Zobrazeno 1 - 8
of 8
pro vyhledávání: '"Elina Harlin"'
Publikováno v:
In Studies in Surface Science and Catalysis 1999 126:163-170
Publikováno v:
Industrial & Engineering Chemistry Research. 47:5402-5412
An experimental investigation of structure−performance effects in zeolite catalyzed skeletal isomerization has been carried out. Two structurally different, medium-pore-size zeolites (H-TON and H-FER) with similar acidities were compared in butene
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::5b8b85aba10077c3a7e7c9fb0f172339
https://doi.org/10.1021/ie800061q
https://doi.org/10.1021/ie800061q
Autor:
J.I. Villegas, Narendra Kumar, Matias Kangas, Fredrik Sandelin, D. Yu. Murzin, Tapio Salmi, Elina Harlin
Publikováno v:
Catalysis Today. 100:363-366
An investigation of the effect of reaction conditions on product distribution in the skeletal isomerisation reaction of linear butenes has been carried out. The main reaction routes over ferrierite have been identified. Beside the main product isobut
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::297f9a387f511954a47508ca1971a29f
https://doi.org/10.1016/j.cattod.2004.10.024
https://doi.org/10.1016/j.cattod.2004.10.024
Publikováno v:
Catalysis Today. 78:171-180
Alumina-supported vanadium oxide catalysts with vanadium contents of 2, 5 and 11 wt.% were prepared by incipient wetness impregnation and characterised by XRD, Raman spectroscopy and H 2 -TPR. The catalysts with the low vanadium contents contained va
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::1cad701f5419f5aa81af16744e82881b
https://doi.org/10.1016/s0920-5861(02)00326-7
https://doi.org/10.1016/s0920-5861(02)00326-7
Publikováno v:
Industrial & Engineering Chemistry Research. 41:5619-5626
The kinetics of isobutane dehydrogenation was studied on a chromia/alumina catalyst developed for fluidized-bed operation. The dehydrogenation activity measurements were carried out in a laboratory-scale plug-flow reactor at 520−580 °C under atmos
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::3398218815f74eff6c059124dd9d1684
https://doi.org/10.1021/ie020371j
https://doi.org/10.1021/ie020371j
Autor:
Baudouin Heinrich, Frederic Meunier, Marc J. Ledoux, A. Outi I. Krause, M. Elina Harlin, Cuong Pham-Huu
Publikováno v:
Applied Catalysis A: General. 181:157-170
MoO 3 activated under butane and hydrogen mixture at 623 K was tested for the reactions of simultaneous isomerization and dehydrogenation of n -butane at 823 K. The active phase, a mixture of oxycarbide and oxide of molybdenum, was active but unstabl
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::31a5ce767bbab8ddfa212c6f0ebec654
https://doi.org/10.1016/s0926-860x(98)00417-7
https://doi.org/10.1016/s0926-860x(98)00417-7
s The deactivation of molybdenum oxycarbide supported on SiC catalyst during the n-butane dehydrogenation at 550 °C was characterized by a combination of XRD and TPO techniques. Deactivation was due to carbonaceous residue formation on the catalyst
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::5564593e2aaacc3abf8e21f4b0a69b9e
https://doi.org/10.1016/s0167-2991(99)80463-7
https://doi.org/10.1016/s0167-2991(99)80463-7
Publikováno v:
Industrial & Engineering Chemistry Research; Jul2008, Vol. 47 Issue 15, p5402-5412, 11p