Conceptual Process Design and Economics for the Production of High-Octane Gasoline Blendstock via Indirect Liquefaction of Biomass through Methanol/Dimethyl Ether Intermediates

Eric Tan, Michael Talmadge, Jesse Hensley, Joshua Schaidle, Abhijit Dutta, Lesley Snowden-Swan, David Humbird, Mary Biddy

Research output: Contribution to journalArticlepeer-review

42 Scopus Citations

Abstract

This work describes in detail one potential conversion process for the production of high-octane gasoline blendstock via indirect liquefaction of biomass. The processing steps of this pathway include the conversion of biomass to synthesis gas via indirect gasification, gas clean-up via reforming of tars and other hydrocarbons, catalytic conversion of syngas to methanol, methanol dehydration to dimethyl ether (DME), and the homologation of DME over a zeolite catalyst to high-octane gasoline-range hydrocarbon products. The current process configuration has similarities to conventional methanol-to-gasoline (MTG) technologies, but there are key distinctions, specifically regarding the product slate, catalysts, and reactor conditions. A techno-economic analysis is performed to investigate the production of high-octane gasoline blendstock. The design features a processing daily capacity of 2000 tonnes (2205 short tons) of dry biomass. The process yields 271 liters of liquid fuel per dry tonne of biomass (65 gal/dry ton), for an annual fuel production rate of 178 million liters (47 MM gal) at 90% on-stream time. The estimated total capital investment for an nth-plant is $438 million. The resulting minimum fuel selling price (MFSP) is $0.86 per liter or $3.25 per gallon in 2011 US dollars. A rigorous sensitivity analysis captures uncertainties in costs and plant performance. Sustainability metrics for the conversion process are quantified and assessed. The potential premium value of the high-octane gasoline blendstock is examined and found to be at least as competitive as fossil-derived blendstocks. A simple blending strategy is proposed to demonstrate the potential for blending the biomass-derived blendstock with petroleum-derived intermediates. Published 2015. This article is a U.S. Government work and is in the public domain in the USA. Biofuels, Bioproducts and Biorefining published by Society of Industrial Chemistry and John Wiley & Sons Ltd.

Original languageAmerican English
Pages (from-to)17-35
Number of pages19
JournalBiofuels, Bioproducts and Biorefining
Volume10
Issue number1
DOIs
StatePublished - 2016

Bibliographical note

Publisher Copyright:
© 2016 Society of Chemical Industry and John Wiley & Sons, Ltd.

NREL Publication Number

  • NREL/JA-5100-65305

Keywords

  • Biomass
  • Dimethyl ether homologation
  • High-octane gasoline
  • Indirect gasification
  • Process design
  • Sustainability
  • Techno-economic analysis
  • Thermochemical conversion

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