Influence of Steam Reforming Catalyst Geometry on the Performance of Tubular Reformer – Simulation Calculations

Journal title

Chemical and Process Engineering




No 2 June

Publication authors

Divisions of PAS

Nauki Techniczne


Polish Academy of Sciences Committee of Chemical and Process Engineering


2015[2015.01.01 AD - 2015.12.31 AD]


ISSN 0208-6425


Shumake (2007), Optimize your hydrogen plant operations Hydrocarb, Process, 9. ; Peña (1996), New catalytic routes for syngas and hydrogen production, Appl Catal, 144, ; Michel (2007), Steam reforming - the next generation of catalysts Materials of the Nitrogen Syngas International Conference Exhibition, Bahrain, 25. ; Ferreira (2005), New trends in reforming technologies : from hydrogen industrial plants to multifuel microreformers, Catal Rev, 47, ; Franczyk (2009), Deactivation of steam reforming catalysts under industrial conditions, Przem Chem, 88. ; Rostrup (1984), Catalytic steam reforming In Catalysis - science and technology Springer - Verlag, Vol, ; Gołębiowski (2009), Industrial catalyst technologies developed by INS Puławy Fifty years of experience, Przem Chem, 88. ; Yu (2006), Simulation of natural gas steam reforming furnace, Fuel Process Technol, 87, ; Borowiecki (2005), Modern synthesis gas and hydrogen plants, Przem Chem, 84. ; Holladay (2009), An overview of hydrogen production technologies, Catal Today, 139, ; Ziółkowski (1980), A mathematical model of a unit reactor pipe for catalytic conversion of methane by water steam Formulation of the model Inż, Chem Proc, 1. ; Christiansen (1970), Numerical solution of ordinary simultaneous differential equations of the st order using a method for automatic step change, Numer Math, 14. ; Rostrup (2011), Concepts in Syngas Manufacture In Catalytic Science Series Imperial College Press, Vol, 10, ; Ziółkowski (1982), b Experimental verification in pilot scale of a mathematical model of a unit pipe reactor for catalytic conversion of methane by water vapour Inż, Chem Proc, 3. ; Gołębiowski (1977), Differentialreaktor für kinetische Untersuchungen katalytischer Reaktionen, Chem Techn, 29. ; Ziółkowski (1982), a Over - all heat transfer coefficient at the gas stream heating by the wall of a tubular apparatus packed with a static granular bed Inż, Chem Proc, 3. ; Leva (1947), Heat transfer to gases through packed tubes, Ind Eng Chem, 39, ; Wu (2007), Mechanical strength of solid catalysts : recent developments and future prospects, AIChE Journal, 53,