Premium
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.
Accelerating Research
Robert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom
Address
John Eccles HouseRobert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom