INVESTIGADORES
QUERINI Carlos Alberto
artículos
Título:
Coke and Product Profiles Formed Along the Catalyst Bed during n-Heptane Reforming. II. Influence of S on Pt/Al2O3 and Pt?Re/Al2O3
Autor/es:
QUERINI, C.A.; FUNG, S.C.
Revista:
JOURNAL OF CATALYSIS
Referencias:
Año: 1996 vol. 161 p. 263 - 273
ISSN:
0021-9517
Resumen:
Studies of coke and product profiles along catalyst beds of
Pt/Al2O3 and Pt?Re/Al2O3 during n-heptane reforming have provided
insight into catalyst deactivation and reaction mechanisms.
The addition of rhenium to a Pt catalyst changes coke and product
profiles similar to those observed with an increase in pressure.
Sulfur modifies these profiles in the opposite direction of rhenium.
It affects the catalyst in a similar manner to a decrease in reactor
pressure: a reduction in hydrogenolysis activity, an increase in dehydrogenation
and coke-make, and a shift of the maximum in the
coke profile toward the bottom of the reactor. Due to a slow stripping
of sulfur during reforming reactions, an increasing sulfur concentration
along the bed is observed at the end of several-days run.
As a consequence, the coke profile does not match exactly with the
C5-ring naphthene concentration profile, as was previously found
on both unsulfided Pt and Pt?Re catalysts. The observed increase
in coke-make and dehydrogenation activity, when sulfur is added
to the Pt?Re catalyst, is probably due to a decrease in the hydrogen
surface fugacity produced through electronic modifications of Pt by
adsorbed sulfur atoms.
insight into catalyst deactivation and reaction mechanisms.
The addition of rhenium to a Pt catalyst changes coke and product
profiles similar to those observed with an increase in pressure.
Sulfur modifies these profiles in the opposite direction of rhenium.
It affects the catalyst in a similar manner to a decrease in reactor
pressure: a reduction in hydrogenolysis activity, an increase in dehydrogenation
and coke-make, and a shift of the maximum in the
coke profile toward the bottom of the reactor. Due to a slow stripping
of sulfur during reforming reactions, an increasing sulfur concentration
along the bed is observed at the end of several-days run.
As a consequence, the coke profile does not match exactly with the
C5-ring naphthene concentration profile, as was previously found
on both unsulfided Pt and Pt?Re catalysts. The observed increase
in coke-make and dehydrogenation activity, when sulfur is added
to the Pt?Re catalyst, is probably due to a decrease in the hydrogen
surface fugacity produced through electronic modifications of Pt by
adsorbed sulfur atoms.
2O3 and Pt?Re/Al2O3 during n-heptane reforming have provided
insight into catalyst deactivation and reaction mechanisms.
The addition of rhenium to a Pt catalyst changes coke and product
profiles similar to those observed with an increase in pressure.
Sulfur modifies these profiles in the opposite direction of rhenium.
It affects the catalyst in a similar manner to a decrease in reactor
pressure: a reduction in hydrogenolysis activity, an increase in dehydrogenation
and coke-make, and a shift of the maximum in the
coke profile toward the bottom of the reactor. Due to a slow stripping
of sulfur during reforming reactions, an increasing sulfur concentration
along the bed is observed at the end of several-days run.
As a consequence, the coke profile does not match exactly with the
C5-ring naphthene concentration profile, as was previously found
on both unsulfided Pt and Pt?Re catalysts. The observed increase
in coke-make and dehydrogenation activity, when sulfur is added
to the Pt?Re catalyst, is probably due to a decrease in the hydrogen
surface fugacity produced through electronic modifications of Pt by
adsorbed sulfur atoms.