TY - JOUR
T1 - Valorization of Waste Lipids through Hydrothermal Catalytic Conversion to Liquid Hydrocarbon Fuels with in Situ Hydrogen Production
AU - Kim, Dongwook
AU - Vardon, Derek R.
AU - Murali, Dheeptha
AU - Sharma, Brajendra K.
AU - Strathmann, Timothy J.
N1 - Funding Information:
Support for D.K. was provided by a STX Scholarship Foundation. Support for DRV was provided by a National Science Foundation Graduate Research Fellowship (DGE-1144245). In addition, financial support was provided by National Science Foundation Division of Chemical, Bioengineering, Environmental, and Transport Systems (CBET-1555549). Joe Pickowitz (ISTC-UIUC) is acknowledged for supplying sewer trap grease, WVO, and DDGS oil; and John Scott (ISTC-UIUC) is acknowledged for providing assistance with analytical equipment used in analysis.
Publisher Copyright:
© 2016 American Chemical Society.
Copyright:
Copyright 2017 Elsevier B.V., All rights reserved.
PY - 2016/3/7
Y1 - 2016/3/7
N2 - We demonstrate hydrothermal (300°C, 10 MPa) catalytic conversion of real waste lipids (e.g., waste vegetable oil, sewer trap grease) to liquid hydrocarbon fuels without net need for external chemical inputs (e.g., H2 gas, methanol). A supported bimetallic catalyst (Pt-Re/C; 5 wt % of each metal) previously shown to catalyze both aqueous phase reforming of glycerol (a triacylglyceride lipid hydrolysis coproduct) to H2 gas and conversion of oleic and stearic acid, model unsaturated and saturated fatty acids, to linear alkanes was applied to process real waste lipid feedstocks in water. For reactions conducted with an initially inert headspace gas (N2), waste vegetable oil (WVO) was fully converted into linear hydrocarbons (C15-C17) and other hydrolyzed byproducts within 4.5 h, and H2 gas production was observed. Addition of H2 to the initial reactor headspace accelerated conversion, but net H2 production was still observed, in agreement with results obtained for aqueous mixtures containing model fatty acids and glycerol. Conversion to liquid hydrocarbons with net H2 production was also observed for a range of other waste lipid feedstocks (animal fat residuals, sewer trap grease, dry distiller's grain oil, coffee oil residual). These findings demonstrate potential for valorization of waste lipids through conversion to hydrocarbons that are more compatible with current petroleum-based liquid fuels than the biodiesel and biogas products of conventional waste lipid processing technologies.
AB - We demonstrate hydrothermal (300°C, 10 MPa) catalytic conversion of real waste lipids (e.g., waste vegetable oil, sewer trap grease) to liquid hydrocarbon fuels without net need for external chemical inputs (e.g., H2 gas, methanol). A supported bimetallic catalyst (Pt-Re/C; 5 wt % of each metal) previously shown to catalyze both aqueous phase reforming of glycerol (a triacylglyceride lipid hydrolysis coproduct) to H2 gas and conversion of oleic and stearic acid, model unsaturated and saturated fatty acids, to linear alkanes was applied to process real waste lipid feedstocks in water. For reactions conducted with an initially inert headspace gas (N2), waste vegetable oil (WVO) was fully converted into linear hydrocarbons (C15-C17) and other hydrolyzed byproducts within 4.5 h, and H2 gas production was observed. Addition of H2 to the initial reactor headspace accelerated conversion, but net H2 production was still observed, in agreement with results obtained for aqueous mixtures containing model fatty acids and glycerol. Conversion to liquid hydrocarbons with net H2 production was also observed for a range of other waste lipid feedstocks (animal fat residuals, sewer trap grease, dry distiller's grain oil, coffee oil residual). These findings demonstrate potential for valorization of waste lipids through conversion to hydrocarbons that are more compatible with current petroleum-based liquid fuels than the biodiesel and biogas products of conventional waste lipid processing technologies.
KW - Aqueous phase reforming
KW - Decarbonylation
KW - Decarboxylation
KW - Deoxygenation
KW - Hydrogenation
KW - Waste fats and grease
KW - Waste-to-energy
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U2 - 10.1021/acssuschemeng.5b01768
DO - 10.1021/acssuschemeng.5b01768
M3 - Article
AN - SCOPUS:84960194245
SN - 2168-0485
VL - 4
SP - 1775
EP - 1784
JO - ACS Sustainable Chemistry and Engineering
JF - ACS Sustainable Chemistry and Engineering
IS - 3
ER -