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Upgraded biofuel from residue biomass by Thermo-Catalytic Reforming and hydrodeoxygenation
Affiliation:1. Department of Mechanical and Industrial Engineering, University of Toronto, 5 King''s College Road, M5S 3G8 Toronto, Ontario, Canada;2. Aerospace Research Center, National Research Council of Canada, 1200 Montreal Road, K1A 0R6 Ottawa, Ontario, Canada
Abstract:Research is focused on the utilisation of waste or residue biomass for bioenergy conversion. A promising conversion technology for the production of liquid biofuels from residue biomass is a process called Thermo-Catalytic Reforming (TCR®​) which is a combination of prior thermal treatment of the biomass at mild temperatures (intermediate pyrolysis) followed by a second catalytic treatment step at elevated temperatures (reforming). This article focuses on the conversion of TCR® liquids from digestate as a feedstock for subsequent hydrocarbon production. The generated bio-oil showed a lower heating value of 34.0 MJ kg1 with an oxygen content of 7.0% and a water content of 2.2%. The bio-oil was hydrodeoxygenated using an industrial NiMo–Al2O3 catalyst at temperatures of 503 K–643 K and a pressure of 14 MPa. The hydrodeoxygenated bio-oil reached a lower heating value of 42.3 MJ kg−1 with an oxygen content below 0.8 mg kg−1 and water content of 30 ppm. Product yields and catalyst life give confidence that upgrading of the TCR®​ bio-oil offers a suitable option to meet the high standards of common fuels.
Keywords:Thermo-Catalytic Reforming  Intermediate pyrolysis  Biofuel  Pyrolysis oil  Hydrodeoxygenation  Digestate  HDO"}  {"#name":"keyword"  "$":{"id":"kwrd0045"}  "$$":[{"#name":"text"  "_":"hydrodeoxygenation  LHV"}  {"#name":"keyword"  "$":{"id":"kwrd0055"}  "$$":[{"#name":"text"  "_":"lower heating value  LHSV"}  {"#name":"keyword"  "$":{"id":"kwrd0065"}  "$$":[{"#name":"text"  "_":"Liquid hourly space velocity  TAN"}  {"#name":"keyword"  "$":{"id":"kwrd0075"}  "$$":[{"#name":"text"  "_":"total acid number  Thermo-Catalytic Reforming
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