Hydrocracking of a long chain paraffin, hexadecane, was carried out on a Mo/Hb-alumina bi-functional catalyst with a weak dehydrogenating function. It was found through an isomerization selectivity analysis that the behavior of the system is away from ideal hydrocracking conditions. To implement for this system the single event concept, until now applied only to systems for which the ideal hydrocracking assumption was valid, a hybrid model that includes the more general case in which reactions on the acid sites are not rate determining was developed. This model was called the single-event-lumped-parameter hybrid (SELPH) model, for it considers fundamental rate constants for the reactions that take place on the acid sites using the single ev...
A kinetic dual-function model was employed to simulate the performance of binary mixtures of Pt/zeol...
Hydroisomerization and hydrocracking using bifunctional catalysts with hydrogenation-dehydrogenation...
The construction of kinetic models is an important step in the development of refining processes. In...
With increasing environmental concerns, gasoline and lubricant oils with high octane number are bein...
The derivation of kinetic models for the development and simulation of hydrocarbon processes require...
A mechanistic kinetic model for the hydrocracking of paraffins based on the single-event kinetics ap...
Hydrocracking of normal octane was carried out at temperatures from 493 to 548 K and pressures of 15...
A methodology was developed to interpret the results of n-.paraffins hydroisomerization over bifunct...
Two separate mechanistic kinetic models have been developed for the hydrocracking of complex feedsto...
Bifunctional catalysts consisting of palladium or platinum and supported on amorphous silica-alumina...
L'hydrocraquage est un procédé catalytique majeur dans la valorisation des coupes pétrolières lourde...
The paper deals with hydrocracking on metal-loaded zeolites. A fundamental approach is presented in ...
The hydrocracking reactivity of two model compounds, namely n-C(16)H(34) (n-C16) and n-C(28)H(58) (n...
The paper deals with hydrocracking on metal-loaded zeolites. A fundamental approach is presented in ...
Hydrocracking feedstocks contain a wide variation in the concentration of various compunds types, i....
A kinetic dual-function model was employed to simulate the performance of binary mixtures of Pt/zeol...
Hydroisomerization and hydrocracking using bifunctional catalysts with hydrogenation-dehydrogenation...
The construction of kinetic models is an important step in the development of refining processes. In...
With increasing environmental concerns, gasoline and lubricant oils with high octane number are bein...
The derivation of kinetic models for the development and simulation of hydrocarbon processes require...
A mechanistic kinetic model for the hydrocracking of paraffins based on the single-event kinetics ap...
Hydrocracking of normal octane was carried out at temperatures from 493 to 548 K and pressures of 15...
A methodology was developed to interpret the results of n-.paraffins hydroisomerization over bifunct...
Two separate mechanistic kinetic models have been developed for the hydrocracking of complex feedsto...
Bifunctional catalysts consisting of palladium or platinum and supported on amorphous silica-alumina...
L'hydrocraquage est un procédé catalytique majeur dans la valorisation des coupes pétrolières lourde...
The paper deals with hydrocracking on metal-loaded zeolites. A fundamental approach is presented in ...
The hydrocracking reactivity of two model compounds, namely n-C(16)H(34) (n-C16) and n-C(28)H(58) (n...
The paper deals with hydrocracking on metal-loaded zeolites. A fundamental approach is presented in ...
Hydrocracking feedstocks contain a wide variation in the concentration of various compunds types, i....
A kinetic dual-function model was employed to simulate the performance of binary mixtures of Pt/zeol...
Hydroisomerization and hydrocracking using bifunctional catalysts with hydrogenation-dehydrogenation...
The construction of kinetic models is an important step in the development of refining processes. In...