Cited by 104Catalysis and Hydrodesulfurization StudiesCatalysts for Methane ReformingCatalysis for Biomass Conversion

Converting Algal Triglycerides to Diesel and HEFA Jet Fuel Fractions

Robota, Heinz J., Alger, Jhoanna C., Shafer, Linda·2013·Energy & Fuels

Abstract

Over 2 L of algal triglycerides were first converted to n -alkanes using a 3% Pd/carbon catalyst in a fixed bed reactor at 350 °C under 800 psig of H 2 . The starting triglyceride was composed of 10.5% C 16 and 85.2% C 18 fatty acids. The Pd/C catalyst exhibited primarily decarbonylation and total reduction deoxygenation pathways, which changed in relative contribution over the nearly 200 h of continuous operation. Both the C 18 /(C 18 +C 17 ) and C 16 /(C 16 +C 15 ) product ratios changed from 0.3 at the start of the deoxygenation run to 0.6 at its conclusion. Overall, the catalyst became more active during the run. After a first pass deoxygenation, over 85% of the product was composed of n -alkanes divided nearly equally between the C n and C n –1 chain lengths corresponding to the starting fatty acid chain lengths. The alkanes along with a few percent 1-alcohols were separated from the remaining incompletely converted components by distillation and subjected to a polishing hydrogenation using a 0.5% Pt/alumina catalyst. A portion of this first pass n -alkane composite was hydroisomerized to improve its cold flow properties using a 0.5% Pt/US-Y zeolite catalyst. Even with an iso/normal ratio of just over 1 in the product stream, the mixture solidified near ambient temperature. To further improve the cold flow properties of this diesel composition, it was subjected to a solvent dewaxing procedure, which yielded a product that remained liquid at −20 °C. The incompletely converted components remaining after the first pass deoxygenation were subjected to a second deoxygenation pass under the same conditions used for the fresh triglycerides. The product alkanes were again separated by distillation, alcohols were reduced to alkanes, and a single composite alkane mixture was prepared by combining the first and second pass alkanes. Overall, more than 95% of the product stream produced by the two deoxygenation passes was composed of n -alkanes. This final composite mixture was processed further to a HEFA (hydrotreated esters and fatty acids) jet composition using the same 0.5% Pt/US-Y zeolite catalyst at three different conversion severities. With single pass cracking conversions of 43%, 59%, and 93%, yield losses of 41%, 44%, and 75% to a C 8– naphtha fraction were observed. Such high yield losses argue against a strategy where HEFA jet is the primarily targeted product. We suggest a strategy in which the yield loss to naphtha can be limited to less than 10% based on making principally a renewable diesel fuel from which a HEFA jet can be extracted as a minority product.

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Crossref · 10.1021/ef301977b

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Authors
Robota, H. J., Alger, J. C., & Shafer, L.
Affiliations
University of Dayton Research Institute (US)
Corresponding author
Robota, Heinz J.
Venue
Energy & Fuels
Published
2013-02-07
Volume
27
Issue
2
Pages
985-996
ISSN
  • 0887-0624 (ISSN-L)
  • 1520-5029
OpenAlex
W2325000870
Cited by
104
References
19
Citations by year
2026: 5 · 2025: 7 · 2024: 10 · 2023: 4 · 2022: 5 · 2021: 9 · 2020: 9 · 2019: 11 · 2018: 10 · 2017: 15 · 2016: 6 · 2015: 8 · 2014: 5
FWCI
8.40
Type
journal article
Language
en
Open access
closed
Locations
Energy & Fuels (publishedVersion)
Topics
  • Physical Sciences › Engineering › Mechanical Engineering › Catalysis and Hydrodesulfurization Studies
  • Physical Sciences › Chemical Engineering › Catalysis › Catalysts for Methane Reforming
  • Physical Sciences › Engineering › Biomedical Engineering › Catalysis for Biomass Conversion
Keywords
deoxygenation, palladium on carbon, Pt/Al2O3 catalyst, hydroisomerization, solvent dewaxing, diesel fuel, cold flow properties, catalyst deactivation, biodiesel upgrading, fixed-bed reactor

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