Zobrazeno 1 - 10
of 13
pro vyhledávání: '"GF Froment"'
Publikováno v:
Bulletin des Sociétés Chimiques Belges. 93:823-830
A Hougen-Watson model with interconverting sites (H.W.-I.S.) has been formulated to account for the influence of H2 and H2S on the number of active sites. The model assumes that the ratio of the concentration of active sites for hydrogenolysis and hy
Publikováno v:
Journal of Catalysis. 174:177-184
The isomerization hydrocracking of heptadecane on Pt/H–ZSM-22 was studied in a continuous flow type, fixed-bed, vapor-phase reactor. High yields of skeletal isomerization of heptadecane (90%) were obtained. The low tendency to cracking of isoheptad
Publikováno v:
Catalysis Letters. 37:207-212
1-cyclohexyloctane is isomerized on the large pore, bifunctional zeolite catalyst Pt/H-Y. The detailed isomerization mechanism of this naphtene molecule is revealed through a thorough analysis of the numerous isomerization products. It is found that
Publikováno v:
Applied Catalysis. 76:131-142
Intimate mixtures of bifunctional catalysts based on ZSM-22 and Y zeolites do not show merely the intermediate catalytic properties between those found for the individual zeolites. Such mixtures produce enhanced yields of multibranched isodecanes fro
Publikováno v:
Applied Catalysis. 76:95-116
Detailed product distributions from the bifunctional conversion of decane over Pt/ZSM-22, Pt/ZSM-5 and Pt/USY catalysts are compared. In contrast to other zeolites, the product selectivities from decane on Pt/ZSM-22 vary largely with the reaction con
The Pt/H-ZSM-22 catalyst exhibits peculiar dimethylbranching selectivities in the skeletal isomerization of C8-C11 n-alkanes. Out of the large number of theoretically possible dibranched skeletal isomerization products, a few dimethylbranched isomers
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2227b2f3e5db7f78e21fc77c02a93461
https://doi.org/10.1016/s0167-2991(97)80768-9
https://doi.org/10.1016/s0167-2991(97)80768-9
Octane, decane and undecane are converted over bifunctional Pt/H-Y and Pt/H-ZSM-22 zeolites and on intimate 50–50 and 80–20 wt/wt mixtures of these zeolites. Compared to the individual zeolites, the zeolite mixtures exhibit an enhanced catalytic
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::c5fa23484d365e7f4b3e85bbecb791cb
https://doi.org/10.1016/s0167-2991(08)64416-x
https://doi.org/10.1016/s0167-2991(08)64416-x
Publikováno v:
Industrial & Engineering Chemistry Product Research and Development. 20:654-660
Autor:
R.P. De Pauw, GF Froment
Publikováno v:
Chemical Engineering Science. 30:789-801
This work concerns the methodology of characterizing the deactivation of a catalyst by coke deposition. The isomerization of n.pentane on a platinum reforming catalyst was studied in a tubular reactor permitting easy sampling of the gas phase at seve
Publikováno v:
Industrial & Engineering Chemistry Process Design and Development. 15:495-504