Zobrazeno 1 - 4
of 4
pro vyhledávání: '"Carl-Robert Florén"'
Autor:
Per-Anders Carlsson, Gudmund Smedler, David Thompsett, Agnes Raj, Magnus Skoglundh, Carl-Robert Florén, Peter Velin
Publikováno v:
Catalysis Science & Technology. 10:5460-5469
The catalytic activity for dry and wet methane oxidation over a series of palladium–alumina catalysts with palladium loadings from 0.23 to 3.6 wt% Pd and systematically varied PdO dispersions from 8.1 to 39% was evaluated by flow reactor measuremen
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::5d373ac0ca6ea951d1487c1b8ca8e693
https://doi.org/10.1039/d0cy00734j
https://doi.org/10.1039/d0cy00734j
Publikováno v:
Catalysis Science & Technology. 10:5480-5486
The kinetics of total methane oxidation over a 0.15 wt% Pd/Al2O3 monolith catalyst has been measured during temperature programmed methane oxidation experiments at total pressures from 1 to 10 atm and compared with multiscale simulations. The methane
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::6fff1e288d84ddba874526ba86ea3100
https://doi.org/10.1039/d0cy00813c
https://doi.org/10.1039/d0cy00813c
Publikováno v:
Catalysis Science & Technology. 9:3055-3065
A two-dimensional multiscale model is developed for complete methane oxidation in a continuous flow reactor. The model considers mass and heat transfer for a porous alumina supported palladium catalyst coated on a ceramic monolith substrate and the s
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::014794bef14a1a1d911a91b429cca10e
https://doi.org/10.1039/c8cy02461h
https://doi.org/10.1039/c8cy02461h
Autor:
Magnus Skoglundh, Heikki Korpi, Maxime Van den Bossche, Henrik Grönbeck, Carl-Robert Florén, Per-Anders Carlsson, Derek Creaser
Publikováno v:
Catalysis Science & Technology. 8:508-520
A comprehensive model is developed for complete methane oxidation over supported palladium. The model is based on first-principles microkinetics and accounts for mass and heat transport in a porous catalytic layer. The turnover frequency (TOF) is sim
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::0ab675babde46bc48283b72c71f9299b
https://doi.org/10.1039/c7cy02135f
https://doi.org/10.1039/c7cy02135f