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Techno-economic prospects for producing Fischer-Tropsch jet fuel and electricity from lignite and woody biomass with CO2 capture for EOR

Journal Article · · Applied Energy
 [1];  [2];  [3];  [3];  [4];  [2]
  1. Princeton Univ., NJ (United States). Andlinger Center for Energy and the Environment; Princeton Univ., NJ (United States)
  2. Princeton Univ., NJ (United States). Andlinger Center for Energy and the Environment
  3. Dept. of Energy Politecnico di Milano, Milano (Italy)
  4. Princeton Univ., NJ (United States). Andlinger Center for Energy and the Environment; Univ. of Queensland, Brisbane, QLD (Australia). Dow Center for Sustainable Engineering Innovation. Energy Initiative
This work explores the prospective techno-economic performance of facilities that produce low- and net-negative-carbon liquid transportation fuels and electricity with CO2 capture for enhanced oil recovery. The lignite and biomass-to-jet fuel process is based on KBR’s TRIG gasifier, Rectisol (for sulfur removal and CO2 capture), fixed-bed low temperature Fischer-Tropsch synthesis of liquid fuels, and Brayton/Rankine combined cycles to convert synthesis/refining off-gases and waste heat to electricity. This work leverages a recent, highly-detailed assessment of a prospective first-of-a-kind (FOAK) demonstration facility to develop highly detailed Aspen Plus process simulations for nine prospective Nth-of-a-kind (NOAK) plant equipment configurations. Component-level capital costs from the FOAK study are scaled and adjusted to reflective prospective learning-by-doing to estimate capital costs for the NOAK designs. NOAK plant economic performance is found to be largely insensitive to variations in plant configurations and electricity output fraction, but biomass input fraction significantly affects profitability. Facilities that consume only carbon–neutral biomass, with no lignite co-feed, have significantly net-negative carbon emissions and the most favorable prospective economics when carbon emissions are priced. For these facilities, the crude oil price required for plant economic viability falls rapidly from $$\$$$$100/bbl as carbon emission prices increase above $$\$$$$120/tonne CO2eq. In general, plants that co-fire lignite with biomass are less profitable (than 100% biomass plants) due to their higher net greenhouse gas emissions.
Research Organization:
Princeton University, NJ (United States)
Sponsoring Organization:
USDOE; USDOE Office of Fossil Energy (FE)
Grant/Contract Number:
FE0023697
OSTI ID:
1849135
Alternate ID(s):
OSTI ID: 1809868
Journal Information:
Applied Energy, Journal Name: Applied Energy Journal Issue: C Vol. 279; ISSN 0306-2619
Publisher:
ElsevierCopyright Statement
Country of Publication:
United States
Language:
English

References (25)

Metal dusting of high temperature alloys journal March 1993
Occurrence of metal dusting– referring to failure cases journal October 2003
Economic and environmental evaluation of coal-and-biomass-to-liquids-and-electricity plants equipped with carbon capture and storage journal August 2015
Process integration: Selection of the optimal utility system journal March 1998
Targeting the optimal integration of steam networks: Mathematical tools and methodology journal June 1999
Shell coal IGCCS with carbon capture: Conventional gas quench vs. innovative configurations journal November 2011
Heat integration and heat recovery steam cycle optimization for a low-carbon lignite/biomass-to-jet fuel demonstration project journal April 2019
Design and analysis of a low-carbon lignite/biomass-to-jet fuel demonstration project journal February 2020
MINLP model and two-stage algorithm for the simultaneous synthesis of heat exchanger networks, utility systems and heat recovery cycles journal November 2017
A bilevel decomposition method for the simultaneous heat integration and synthesis of steam/organic Rankine cycles journal September 2019
A systematic methodology for the techno-economic optimization of Organic Rankine Cycles journal September 2017
Investment and production costs of synthetic fuels – A literature survey journal March 2014
Plant-wide modeling of an indirect coal–biomass to liquids (CBTL) plant with CO2 capture and storage (CCS) journal December 2014
The cost of CO2 capture and storage journal September 2015
Decarbonized hydrogen and electricity from natural gas journal July 2005
Co-production of hydrogen, electricity and CO from coal with commercially ready technology. Part B: Economic analysis journal July 2005
Technical review on jet fuel production journal September 2013
Biomass to liquid transportation fuel via Fischer Tropsch synthesis – Technology review and current scenario journal May 2016
Techno-Economic Analysis of a Novel Indirect Coal–Biomass to Liquids Plant Integrated with a Combined Cycle Plant and CO 2 Capture and Storage journal February 2016
Making Fischer−Tropsch Fuels and Electricity from Coal and Biomass: Performance and Cost Analysis journal January 2011
Coal and Biomass to Liquid Transportation Fuels: Process Synthesis and Global Optimization Strategies journal May 2014
Using An Hyperbola as a Transition Model to Fit Two-Regime Straight-Line Data journal August 1974
Using Hydrogen as Gas Turbine Fuel journal January 2005
Using Hydrogen as Gas Turbine Fuel: Premixed Versus Diffusive Flame Combustors journal January 2014
Fundamental Impact of Firing Syngas in Gas Turbines conference March 2009