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Title: Upgrading biomass liquid fuels. [Wood-derived oil]

Conference ·
OSTI ID:6225011

Catalytic hydrotreating of wood-derived liquids is being studied using a continuous-feed, fixed-bed reactor. Commercial hydrotreating catalysts and conditions are used to hydrodeoxygenate and hydrocrack the biomass liquefaction products generated by high-pressure processing. Biomass flash pyrolyzates require alternate processing to first stabilize the products prior to catalytic hydrotreating. Experiments are performed in an upflow reactor wherein both liquid phase and gas phase reactions are considered to be important. Although hydrocarbons are not produced in any significant amount by thermochemical direct liquefaction of wood, the use of a secondary hydrogenation step to treat the initial product can result in nearly pure hydrocarbons. These hydrocarbons are primarily cyclics and aromatics which would be useful in gasoline blending. Experimental results with either cobalt/molybdenum or nickel/molybdenum catalyst show that deoxygenation of the primarily phenolic wood oil is achieved in either case. The extent of saturation of the liquid product is dependent on catalyst type, operating temperature and relative flows of oil feedstock and hydrogen gas. Future work will include new catalyst testing, longer term runs to better quantify carbon fouling of the catalyst bed and detailed chemical analysis of intermediate products to elucidate the process chemistry. 12 refs., 1 fig., 7 tabs.

Research Organization:
Pacific Northwest Labs., Richland, WA (USA)
DOE Contract Number:
AC06-76RL01830
OSTI ID:
6225011
Report Number(s):
PNL-SA-13476; CONF-8510167-3; ON: DE86004020
Resource Relation:
Conference: Biomass thermal chemical conversion contractors' meeting, Minneapolis, MN, USA, 15 Oct 1985
Country of Publication:
United States
Language:
English