The
development of an economic and sustainable catalytic system
was crucial for lignin-based biorefinery. Herein, we reported a low-cost
Cu/CuMgAlO
x
catalyst with promising activity
toward lignin hydrodeoxygenation (HDO) through a H2-free
method. Supercritical methanol was used as the hydrogen donor, solvent,
and reactant simultaneously. Guaiacol was employed as a representative
lignin model compound to reveal the HDO mechanism of lignin derivatives.
HDOs of guaiacol performed at 250, 275, 300, and 350 °C with
durations ranging from 15 to 120 min indicated a high HDO efficiency
of the catalytic system. The obtained liquid products were categorized
to oxygen-containing unsaturated products (OUPs), oxygen-containing
saturated products (OSPs), and cycloalkanes. A kinetic model based
on a simplified reaction process containing the three following conversion
steps was established: guaiacol transformed to OUPs through the initial
HDO, then hydrogenated to OSPs (medium HDO), and eventually turned
to cycloalkanes by the deep HDO. The deep HDO was the rate-determining
step, and the apparent activation energies of the three steps were
all lower than those in the literature. Phenol, 1,2-cyclohexanediol,
anisole, and veratrole were the major intermediates, the HDOs of which
were programed for pathway verification. Remarkably, catechol (the
culprit of condensation) was not produced in this system. Overall,
a detailed reaction network of guaiacol HDO was established, and the
veil of Cu/CuMgAlO
x
-catalyzed lignin-derivatives
HDO in supercritical methanol was revealed. This work paved the way
for the application of Cu/CuMgAlO
x
catalyst
in lignin-derivatives upgrading.
The
fundamental understanding of the catalytic performance of copper-based
catalysts for lignin hydroconversion is delayed compared with the
empirical optimization of the catalyst preparation. Herein, we investigate
the interplay between the lignin-abundant oxygen-containing functional
groups and Cu active species via the catalytic β-O-4 lignin
linkage hydrogenolysis. Catalyst performance data and elemental spectra
characterizing the catalyst demonstrate the dominance of Cu0 in the catalysis. Remarkably, Cα–OH and
CαO in the aliphatic chain play critical
roles in this process, without which the linkage cannot be broken.
These groups markedly accelerate the linkage cleavage by decreasing
both the chemisorption energy between Cβ–O
and Cu0 and the bond dissociation energy of the linkage.
On the contrary, the methoxyl groups attached to the aromatic rings
hinder the bond cleavage as a result of the steric effect. Such hindrance
is significantly affected by the amount and position of the methoxyl
groups. The results of this work highlight the importance of the unique
structures of lignin in its reductive depolymerization catalyzed by
copper-based catalysts, which appear to offer an opportunity for tailoring
efficient copper-based catalysts for lignin hydrogenolysis.
Production
of jet fuel precursors from waste kraft lignin through
a depolymerization and hydrodeoxygenation (DHDO) method with a complex
copper acid catalyst is reported. The kraft lignin undergoes a high
degree of depolymerization, deoxygenation, hydrogenation, and C–C
coupling. Monomers and dimers with molecular weights in the ranges
of <200 Da and 354–452 Da are obtained with optimized yields
reaching 93.29 and 39.30 C% at 360 °C for 8 h, while trimers
and oligomers with higher molecular weights are also generated with
lower contents. The high carbon yields of monomers and dimers are
given by the incorporation of methanol solvent. The double bond equivalent
(DBE) and polydispersity index (PDI) decrease from 14.77 and 2.77
in kraft lignin to 9.05 and 1.35 in the products, while the high heating
value (HHV) increases from 24.53 to 36.47 MJ/kg after reaction. Furthermore,
over 45% of the optimized products have boiling points in the range
of that of commercial jet fuel (60–280 °C). All these
results demonstrate the appropriate properties of the products from
kraft lignin DHDO as potential jet fuel precursors.
In
the field of photocatalysis, the crystal phase engineering of
titanium dioxide is a research hotspot. Titanium dioxide heterojunctions
often exhibit better photocatalytic performance than single-phase
TiO2. Here, a two-step hydrothermal and calcination method
is used to build the phase interface between TiO2 (B) and
rutile for the first time, and a narrow band gap heterojunction TiO2 material is synthesized. The heterojunction TiO2 material is characterized by transmission electron microscopy (TEM),
ultraviolet (UV), X-ray photoelectron spectroscopy (XPS), and electron
paramagnetic resonance (EPR). The two phases are connected by a corner-sharing
at the phase interface. The different positions of the conduction
bands and valence bands between the two phases result in the effective
separation of photogenerated electrons and holes through the phase
interface. Under light, the photogenerated holes are transferred to
the rutile phase and quickly consumed by the sacrificial agent, and
the surplus photogenerated electrons participate in the H2 evolution reaction. When the ratio of TiO2 (B) to rutile
is about 2/1, the TiO2 (B)/rutile heterojunction exhibits
the highest photocurrent and the best H2 evolution performance
under the present experimental conditions.
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