Topics in Current Chemistry (2019) 377:1
1 3
glycerol (3) into propene. A highly concentrated aqueous feedstock solution of 3
(90% vol.) was mixed with a stream of molecular hydrogen and fed to a fixed‑bed
reactor operated at 300 °C. Up to 90% propene selectivity and quantitative glycerol
conversion were obtained over a Fe/Mo heterogeneous catalyst supported on carbon.
(a)
(b)
(c)
Fig. 10a–c Continuous flow strategies for the preparation of benzene (23), toluene (24), and xylene (25)
from a furfural (6), b HMF (7), and c glycerol (3)
120
Reprinted from the journal
1 3
glycerol (3) into propene. A highly concentrated aqueous feedstock solution of 3
(90% vol.) was mixed with a stream of molecular hydrogen and fed to a fixed‑bed
reactor operated at 300 °C. Up to 90% propene selectivity and quantitative glycerol
conversion were obtained over a Fe/Mo heterogeneous catalyst supported on carbon.
(a)
(b)
(c)
Fig. 10a–c Continuous flow strategies for the preparation of benzene (23), toluene (24), and xylene (25)
from a furfural (6), b HMF (7), and c glycerol (3)
120
Reprinted from the journal