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J. Chem. Sci.
(2019) 131:20
hydrocarbon oxidation reaction and hydrogen–oxygen starting materials. A solution of TiO(NO3)2 (9.89 mmol),
recombination reaction.27–30 When catalyst coated over
which was prepared from titanium tetraisopropoxide, PdCl2
(0.31 mmol), and glycine (10.99 mmol) were taken in a
cordierite monolith, it showed very good catalytic activ-
300 mL crystallizing dish. The solution was kept in a 350 ◦C
ity towards hydrogen-oxygen recombination reaction at
room temperature.31 On Pd2+ ion substitution in TiO2
preheated muffled furnace and combustion of starting
materials took place followed by dehydration. The dish was
lattice, a stable stoichiometric compound Ti1−x Pdx O2−x
kept inside the furnace for more than 20 min to burn all
(x=0.03) is formed with one oxide ion vacancy per Pd2+
the carbon contents. Then the dish was removed from the
ion for charge compensation. When Pd2+ is substituted,
furnace, allowed to cool and collected the catalyst pow-
an oxide ion vacancy is automatically created in the lat-
der. The catalyst was ground in a pestle and mortar and
tice. Pd2+ ion and oxide ion vacancy were next to each
characterized by PXRD. The combustion reaction is given
other as seen from the structure.31 Pd ion acted as an
by:
electrophile and oxide ion vacancy as a nucleophile.
TiO2 is cheaper reducible oxide support and non-toxic.
100% Pd ion dispersion is achieved so that all the Pd
metal used becomes the active site.
Here we have attempted Heck coupling reaction with
ionic palladium substituted TiO2 having composition
9(1 − x)TiO(NO3)2 + 10(1 − x)C2H5NO2
+ 9xPdCl2 → 9Ti1−x Pdx O2−
δ
+ 20(1 − x)CO2 + 14(1 − x)N2
+ (25 − 34x)H2O + 18xHCl: x = 0.01, 0.02, 0.03.
Ti0.97Pd0.03O1.97. To avoid handling nano-material in the
form of powder, and also to see if a catalyst cartridge
can be developed, we coated the catalyst on cordierite
monolith by solution combustion method.31,32 We have
avoided the use of powder catalyst. The reaction was
carried out with the solid monolith and removed it from
the reaction flask, reused it and calculated overall TOF
which was very high. The Heck coupling reaction was
done in a specially designed reaction flask, which pre-
vents breaking of cordierite monolith from fast rotating
magnetic beads.
X-ray diffraction patterns were recorded on a Philips
X’Pert Diffractometer at a scan rate of 0.1◦/min with a step
size in the 2 range between 10◦ and 90◦. The diffraction
θ
profiles were refined by Rietveld refinement method.
γ
2.3 Coating of −Al2 O3 over cordierite monolith
γ
Before coating the catalyst over monolith, −Al2O3 was
coated over monolith to increase the surface area and adhe-
sion to TiO2. This process was done by solution combustion
method by taking 15 mmol of Al(NO3)3 and 9 mmol of
glycine. A solution of starting materials was made and pre-
weighed monolith was dipped in the solution and kept inside
the furnace for combustion. After 15 min, monolith was
removed from the furnace and allowed to cool. The weight
of the monolith was taken. This procedure was repeated until
2. Experimental
γ
the weight of the coated −Al2O3 was 2 to 2.5% of cordierite
2.1 General
monolith weight.
X-ray diffraction patterns of catalysts were recorded on a
Philips X’Pert Diffractometer. Reactions were monitored
by using pre-coated silica TLC plates. Mass spectra were
recorded on EI and ESI (TOF) modes. NMR spectra were
recorded in at 400 MHz spectrometers in CDCl3, tetramethyl-
silane (TMS; δ = 0.00 ppm) served as an internal standard
for 1H NMR. The corresponding residual non-deuterated
solvent signal (CDCl3; δ = 77.00 ppm) was used as inter-
nal standard for 13C NMR. Column chromatography was
carried out on silica gel 230–400 mesh or 100–200 mesh
(SDFCL) and thin-layer chromatography was carried out
using SILICA GEL GF-254. Chemicals obtained from Sigma
Aldrich and SD Fine chemicals were used without further
purification.
2.4 Coating Ti0.97Pd0.03 O1.97 catalyst over cordierite
monolith
The solution was prepared in a beaker using starting mate-
rials such as TiO(NO3)2, palladium chloride and glycine. A
piece of the pre-weighed monolith was dipped in the solution
and kept inside the preheated muffled furnace for combustion.
After 20–30 min the hot monolith was taken out and allowed
to cool to room temperature. Then the cooled monolith was
kept for sonication process to remove loosely held particles.
The monolith was dried again to remove the moisture and
allowed to cool down. This procedure was repeated to get the
desired weight of catalyst to be coated. About 50 mg of cat-
alyst was coated on the monolith of 2.5 cm diameter, 2 cm
height with 400 cells/inch. Alumina coated monolith and cat-
alyst coated monolith are shown in Figure 1. We observed that
2.2 Synthesis of Ti0.97Pd0.03O1.97 powder catalyst
The catalyst Ti0.97Pd0.03O1.97 was synthesized by solution catalyst becomes black during the reaction due to adsorption
combustion method. Titanium tetraisopropoxide of olefins on palladium. After the reaction, catalyst is regen-
(Ti(OC3H7)4), palladium chloride and glycine were used as erated by heating at 200 ◦C in the air for about 2 h. Then it