Results 171 to 180 of about 5,287 (218)
Some of the next articles are maybe not open access.

Naphtha reforming on mono and bimetallic catalysts

Applied Catalysis, 1987
Abstract Catalytic activity, selectivity and stability in the reforming of several naphtha cuts on Pt/Al 2 O 3 , Pt-Re-S/Al 2 O 3 and Pt-Ge/Al 2 O 3 were studied by carrying out activity-deactivation tests which consist of three periods. During the first and third periods, industrial conditions were reproduced, and during the second one, pressure ...
C.A. Querini, N.S. Figoli, J.M. Parera
openaire   +1 more source

Kinetic Modeling of Naphtha Catalytic Reforming Reactions

Energy & Fuels, 2000
In this work a kinetic model for the naphtha catalytic reforming process is presented. The model utilizes lumped mathematical representation of the reactions that take place, which are written in terms of isomers of the same nature. These groups range from 1 to 11 atoms of carbon for paraffins, and from 6 to 11 carbon atoms for naphthenes and aromatics.
Jorge Ancheyta-Juárez   +1 more
openaire   +1 more source

Catalytic Reforming of Hydrogenated Shale-Oil Naphtha

Product R&D, 1972
C a t a l y t i c reforming i s a ' p rocess f o r conver t ing low-octane naphthas or gaso l ines i n t o high-octane products. Most c a t a l y t i c reforming processes r e q u i r e very c l ean feeds tocks t o avoid d e a c t i v a t i n g t h e c a t a l y s t s .
L. K. Barker, P. L. Cottingham
openaire   +1 more source

A dynamic model for naphtha catalytic reformers

Proceedings of the 2004 IEEE International Conference on Control Applications, 2004., 2005
A kinetics-based dynamic model for commercial naphtha fixed-bed catalytic reformers is developed in this paper. The dynamic model is composed of the reforming reaction model, the heater model and the separator model, which is capable to capture the major dynamics that occur in this process system.
null Yongyou Hu   +3 more
openaire   +1 more source

XPS studies of Pt—Sn naphtha reforming catalysts

Applied Catalysis, 1990
Abstract Pt—Sn has been supported on a nonporous (110 m2/g) alumina, a higher surface area (250 m2/g) porous alumina and a silica (700 m2/g). Both Sn (O) and Pt (O) have been observed in the reduced samples. Sn(O), and presumably alloy formation, occurs to a greater extent when platinum and tin are added as a complex dissolved in acetone as compared ...
Yong-Xi Li   +2 more
openaire   +1 more source

Kinetic of Naphtha Catalytic Reforming. Influence of Space Velocity on Naphtha Composition Changes

Oil, gas (Hamburg), 1996
In order to develop a kinetic model of reforming reactions the influence of space velocities on the change in composition of whole naphtha was studied. The activity of two commercial Pt-Re/Al2O3 catalysts (R-16 G and R-62) was tested in a pilot plant at space velocities 2.5-5.4 h-1, hydrogen: hydrocarbon mol ratio 5:1 and temperature 505 C.
Vrbanović, Željko   +2 more
openaire   +1 more source

Trimetallic naphtha reforming catalysts

Applied Catalysis A: General, 2004
L.S. Carvalho   +5 more
openaire   +1 more source

Catalytic Naphtha Reforming

2019
Mark J. Kaiser   +3 more
openaire   +1 more source

Home - About - Disclaimer - Privacy