flooding in a countercurrent trickle-bed reactor using additional void space[ J ]. Chemical Engineering Journal, 2008( 138 ): 333 - 340.
[ 19 ] 方向晨. 一种固定床气液逆流反应器的操作方法: CN,1552511[ P ]. 2004 - 12 - 08.
[ 20 ] 杨福利. 一种气液逆流式反应器: CN,2 761 258[ P ]. 2006 - 03 - 01.
[ 21 ] 张志华. 一种气液逆流式反应器:CN,2 726 713[ P ]. 2004 - 09 - 11.
[ 22 ] 李 扬. 气液逆流反应器和气液逆流加氢工艺方法 :CN,102 039 105[ P ]. 2011 - 05 - 04.
[ 23 ] Ramesh Gupta. COUNTERCURRNT REACTION VESSEL US6 007 787[ P ]. 1999 - 12 - 28.
[ 24 ] Ramesh Gupta. HYDROPROCESSING IN A COUNTERCURR-
ENT REACTION VESSEL: US,5 985 131[ P ]. 199 - 11 - 16.
[ 25 ] ZAPKE A, KROGER D G. THE INFLUENCE OF FLUID PRO-
PERTIES AND INLET GEOMETRY ON FLOODING IN VERTICAL AND INCLINED TUBES[ J ]. Multiphase Flow, 1996
( 22 ): 461 - 472.
[ 26 ] Wallis G B. Air-water countercurrent annular flow[ J ]. Int J Multiphase Flow, 1983( 9 ): 349 - 366.
[ 27 ] Mishima K, Nishihara. Flooding velocities for countercurrent air- water flow in thin rectangular channels[ J ]. Annu Rep Res Reactor Inst, 1984( 17 ): 1 - 14.
[ 28 ] Hewitt GF. In search of two-phase flow, Lecture[ C ]. 30th US National Heat Transfer Conference, 1995. |