Biomass to Liquid Transportation Fuels via Biological and Thermochemical Conversion: Process Synthesis and Global Optimization Strategies

被引:22
|
作者
Matthews, Logan R. [1 ,2 ,3 ]
Niziolek, Alexander M. [1 ,2 ,3 ]
Onel, Onur [1 ,2 ,3 ]
Pinnaduwage, Neesha [3 ]
Floudas, Christodoulos A. [1 ,2 ]
机构
[1] Texas A&M Univ, Artie McFerrin Dept Chem Engn, College Stn, TX 77843 USA
[2] Texas A&M Univ, Texas A&M Energy Inst, College Stn, TX 77843 USA
[3] Princeton Univ, Dept Chem & Biol Engn, Princeton, NJ 08544 USA
基金
美国国家科学基金会;
关键词
NATURAL-GAS PROCESSES; MIXALCO PROCESS; HYDROCARBON BIOREFINERY; TECHNOECONOMIC ANALYSIS; CATALYTIC CONVERSION; CARBOXYLATE PLATFORM; SUSTAINABLE DESIGN; ROBUST SOLUTIONS; HYBRID BIOMASS; COAL;
D O I
10.1021/acs.iecr.5b03319
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Biological conversion of biomass into gasoline, diesel, and kerosene provides an alternative means to meet liquid transportation fuel demand, going beyond the traditional thermochemical methods involving gasification, Fischer-Tropsch conversion) and methanol synthesis. Process synthesis is an ideal methodology for comparing the developing biological technologies with established thermochemical methods through input-output modeling of biorefinery units and inclusion in a superstructure. The resulting model takes the form of a mixed-integer nonlinear optimization problem with full heat, power, and water integration. In the novel superstructure, the MixAlco process for biological conversion is modeled, in which biomass is fermented into carboxylic acid salts which are further upgraded into liquid transportation fuels. The model is solved to global optimality based on the minimization of the cost of liquid transportation fuels production using a branch-and-bound global optimization algorithm to provide upper bound Solutions, valid lower bound solutions, and an optimality gap. Case studies analyze the performance of the MixAlco process relative to the existing Fischer-Tropsch and methanol synthesis routes when switchgrass is used as the biomass feedstock at capacities ranging from 1000 bbl per day to 200 000 bbl per day of gasoline equivalent liquid transportation fuels by energy content. From an economic perspective, the MixAlco process is not competitive with the existing methods, with break-even oil prices from $102.08/bbl to $169.06/bbl. However, a combined MixAlco thermochemical process is also analyzed, with leftover biomass residue from the fermenter converted into synthesis gas and upgraded to fuels. This proposed process provides break-even oil prices of $79.40/bbl to $144.00/bbl, competitive with and even sometimes outperforming the thermochemical methods for fuel production from biomass. The processes are also analyzed for their greenhouse gas impact, and parametric analysis is conducted on investment cost and switchgrass price parameters to study their impact on the biorefineries.
引用
收藏
页码:3203 / 3225
页数:23
相关论文
共 50 条
  • [31] CONVERSION OF NATURAL-GAS TO TRANSPORTATION FUELS VIA THE SHELL MIDDLE DISTILLATE SYNTHESIS PROCESS (SMDS)
    VANWECHEM, VMH
    SENDEN, MMG
    NATURAL GAS CONVERSION II, 1994, 81 : 43 - 71
  • [32] A review of conversion of lignocellulose biomass to liquid transport fuels by integrated refining strategies
    Wang, Chenguang
    Zhang, Xinghua
    Liu, Qiang
    Zhang, Qi
    Chen, Lungang
    Ma, Longlong
    FUEL PROCESSING TECHNOLOGY, 2020, 208
  • [33] Review of recent reports on process technology for thermochemical conversion of whole algae to liquid fuels
    Elliott, Douglas C.
    ALGAL RESEARCH-BIOMASS BIOFUELS AND BIOPRODUCTS, 2016, 13 : 255 - 263
  • [34] Conversion of biomass to sugars via ionic liquid hydrolysis: process synthesis and economic evaluation
    Sen, S. Murat
    Binder, Joseph B.
    Raines, Ronald T.
    Maravelias, Christos T.
    BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR, 2012, 6 (04): : 444 - 452
  • [35] A critical review of separation technologies in lignocellulosic biomass conversion to liquid transportation fuels production processes
    Ibarra-Gonzalez, Paola
    Christensen, Lars Porskjaer
    Ronga, Ben-Guang
    CHEMICAL ENGINEERING COMMUNICATIONS, 2022, 209 (04) : 529 - 554
  • [36] A strategy for the simultaneous catalytic conversion of hemicellulose and cellulose from lignocellulosic biomass to liquid transportation fuels
    Han, Jeehoon
    Sen, S. Murat
    Alonso, David Martin
    Dumesic, James A.
    Maravelias, Christos T.
    GREEN CHEMISTRY, 2014, 16 (02) : 653 - 661
  • [37] Hardwood Biomass to Gasoline, Diesel, and Jet Fuel: 1. Process Synthesis and Global Optimization of a Thermochemical Refinery
    Baliban, Richard C.
    Elia, Josephine A.
    Floudas, Christodoulos A.
    Gurau, Barri
    Weingarten, Michael B.
    Klotz, Stephen D.
    ENERGY & FUELS, 2013, 27 (08) : 4302 - 4324
  • [38] Conversion of carbon dioxide and methane in biomass synthesis gas for liquid fuels production
    Chattanathan, Shyamsundar Ayalur
    Adhikari, Sushil
    Taylor, Steven
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (23) : 18031 - 18039
  • [39] Thermochemical production of liquid fuels from biomass: Thermo-economic modeling, process design and process integration analysis
    Tock, Laurence
    Gassner, Martin
    Marechal, Francois
    BIOMASS & BIOENERGY, 2010, 34 (12): : 1838 - 1854
  • [40] Process systems engineering studies for the synthesis of catalytic biomass-to-fuels strategies
    Han, Jeehoon
    Sen, S. Murat
    Luterbacher, Jeremy S.
    Alonso, David Martin
    Dumesic, James A.
    Maravelias, Christos T.
    COMPUTERS & CHEMICAL ENGINEERING, 2015, 81 : 57 - 69