| 1 |
Description of reaction rate for steam methane reforming throughout a channel in combination with diffusion in a porous catalytic wall: Extension to concentration variation along flow direction
Saito M, Sakurai S, Iwai H, Yoshida H
International Journal of Hydrogen Energy, 42(5), 3027, 2017 |
| 2 |
The limiting process in steam methane reforming with gas diffusion into a porous catalytic wall in a flow reactor
Saito M, Kojima J, Iwai H, Yoshida H
International Journal of Hydrogen Energy, 40(29), 8844, 2015 |
| 3 |
Preferential oxidation of CO over Au/CuOx-CeO2 catalyst in microstructured reactors studied through CFD simulations
Uriz I, Arzamendi G, Dieguez PM, Laguna OH, Centeno MA, Odriozola JA, Gandia LM
Catalysis Today, 216, 283, 2013 |
| 4 |
Catalytic coatings for structured supports and reactors: VOx/TiO2 catalyst coated on stainless steel in the oxidative dehydrogenation of propane
Lofberg A, Giornelli T, Paul S, Bordes-Richard E
Applied Catalysis A: General, 391(1-2), 43, 2011 |
| 5 |
An industrial view of process intensification
Becht S, Franke R, Geisselmann A, Hahn H
Chemical Engineering and Processing, 48(1), 329, 2009 |
| 6 |
Micro process technology as a means of process intensification
Becht S, Franke R, Geisselmann A, Hahn H
Chemical Engineering & Technology, 30(3), 295, 2007 |
| 7 |
Influence of the operating conditions on yield and selectivity for the partial oxidation of ethane in a catalytic membrane reactor
Georgieva K, Mednev I, Handtke D, Schmidt J
Catalysis Today, 104(2-4), 168, 2005 |
| 8 |
Millisecond catalytic wall reactors: dehydrogenation of ethane
Venkataraman K, Redenius JM, Schmidt LD
Chemical Engineering Science, 57(13), 2335, 2002 |
| 9 |
Deactivation kinetics in the hydrogenation of nitrobenzene to aniline on the basis of a coke formation kinetics -investigations in an isothermal catalytic wall reactor
Klemm E, Amon B, Redlingshofer H, Dieterich E, Emig G
Chemical Engineering Science, 56(4), 1347, 2001 |
