Theoretical analysis of the effect of catalyst mass distribution and operation parameters on the performance of a Pd-based membrane reactor for water–gas shift reaction

[1]  Jam Hans Kuipers,et al.  Modelling of packed bed membrane reactors for autothermal production of ultrapure hydrogen , 2006 .

[2]  Optimization of the active component distribution through the catalyst bed for the case of adiabatic reactor , 2005 .

[3]  W. Ho,et al.  Modeling of CO2-selective water gas shift membrane reactor for fuel cell , 2005 .

[4]  Akira Endo,et al.  Simulation of a Porous Ceramic Membrane Reactor for Hydrogen Production , 2005 .

[5]  Modelling a catalytic membrane reactor with plug flow pattern and a hypothetical equilibrium gas-phase reaction with Δn ≠ 0 , 2005 .

[6]  R. Hughes,et al.  The catalytic dehydrogenation of isobutane to isobutene in a palladium/silver composite membrane reactor , 2005 .

[7]  A. Seidel-Morgenstern,et al.  Compatibility of hydrogen transfer via Pd-membranes with the rates of heterogeneously catalysed steam reforming , 2005 .

[8]  Sungwon Hwang,et al.  Heterogeneous catalytic reactor design with optimum temperature profile I: application of catalyst dilution and side-stream distribution , 2004 .

[9]  A. Mendes,et al.  Modeling a dense polymeric catalytic membrane reactor with plug flow pattern , 2003 .

[10]  V. Violante,et al.  Pd-Ag Membrane Reactors for Water Gas Shift Reaction , 2003 .

[11]  C. Fukuhara,et al.  Two-Dimensional Simulation of a Membrane Reactor for Dehydrogenation of Ethylbenzene, Considering Heat and Mass Transfer , 2003 .

[12]  L. Lorenzen,et al.  The Dehydrogenation of 2-butanol in a Pd-Ag Membrane Reactor. , 2002 .

[13]  Mario Conte,et al.  Hydrogen economy for a sustainable development: state-of-the-art and technological perspectives , 2001 .

[14]  V. Violante,et al.  Experimental and simulation of both Pd and Pd/Ag for a water gas shift membrane reactor , 2001 .

[15]  Roland Dittmeyer,et al.  Membrane reactors for hydrogenation and dehydrogenation processes based on supported palladium , 2001 .

[16]  E. Drioli,et al.  An analysis of the performance of membrane reactors for the water–gas shift reaction using gas feed mixtures , 2000 .

[17]  R. Bagatin,et al.  Fixed bed reactors , 1999 .

[18]  Donald J. Chmielewski,et al.  Conversion targets for plug flow membrane reactors , 1999 .

[19]  Geert Versteeg,et al.  High-temperature membrane reactors: potential and problems , 1999 .

[20]  Jan Galuszka,et al.  Methane conversion to syngas in a palladium membrane reactor , 1998 .

[21]  M. Tekić,et al.  Non-isothermal two-membrane reactors for reversible gas phase reactions , 1998 .

[22]  M. Tekić,et al.  Applicability of two-membrane reactors for reversible gas phase reaction. Effects of flow patterns and inerts , 1997 .

[23]  Naotsugu Itoh,et al.  An adiabatic type of palladium membrane reactor for coupling endothermic and exothermic reactions , 1997 .

[24]  Optimal distribution of catalyst for a case involving heterogeneous and homogeneous reactions , 1997 .

[25]  R. Hughes,et al.  Ethane dehydrogenation in a catalytic membrane reactor coupled with a reactive sweep gas , 1995 .

[26]  A. Chakma,et al.  A simulation study on the thermal decomposition of hydrogen sulfide in a membrane reactor , 1995 .

[27]  K. P. Jong,et al.  Carbon: Hydrogen Carrier or Disappearing Skeleton? , 1995 .

[28]  N. Itoh,et al.  Radial mixing diffusion of hydrogen in a packed-bed type of palladium membrane reactor , 1994 .

[29]  Bernard P. A. Grandjean,et al.  Catalytic palladium‐based membrane reactors: A review , 1991 .

[30]  N. Sato,et al.  The water gas shift reaction assisted by a palladium membrane reactor , 1991 .

[31]  D. Newsome.  The Water-Gas Shift Reaction , 1980 .

[32]  G. Froment,et al.  Chemical Reactor Analysis and Design , 1979 .

[33]  D. Mears,et al.  The role of axial dispersion in trickle-flow laboratory reactors , 1971 .

[34]  F. A. Lewis,et al.  The Palladium-Hydrogen System , 1967, Platinum Metals Review.