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Mild hydrotreating of biomass pyrolysis oils to produce a suitable refinery feedstock
Author(s) -
French Richard J.,
Hrdlicka Jason,
Baldwin Robert
Publication year - 2010
Publication title -
environmental progress and sustainable energy
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.495
H-Index - 66
eISSN - 1944-7450
pISSN - 1944-7442
DOI - 10.1002/ep.10419
Subject(s) - hydrodesulfurization , pyrolysis , refinery , raw material , oil refinery , fuel oil , waste management , diesel fuel , petroleum , pyrolysis oil , gasoline , petroleum product , distillation , kerosene , fluid catalytic cracking , refining (metallurgy) , environmental science , pulp and paper industry , chemistry , catalysis , organic chemistry , materials science , metallurgy , engineering
Fast pyrolysis produces a liquid product that represents ∼70% of the mass of the starting material. However, since the raw oil is highly corrosive, largely immiscible with hydrocarbons, and only partly volatile, it is unsuitable for use in a conventional petroleum refinery or as a finished fuel. Catalytic hydroprocessing can remove oxygen to make a gasoline‐ or diesel‐like product, but the processing costs have not been attractive. Economic analysis suggests that mild hydroprocessing, leaving 7 wt % oxygen in the pyrolysis oil reduce hydrotreating costs to a range that is more economically viable. If the physical and chemical properties of the mildly hydrotreated products were acceptable, these materials could potentially be available for coprocessing in a petroleum refinery leveraging the economies of scale and existing refining infrastructure to produce a lower‐cost product. Mildly hydrotreated pyrolysis oil with low acidity, good miscibility with hydrocarbons, and high volatility was generated in a semibatch laboratory reactor. A 0.5‐L sample was produced at 360°C, 2500 psig hydrogen, with a hydrogen flow of 0.22 sl/g‐oil/h and 10 wt % nickel‐molybdenum/Al 2 O 3 catalyst. Yields were 36% light product (7% oxygen) and 30% liquid residue. This oil will be subjected to further physical and chemical tests to determine the technical feasibility of co‐processing in a petroleum refinery. © 2010 American Institute of Chemical Engineers Environ Prog, 2010.