Enhancing catalyst effectiveness by increasing catalyst film thickness in coated-wall microreactors: Exploiting heat effects in catalytic methane steam micro-reformers
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[1] Steve Perry,et al. Microchannel Process Technology for Compact Methane Steam Reforming , 2004 .
[2] Jacob A. Moulijn,et al. Monoliths in Heterogeneous Catalysis , 1994 .
[3] Yong Wang,et al. From seconds to milliseconds to microseconds through tailored microchannel reactor design of a steam methane reformer , 2007 .
[4] Jacques Mettes,et al. Radial Microchannel Reactors (RMRs) for Efficient and Compact Steam Reforming of Methane: Experimental Demonstration and Design Simulations , 2013 .
[5] James J. Carberry,et al. The catalytic effectiveness factor under nonisothermal conditions , 1961 .
[6] D. Vlachos,et al. Enhancing stability in parallel plate microreactor stacks for syngas production , 2011 .
[7] Dionisios G. Vlachos,et al. Intensification of steam reforming of natural gas: Choosing combustible fuel and reforming catalyst , 2010 .
[8] Michael Baldea,et al. Pseudodistributed Feed Configurations for Catalytic Plate Microchannel Reactors , 2014 .
[9] Michael Baldea,et al. Optimizing the catalyst distribution for countercurrent methane steam reforming in plate reactors , 2011 .
[10] E. W. Thiele. Relation between Catalytic Activity and Size of Particle , 1939 .
[11] G. Froment,et al. Methane steam reforming, methanation and water‐gas shift: I. Intrinsic kinetics , 1989 .
[12] Yongchan Kim,et al. Minimization of hot spot in a microchannel reactor for steam reforming of methane with the stripe combustion catalyst layer , 2013 .
[13] Ho Ting Luk,et al. Techno-economic Analysis of Distributed Hydrogen Production from Natural Gas , 2012 .
[14] J. Carberry. The micro‐macro effectiveness factor for the reversible catalytic reaction , 1962 .
[15] Yi Cheng,et al. Catalytic performance of Ni catalysts for steam reforming of methane at high space velocity , 2011 .
[16] Rutherford Aris,et al. On shape factors for irregular particles—I: The steady state problem. Diffusion and reaction , 1995 .
[17] Michael Baldea,et al. A thermal‐flywheel approach to distributed temperature control in microchannel reactors , 2013 .
[18] Iftekhar A. Karimi,et al. Evaluation of utilization alternatives for stranded natural gas , 2012 .
[19] Mustafa Karakaya,et al. Parametric study of methane steam reforming to syngas in a catalytic microchannel reactor , 2012 .
[20] B. Wilhite,et al. Influence of internal heat removal upon effectiveness, stability of an exothermic catalytic film: Implications for process intensification , 2012 .
[21] Yi Cheng,et al. Steam reforming of methane over Ni catalyst in micro-channel reactor , 2011 .
[22] Michael Baldea,et al. Robust autothermal microchannel reactors , 2015, Comput. Chem. Eng..
[23] M. Balat. Potential importance of hydrogen as a future solution to environmental and transportation problems , 2008 .
[24] Milorad P. Dudukovic,et al. Recuperative coupling of exothermic and endothermic reactions , 2006 .
[25] Ravi Arora,et al. Microchannel Technology Scale-up to Commercial Capacity , 2005 .
[26] M J Economides,et al. THE ECONOMICS OF GAS TO LIQUIDS COMPARED TO LIQUEFIED NATURAL GAS , 2005 .
[27] Dionisios G. Vlachos,et al. Scale-out of Microreactor Stacks for Portable and Distributed Processing: Coupling of Exothermic and Endothermic Processes for Syngas Production , 2010 .
[28] J. Andrews,et al. Re-envisioning the role of hydrogen in a sustainable energy economy , 2012 .
[29] J. Carberry,et al. The non-isothermal catalytic effectiveness factor for monolith supported catalysts , 1973 .
[30] Jacques Mettes,et al. Design of an annular microchannel reactor (AMR) for hydrogen and/or syngas production via methane steam reforming , 2014 .
[31] C. Satterfield,et al. Effectiveness Factor for Porous Catalysts. Langmuir-Hinshelwood Kinetic Expressions , 1965 .
[32] George Leckie,et al. Stranded gas: a vital resource , 2002 .
[33] Dionisios G. Vlachos,et al. High vs. low temperature reforming for hydrogen production via microtechnology , 2009 .