Comparative techno-economic analysis and process design for indirect liquefaction pathways to distillate-range fuels via biomass-derived oxygenated intermediates upgrading

被引:36
作者
Tan, Eric C. D. [1 ]
Snowden-Swan, Lesley J. [2 ]
Talmadge, Michael [3 ]
Dutta, Abhijit [4 ]
Jones, Susanne [5 ]
Ramasamy, Karthikeyan K. [6 ]
Gray, Michel [7 ]
Dagle, Robert [8 ]
Padmaperuma, Asanga [9 ]
Gerber, Mark [8 ]
Sahir, Asad H. [10 ]
Tao, Ling [11 ]
Zhang, Yanan [4 ]
机构
[1] Natl Renewable Energy Lab, Biorefinery Anal Grp, Natl Bioenergy Ctr, Golden, CO USA
[2] Pacific Northwest Natl Lab, Technoecon Anal & Life Cycle Anal Bioenergy Syst, Richland, WA USA
[3] Natl Renewable Energy Lab, Natl Bioenergy Ctr, Golden, CO USA
[4] Natl Renewable Energy Lab, Golden, CO 80401 USA
[5] Pacific Northwest Natl Lab, Technoecon Anal, Richland, WA USA
[6] Pacific Northwest Natl Lab, Res & Proc Dev Producing Specialty Chem & Infrast, Richland, WA USA
[7] Pacific Northwest Natl Lab, Biofuels Res, Richland, WA USA
[8] Pacific Northwest Natl Lab, Richland, WA USA
[9] Pacific Northwest Natl Lab, Energy & Efficiency Div, Richland, WA USA
[10] Natl Renewable Energy Lab, Natl Bioenergy Ctr, Res Projects Related Conceptual Proc Design Techn, Golden, CO USA
[11] Natl Renewable Energy Lab, Technoecon Anal Projects, Golden, CO USA
来源
BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR | 2017年 / 11卷 / 01期
关键词
biomass; biorefinery; biofuel; indirect liquefaction; oxygenates; process design; techno-economic analysis; sustainability; ENVIRONMENTAL SUSTAINABILITY IMPACTS; THERMOCHEMICAL CONVERSION; PRODUCT DISTRIBUTION; MIXED OXIDES; CATALYSTS; ETHANOL; GAS; SYNGAS; SYSTEM;
D O I
10.1002/bbb.1710
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
This paper presents a comparative techno-economic analysis (TEA) of five conversion pathways from biomass to gasoline-, jet-, and diesel-range hydrocarbons via indirect liquefaction with a specific focus on pathways utilizing oxygenated intermediates. The four emerging pathways of interest are compared with one conventional pathway (Fischer-Tropsch) for the production of the hydrocarbon blendstocks. The processing steps of the four emerging pathways include biomass-to-syngas via indirect gasification, syngas clean-up, conversion of syngas to alcohols/oxygenates followed by conversion of alcohols/oxygenates to hydrocarbon blendstocks via dehydration, oligomerization, and hydrogenation. Conversion of biomass-derived syngas to oxygenated intermediates occurs via three different pathways, producing: (i) mixed alcohols over a MoS2 catalyst, (ii) mixed oxygenates (a mixture of C2+ oxygenated compounds, predominantly ethanol, acetic acid, acetaldehyde, ethyl acetate) using an Rh-based catalyst, and (iii) ethanol from syngas fermentation. This is followed by the conversion of oxygenates/alcohols to fuel-range olefins in two approaches: (i) mixed alcohols/ethanol to 1-butanol rich mixture via Guerbet reaction, followed by alcohol dehydration, oligomerization, and hydrogenation, and (ii) mixed oxygenates/ethanol to isobutene rich mixture and followed by oligomerization and hydrogenation. The design features a processing capacity of 2000 tonnes/day (2205 short tons) of dry biomass. The minimum fuel selling prices (MFSPs) for the four developing pathways range from $3.40 to $5.04 per gasoline-gallon equivalent (GGE), in 2011 US dollars. Sensitivity studies show that MFSPs can be improved with co-product credits and are comparable to the commercial Fischer-Tropsch benchmark ($3.58/GGE). Overall, this comparative TEA study documents potential economics for the developmental biofuel pathways via mixed oxygenates. (c) 2016 Society of Chemical Industry and John Wiley & Sons, Ltd
引用
收藏
页码:41 / 66
页数:26
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