TY - JOUR
T1 - A centrifugation-first approach for recovering high-yield bio-oil with high calorific values in biomass liquefaction
T2 - A case study of sewage sludge
AU - Mujahid, Rana
AU - Riaz, Asim
AU - Insyani, Rizki
AU - Kim, Jaehoon
N1 - Publisher Copyright:
© 2019 Elsevier Ltd
PY - 2020/2/15
Y1 - 2020/2/15
N2 - A new “centrifuge-first” approach was developed to recover a large amount of bio-oil produced during hydrothermal liquefaction (HTL) of dewatered sewage sludge (DWSS). The entire mixture produced from HTL was first centrifuged to separate the water + water-soluble organics (WSOs) phase from the bio-oil (BO) + solid residue phase, and subsequently, bio-oil was separated from solid residue by simple filtering. The HTL of DWSS at an optimum condition of 325 °C and 12–14 MPa for 30 min resulted in a DWSS conversion of 88%. Under this optimum condition, using the centrifuge-first approach, the yield of bio-oil recovered was 64 wt%, a value that was much higher than that of LLE with dichloromethane (47 wt%) or ethyl acetate (41 wt%). The centrifuge-first approach can be applied to recover bio-oil produced at a variety of HTL parameters, including temperature (300–400 °C), time (30–120 min), and pressure (25–36 MPa). The O/C ratios, calorific values of the bio-oils, and average molecular weights were in the range of 0.03–0.05, 33–36 MJ kg−1, and 130–190 g mol−1, respectively, demonstrating that they were not very sensitive to the process parameters. In addition to the high energy content, the low water content (<1 wt%), low inorganic content (<1 wt%), and low acidity (total acid number <26 mg KOH per g oil) in the bio-oil recovered from the centrifuge-first approach make its use in combustion fuel applications suitable. The major composition of the bio-oils was aromatics, N-cyclic species, and long-chain hydrocarbons.
AB - A new “centrifuge-first” approach was developed to recover a large amount of bio-oil produced during hydrothermal liquefaction (HTL) of dewatered sewage sludge (DWSS). The entire mixture produced from HTL was first centrifuged to separate the water + water-soluble organics (WSOs) phase from the bio-oil (BO) + solid residue phase, and subsequently, bio-oil was separated from solid residue by simple filtering. The HTL of DWSS at an optimum condition of 325 °C and 12–14 MPa for 30 min resulted in a DWSS conversion of 88%. Under this optimum condition, using the centrifuge-first approach, the yield of bio-oil recovered was 64 wt%, a value that was much higher than that of LLE with dichloromethane (47 wt%) or ethyl acetate (41 wt%). The centrifuge-first approach can be applied to recover bio-oil produced at a variety of HTL parameters, including temperature (300–400 °C), time (30–120 min), and pressure (25–36 MPa). The O/C ratios, calorific values of the bio-oils, and average molecular weights were in the range of 0.03–0.05, 33–36 MJ kg−1, and 130–190 g mol−1, respectively, demonstrating that they were not very sensitive to the process parameters. In addition to the high energy content, the low water content (<1 wt%), low inorganic content (<1 wt%), and low acidity (total acid number <26 mg KOH per g oil) in the bio-oil recovered from the centrifuge-first approach make its use in combustion fuel applications suitable. The major composition of the bio-oils was aromatics, N-cyclic species, and long-chain hydrocarbons.
KW - Bio-oil
KW - Centrifugation-first approach
KW - Dewatered sewage sludge
KW - Hydrothermal liquefaction
KW - Separation
UR - https://www.scopus.com/pages/publications/85075741574
U2 - 10.1016/j.fuel.2019.116628
DO - 10.1016/j.fuel.2019.116628
M3 - Article
AN - SCOPUS:85075741574
SN - 0016-2361
VL - 262
JO - Fuel
JF - Fuel
M1 - 116628
ER -