Tuning the regioselectivity of heterogeneous hydroformylation by engineering carbon species microenvironment around Rh sites
Li Huang,
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Jia Wang,
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Qi Liu
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et al.
Journal of Catalysis,
Journal Year:
2025,
Volume and Issue:
unknown, P. 116095 - 116095
Published: March 1, 2025
Language: Английский
Effect of Metal Dispersion in Rh-Based Zeolite and SiO2 Catalysts on the Hydroformylation of Olefin Mixtures from Fischer–Tropsch Synthesis
Catalysts,
Journal Year:
2025,
Volume and Issue:
15(3), P. 212 - 212
Published: Feb. 24, 2025
This
study
investigates
the
hydroformylation
of
C5+
olefins
derived
from
Fischer–Tropsch
synthesis
(FTS)
using
Rh-based
catalysts
supported
on
zeolites
(MFI,
MEL)
and
SiO2.
A
series
were
synthesized
through
two
different
methods:
a
one-pot
hydrothermal
crystallization
process,
which
results
in
highly
dispersed
Rh
species
encapsulated
within
zeolite
framework
(Rh@MFI,
Rh@MEL),
an
impregnation
method
that
produces
larger
nanoparticles
exposed
support
surface
(Rh/MFI,
Rh/MEL,
Rh/SiO2).
Characterization
techniques
such
as
BET,
TEM,
FTIR
employed
to
evaluate
catalysts,
revealing
significant
differences
dispersion
accessibility
species.
Owing
its
more
accessible
mesoporous
structure,
Rh/SiO2
with
pore
size
5.6
nm
exhibited
highest
olefin
conversion
rate
(>90%)
40%
selectivity
C6+
aldehydes.
In
contrast,
zeolite-encapsulated
higher
for
aldehydes
(~50%)
due
better
confinement
linear
aldehyde
formation.
also
examined
influence
FTS
byproducts,
including
paraffins
short-chain
olefins,
reaction.
Results
showed
long-chain
had
negligible
effect
conversion,
while
presence
propene,
reduced
both
competitive
adsorption.
work
highlights
critical
role
catalyst
design,
diffusion,
feedstock
composition
optimizing
performance,
offering
insights
improving
efficiency
syngas-to-olefins
processes.
Language: Английский
Resolving Complex K–Pt–Sn Interactions in PtSn@K-MFI Catalysts for Alkane Dehydrogenation
Adrián Martínez Gómez-Aldaraví,
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Reisel Millán,
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Isabel Millet
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et al.
Journal of the American Chemical Society,
Journal Year:
2025,
Volume and Issue:
unknown
Published: April 3, 2025
K
and
Sn
contents
were
rationalized
during
the
synthesis
of
PtSn@K-MFI
to
maximize
metal
dispersion
stability
along
MFI
crystallites.
Experimental
results
theoretical
calculations
reveal
a
stoichiometry
∼1
per
unit
cell
MFI,
limiting
then
final
incorporation
within
siliceous
crystals
at
∼0.7
wt
%.
Above
this
stoichiometry,
is
not
incorporated
into
solids
unless
significant
amounts
are
simultaneously
present,
leading
formation
tin-silicate
precipitates.
The
optimized
catalysts
improve
catalytic
performance
well-established
references,
as
PtSn/SiO2,
for
propane
dehydration
(PDH)
reaction.
In
particular,
low
loadings
(below
0.5
%)
result
in
higher
time-on-stream
(TOS)
deactivation
profiles
but
excellent
regenarability
after
consecutive
PDH
reaction,
while
content
(close
1
minimizes
TOS
due
maximization
Pt-Sn
bonds
regenerations
sintering.
Increasing
crystallites
facilitates
Pt
sintering
and,
thus,
occurring
catalyst
upon
regeneration
cycles.
As
complex
interconnected
nucleation/crystallization
processes,
fine-tuning
rationalizations
one-pot
approaches
can
substantially
influence
atomic
subnanometric
interactions
consequently,
sintering-resistance
properties
when
exposed
highly
demanding
industrial
conditions.
Language: Английский