Catalytic conversion of glycerol to value added liquid products
Catalytic conversion of glycerol was performed for production of value-added liquid chemicals. In this work, a systematic study has been conducted to evaluate the effects of operating conditions such as glycerol conversion to liquid chemical products in the presence of acid catalysts. Experiments we...
Gespeichert in:
Veröffentlicht in: | Applied catalysis. A, General General, 2010-01, Vol.372 (2), p.224-238 |
---|---|
Hauptverfasser: | , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
Zusammenfassung: | Catalytic conversion of glycerol was performed for production of value-added liquid chemicals. In this work, a systematic study has been conducted to evaluate the effects of operating conditions such as glycerol conversion to liquid chemical products in the presence of acid catalysts. Experiments were performed in a fixed-bed reactor using HZSM-5, HY, silica-alumina and γ-alumina catalysts. The temperature, carrier gas flow rate and weight hourly space velocity (WHSV) were maintained in the range of 350–500
°C, 20–50
mL/min and 5.40–21.60
h
−1, respectively. The main liquid chemicals detected in liquid product were acetaldehyde, acrolein, formaldehyde and hydroxyacetone. Under all experimental conditions complete glycerol conversion was obtained over silica-alumina and γ-alumina. A maximum liquid product yield of approximately 83
g/100
g feed was obtained with these two catalysts when the operating conditions were maintained at 380
°C, 26
mL/min and 8.68
h
−1. Maximum glycerol conversions of 100
wt% and 78.8
wt% were obtained in the presence of HY and HZSM-5 at temperature, carrier gas flow rate and WHSV of 470
°C, 26
mL/min and 8.68
h
−1. HY and HZSM-5 produced maximum liquid product of 80.9 and 59.0
g/100
g feed at temperature of 425 and 470
°C, respectively. Silica-alumina produced the maximum acetaldehyde (∼24.5
g/100
g feed) whereas γ-alumina produced the maximum acrolein (∼25
g/100
g feed). Also, silica-alumina produced highest formaldehyde yield of 9
g/100
g feed whereas HY produced highest acetol yield of 14.7
g/100
g feed. The effect of pore size of these catalysts was studied on optimum glycerol conversion and liquid product yield.
The optimum operating conditions to obtain the maximum glycerol conversion over HZSM-5 (78.8
wt%) and HY (100
wt%) were 470
°C, 26
mL/min and WHSV of 8.68
h
−1. Optimum conversion increased from 80 to 100
wt% and optimum liquid product increased from 59 to 83.3
g/100
g feed when the pore size of catalyst was increased from 0.54 in case of HZSM-5 to 0.74
nm in case of HY; beyond which the effect pore of size was minimal. |
---|---|
ISSN: | 0926-860X 1873-3875 |
DOI: | 10.1016/j.apcata.2009.10.036 |