Glycerol can be dehydrated
with methanol to produce methyl glyceryl
ethers as biologicals and diesel fuel additives. Considering the high
efficiency of mass transfer and product separation in the gas–solid
catalytic process, a fixed-bed continuous-flow reactor was used to
carry out the catalyst evaluation test of the process at 564 K. Compared
with zirconium sulfate, lanthanum nitrate, and ammonium molybdate,
phosphotungstic acid exhibits a higher target product selectivity.
Through loading experiments, it was found that the optimal loading
fraction of phosphotungstic acid on alumina is 10 wt %. After the
alumina carrier is impregnated with nitric acid, the selectivity and
yield of monomethyl glycerol ether can be effectively improved, and
it has little effect on other products. A test of the addition amount
of cerium nitrate as a promoter was carried out. It was shown in the
test that when the addition amount of cerium nitrate is 10 wt %, the
catalyst life increases from 2 to 3.5 h and the selectivity of dimethyl
glycerol ether increases to 54.51%, which is twice the original. However,
the selectivities of monomethyl glycerol ether and trimethyl glycerol
ether decrease by one-half each. Through catalyst characterization,
it was shown that carbon deposition on the catalyst surface is one
of the reasons for catalyst deactivation.