TY - JOUR
T1 - Effective conversion of the carbohydrate-rich macroalgae (Saccharina japonica) into bio-oil using low-temperature supercritical methanol
AU - Zeb, Hassan
AU - Riaz, Asim
AU - Kim, Jaehoon
N1 - Publisher Copyright:
© 2017 Elsevier Ltd
PY - 2017/11/1
Y1 - 2017/11/1
N2 - The use of supercritical methanol (scMeOH) for the liquefaction of the carbohydrate-rich macroalgae Saccharina japonica was investigated at low temperature (250–300 °C). At 300 °C, almost complete conversion (98.1 wt%) and a high bio-oil yield (66.0 wt%) were achieved. These values are higher than those achieved with supercritical ethanol (scEtOH, 87.8 wt% conversion, 60.5 wt% bio-oil yield) and subcritical water (subH2O, 91.9 wt% conversion, 40.3 wt% bio-oil yield) under identical reaction conditions. The superior liquefaction in scMeOH is attributed to the beneficial physical properties of scMeOH, including its higher polarity, superior reactivity, and higher acidity. The superior reactivity of scMeOH was evident from the larger amount of esters (54.6 area%) produced in scMeOH as compared to that in scEtOH (47.2 area%), and the larger amount of methyl/methoxy-containing compounds (78.6 area%) produced in scMeOH than that of ethyl/ethoxy-containing compounds (58.2 area%) produced in scEtOH. The higher bio-oil yield combined with its higher calorific value (29.2 MJ kg−1) resulted in a higher energy recovery of 135% for scMeOH as compared to those of scEtOH (118%) and subH2O (96%). When considering the amount of alcohol consumed during the liquefactions and the production of light bio-oil fractions that evaporate during bio-oil recovery, the higher methanol consumption (5.3 wt%) than that of ethanol (2.3 wt%) leads to similar bio-oil yields (∼51 wt%).
AB - The use of supercritical methanol (scMeOH) for the liquefaction of the carbohydrate-rich macroalgae Saccharina japonica was investigated at low temperature (250–300 °C). At 300 °C, almost complete conversion (98.1 wt%) and a high bio-oil yield (66.0 wt%) were achieved. These values are higher than those achieved with supercritical ethanol (scEtOH, 87.8 wt% conversion, 60.5 wt% bio-oil yield) and subcritical water (subH2O, 91.9 wt% conversion, 40.3 wt% bio-oil yield) under identical reaction conditions. The superior liquefaction in scMeOH is attributed to the beneficial physical properties of scMeOH, including its higher polarity, superior reactivity, and higher acidity. The superior reactivity of scMeOH was evident from the larger amount of esters (54.6 area%) produced in scMeOH as compared to that in scEtOH (47.2 area%), and the larger amount of methyl/methoxy-containing compounds (78.6 area%) produced in scMeOH than that of ethyl/ethoxy-containing compounds (58.2 area%) produced in scEtOH. The higher bio-oil yield combined with its higher calorific value (29.2 MJ kg−1) resulted in a higher energy recovery of 135% for scMeOH as compared to those of scEtOH (118%) and subH2O (96%). When considering the amount of alcohol consumed during the liquefactions and the production of light bio-oil fractions that evaporate during bio-oil recovery, the higher methanol consumption (5.3 wt%) than that of ethanol (2.3 wt%) leads to similar bio-oil yields (∼51 wt%).
KW - Bio-oil
KW - Carbohydrate-rich macroalgae
KW - Liquefaction
KW - Solvent consumption
KW - Supercritical methanol
UR - https://www.scopus.com/pages/publications/85033726913
U2 - 10.1016/j.enconman.2017.08.092
DO - 10.1016/j.enconman.2017.08.092
M3 - Article
AN - SCOPUS:85033726913
SN - 0196-8904
VL - 151
SP - 357
EP - 367
JO - Energy Conversion and Management
JF - Energy Conversion and Management
ER -