TY - JOUR
T1 - A two-step approach for producing oxygen-free aromatics from lignin using formic acid as a hydrogen source
AU - Hidajat, Marcel Jonathan
AU - Riaz, Asim
AU - Kim, Jaehoon
N1 - Publisher Copyright:
© 2018 Elsevier B.V.
PY - 2018/9/15
Y1 - 2018/9/15
N2 - A high-calorific-value oil with a high amount of oxygen-free aromatics was produced from highly recalcitrant concentrated-sulfuric-acid-hydrolysis lignin (CSAHL) using a two-step approach. In the first step, lignin-derived bio-oil (LBO) was produced by the liquefaction of CSAHL in a mixture of supercritical ethanol and formic acid. In the second step, hydrodeoxygenation (HDO) of the LBO over sulfided CoMo/γ-Al2O3 (CoMoSx/γ-Al2O3), Pd/Al2O3, and Ru/γ-Al2O3 catalysts was performed to produce upgraded LBO. Although the yield of the LBO was high (70 wt%), its calorific value and the yield of monoaromatics (mainly oxygenated guaiacol- and syringol-type molecules) were low (27.2 MJ kg−1 and 4 wt% (based on CSAHL), respectively). The LBO was separated from the ethanol and used as a feed for HDO in formic acid, which acts as an in-situ hydrogen donating agent. HDO of the LBO over CoMoSx/γ-Al2O3 at 350 °C for 4 h produced oxygen-free aromatics, such as alkylated benzenes, indanes, and tetralins, with the high yield of 6.8 wt% (based on CSAHL). The degree of deoxygenation was high (>90%) and the upgraded LBO exhibited a high calorific value (>40 MJ kg−1). The effects of different HDO parameters, including catalyst loading, amount of formic acid, reaction time, catalyst type, and solvent type were assessed to gain insight into the LBO deoxygenation mechanisms.
AB - A high-calorific-value oil with a high amount of oxygen-free aromatics was produced from highly recalcitrant concentrated-sulfuric-acid-hydrolysis lignin (CSAHL) using a two-step approach. In the first step, lignin-derived bio-oil (LBO) was produced by the liquefaction of CSAHL in a mixture of supercritical ethanol and formic acid. In the second step, hydrodeoxygenation (HDO) of the LBO over sulfided CoMo/γ-Al2O3 (CoMoSx/γ-Al2O3), Pd/Al2O3, and Ru/γ-Al2O3 catalysts was performed to produce upgraded LBO. Although the yield of the LBO was high (70 wt%), its calorific value and the yield of monoaromatics (mainly oxygenated guaiacol- and syringol-type molecules) were low (27.2 MJ kg−1 and 4 wt% (based on CSAHL), respectively). The LBO was separated from the ethanol and used as a feed for HDO in formic acid, which acts as an in-situ hydrogen donating agent. HDO of the LBO over CoMoSx/γ-Al2O3 at 350 °C for 4 h produced oxygen-free aromatics, such as alkylated benzenes, indanes, and tetralins, with the high yield of 6.8 wt% (based on CSAHL). The degree of deoxygenation was high (>90%) and the upgraded LBO exhibited a high calorific value (>40 MJ kg−1). The effects of different HDO parameters, including catalyst loading, amount of formic acid, reaction time, catalyst type, and solvent type were assessed to gain insight into the LBO deoxygenation mechanisms.
KW - Degree of deoxygenation
KW - Formic acid
KW - Hydrodeoxygenation
KW - Lignin
KW - Oxygen-free aromatics
UR - https://www.scopus.com/pages/publications/85047062654
U2 - 10.1016/j.cej.2018.05.036
DO - 10.1016/j.cej.2018.05.036
M3 - Article
AN - SCOPUS:85047062654
SN - 1385-8947
VL - 348
SP - 799
EP - 810
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
ER -