The role of vapour-liquid equilibrium in Fischer-Tropsch product distribution

被引:28
作者
Masuku, Cornelius Mduduzi [1 ]
Hildebrandt, Diane [1 ]
Glasser, David [1 ]
机构
[1] Univ Witwatersrand, Ctr Mat & Proc Synth, Sch Chem & Met Engn, ZA-2050 Wits, South Africa
关键词
Fischer-Tropsch reaction; Vapour-liquid equilibrium (VLE); Phase equilibria; Product distribution model; Chain propagation probability (alpha); ASF; BUBBLE-COLUMN REACTOR; ALPHA-OLEFIN READSORPTION; SLURRY REACTOR; CHAIN-LENGTH; GAS HOLDUP; ELEVATED PRESSURES; ORGANIC LIQUID; IRON CATALYSTS; SELECTIVITY; HYDROCARBONS;
D O I
10.1016/j.ces.2011.09.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work uses vapour-liquid equilibrium (VLE) to explain the observed two-alpha product distribution in Fischer-Tropsch (FT) reactors. We discuss three possible scenarios or cases of Anderson-Schulz-Flory (ASF) product distribution and VLE. The three cases assume the following: (1) the reaction sets up a single alpha ASF distribution in the total (vapour+liquid) products, (2) the vapour phase follows a single alpha distribution and (3) a single alpha distribution is set up in the liquid phase. We then look at the consequences of these assumptions in conjunction with a simple Raoult's law VLE model on the exit product distributions. We find that only Case 3 gives rise to a two-alpha model in accordance with experimental results that is frequently observed in FT reactors. This model further predicts a relationship between the two values of alpha that are consistent with the measured experimental results. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:6254 / 6263
页数:10
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