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
相关论文
共 38 条
  • [1] A comprehensive mathematical model for the Fischer-Tropsch synthesis in well-mixed slurry reactors
    Ahón, VR
    Costa, EF
    Monteagudo, JEP
    Fontes, CE
    Biscaia, EC
    Lage, PLC
    [J]. CHEMICAL ENGINEERING SCIENCE, 2005, 60 (03) : 677 - 694
  • [2] FISCHER-TROPSCH REACTION MECHANISM INVOLVING STEPWISE GROWTH OF CARBON CHAIN
    ANDERSON, RB
    FRIEDEL, RA
    STORCH, HH
    [J]. JOURNAL OF CHEMICAL PHYSICS, 1951, 19 (03) : 313 - 319
  • [3] ANDERSON RB, 1956, CATALYSTS FISCHERTRO, V4, P337
  • [4] [Anonymous], CHEM IND NY
  • [5] Novel correlations for gas holdup in large-scale slurry bubble column reactors operating under elevated pressures and temperatures
    Behkish, A
    Lemoine, R
    Oukaci, R
    Morsi, BI
    [J]. CHEMICAL ENGINEERING JOURNAL, 2006, 115 (03) : 157 - 171
  • [6] Prediction of the gas holdup in industrial-scale bubble columns and slurry bubble column reactors using back-propagation neural networks
    Behkish, A
    Lemoine, R
    Sehabiague, L
    Oukaci, R
    Morsi, B
    [J]. INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2005, 3
  • [7] Mass transfer characteristics in a large-scale slurry bubble column reactor with organic liquid mixtures
    Behkish, A
    Men, ZW
    Inga, JR
    Morsi, BI
    [J]. CHEMICAL ENGINEERING SCIENCE, 2002, 57 (16) : 3307 - 3324
  • [8] Gas holdup and bubble size behavior in a large-scale slurry bubble column reactor operating with an organic liquid under elevated pressures and temperatures
    Behkish, Arsam
    Lemoine, Romain
    Sehabiague, Laurent
    Oukaci, Rachid
    Morsi, Badie I.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2007, 128 (2-3) : 69 - 84
  • [9] Influence of syngas composition on the transient behavior of a Fischer-Tropsch continuous slurry reactor
    Bremaud, M
    Fongarland, P
    Anfray, J
    Jallais, S
    Schweich, D
    Khodakov, AY
    [J]. CATALYSIS TODAY, 2005, 106 (1-4) : 137 - 142
  • [10] ON THE FORMATION AND COMPOSITION OF THE LIQUID-PHASE IN FISCHER-TROPSCH REACTORS
    CALDWELL, L
    VANVUUREN, DS
    [J]. CHEMICAL ENGINEERING SCIENCE, 1986, 41 (01) : 89 - 96