Genetic algorithm strategy (GA) for optimization of a novel dual-stage slurry bubble column membrane configuration for Fischer–Tropsch synthesis in gas to liquid (GTL) technology
暂无分享,去创建一个
[1] Rajamani Krishna,et al. Multicomponent reaction engineering model for Fe-catalyzed Fischer-Tropsch synthesis in commercial scale slurry bubble column reactors , 1999 .
[2] Rajamani Krishna,et al. Modelling of a bubble column slurry reactor for Fischer Tropsch synthesis , 1999 .
[3] Mohammad Reza Rahimpour,et al. Enhancement of gasoline production in a novel hydrogen- permselective membrane reactor in Fischer-Tropsch synthesis of GTL technology , 2009 .
[4] V. Parmon,et al. Performance of a catalytic membrane reactor for the Fischer–Tropsch synthesis , 2005 .
[5] Catalytic CO hydrogenation on potassic Fe/zeolite LTL , 2002 .
[6] Morteza Sohrabi,et al. Fischer‐Tropsch Synthesis: Modeling and Performance Study for Fe‐HZSM5 Bifunctional Catalyst , 2005 .
[7] Shigeki Hara,et al. Kinetics and hydrogen removal effect for methanol decomposition , 1999 .
[8] M. Dry,et al. The Fischer–Tropsch process: 1950–2000 , 2002 .
[9] Hanning Li,et al. Influence of slurry concentrations on bubble population and their rise velocities in a three-phase slurry bubble column , 2000 .
[10] F. Fernandes. Modeling and Product Grade Optimization of Fischer−Tropsch Synthesis in a Slurry Reactor , 2006 .
[11] Ulrich Kunz,et al. Reactors for Fischer‐Tropsch Synthesis , 2008 .
[12] J. Kuipers,et al. Development of a membrane-assisted fluidized bed reactor - 1 - Gas phase back-mixing and bubble-to-emulsion phase mass transfer using tracer injection and ultrasound experiments , 2005 .
[13] Rubens Maciel Filho,et al. Dynamic modelling of a three-phase catalytic slurry reactor , 2001 .
[14] V. Parmon,et al. Fischer–Tropsch synthesis using plug-through contactor membranes based on permeable composite monoliths. Selectivity control by porous structure parameters and membrane geometry , 2005 .
[15] Ying Liu,et al. Modeling of the Fischer-Tropsch synthesis in slurry bubble column reactors , 2008 .
[16] Frerich J. Keil,et al. Large-scale spherical fixed bed reactors: Modeling and optimization , 1993 .
[17] Klaus-Viktor Peinemann,et al. Membrane Technology: in the Chemical Industry , 2001 .
[18] Milorad P. Dudukovic,et al. Modeling of the Fischer-Tropsch synthesis in slurry bubble column reactors , 2003 .
[19] W. Deckwer,et al. Modeling the Fischer-Tropsch synthesis in the slurry phase , 1982 .
[20] Edward L Cussler,et al. Diffusion: Mass Transfer in Fluid Systems , 1984 .
[21] R. Reid,et al. The Properties of Gases and Liquids , 1977 .
[22] A. M. Adris,et al. Economics and simulation of fluidized bed membrane reforming , 1998 .
[23] M. Rahmani,et al. Mathematical Modeling of Fischer-Tropsch Synthesis in an Industrial Slurry Bubble Column , 2009 .
[24] Giuseppe Barbieri,et al. Simulation of the methane steam re-forming process in a catalytic Pd-membrane reactor , 1997 .
[25] M. Tadé,et al. Chemical Product and Process Modeling Modern Trends in CFD Simulations : Application to GTL Technology , 2011 .
[26] Morteza Sohrabi,et al. A comparison between two kinds of hydrodynamic models in bubble column slurry reactor during Fischer–Tropsch synthesis: Single-bubble class and two-bubble class , 2009 .
[27] F. Kapteijn,et al. Water vapour separation from permanent gases by a zeolite-4A membrane , 2005 .
[28] Evaristo C. Biscaia,et al. A comprehensive mathematical model for the Fischer-Tropsch synthesis in well-mixed slurry reactors , 2005 .
[29] Thomas Turek,et al. Comparison of different reactor types for low temperature Fischer–Tropsch synthesis: A simulation study , 2009 .
[30] N. Itoh,et al. Hydrogen transport from gas to liquid phase through a palladium membrane , 1997 .
[31] J. Marano,et al. Characterization of Fischer-Tropsch liquids for vapor-liquid equilibria calculations , 1997 .
[32] F. Kapteijn,et al. Fischer–Tropsch synthesis with in situ H2O removal – Directions of membrane development , 2008 .
[33] Hongwei Xiang,et al. Modeling of catalyst pellets for Fischer-Tropsch synthesis , 2001 .
[34] M. M. Montazer Rahmati,et al. RATE EQUATIONS FOR THE FISCHER-TROPSCH REACTION ON A PROMOTED IRON CATALYST , 2001 .
[35] J. M. Schweitzer,et al. Reactor Modeling of a Slurry Bubble Column for Fischer-Tropsch Synthesis , 2009 .
[36] Yi-Ning Wang,et al. Heterogeneous modeling for fixed-bed Fischer–Tropsch synthesis: Reactor model and its applications , 2003 .
[37] R. Krishna,et al. Simulation of the transient and steady state behaviour of a bubble column slurry reactor for Fischer–Tropsch synthesis , 2002 .
[38] M. El‐Halwagi,et al. Simulation, integration, and economic analysis of gas-to-liquid processes , 2010 .
[39] F. Larachi,et al. Dimethyl Ether Synthesis with in situ H2O Removal in Fixed-Bed Membrane Reactor: Model and Simulations† , 2010 .
[40] O. Levenspiel. Chemical Reaction Engineering , 1972 .
[41] Mohammad Reza Rahimpour,et al. Optimization of a novel combination of fixed and fluidized-bed hydrogen-permselective membrane reactors for Fischer–Tropsch synthesis in GTL technology , 2009 .
[42] M. Menéndez,et al. Use of membranes in fischer-tropsch reactors , 2000 .
[43] Bernard P. A. Grandjean,et al. Methane steam reforming in asymmetric Pd- and Pd-Ag/porous SS membrane reactors , 1994 .
[44] Mohammad Reza Rahimpour,et al. A comparative study of combination of Fischer–Tropsch synthesis reactors with hydrogen-permselective membrane in GTL technology , 2009 .