Understanding cost drivers and economic potential of two variants of ionic liquid pretreatment for cellulosic biofuel production

被引:96
作者
Konda, N. V. S. N. Murthy [1 ,2 ]
Shi, Jian [1 ,3 ]
Singh, Seema [1 ,3 ]
Blanch, Harvey W. [1 ,2 ,4 ]
Simmons, Blake A. [1 ,3 ]
Klein-Marcuschamer, Daniel [1 ,2 ,5 ]
机构
[1] Joint BioEnergy Inst, Emeryville, CA 94608 USA
[2] Lawrence Berkeley Natl Lab, Phys Biosci Div, Berkeley, CA 94720 USA
[3] Sandia Natl Labs, Biol & Mat Sci Ctr, Livermore, CA 94551 USA
[4] Univ Calif Berkeley, Dept Chem Engn, Berkeley, CA 94720 USA
[5] Univ Queensland, Dow Ctr Sustainable Engn Innovat, St Lucia, Qld, Australia
关键词
Lignocellulosic biofuels; Ionic liquid pretreatment; Techno-economic analysis; One-pot process; Lignin valorization; Process modeling; TECHNOECONOMIC ANALYSIS; ENZYMATIC-HYDROLYSIS; SUGARS; BIOMASS; BIOREFINERY; RECOVERY;
D O I
10.1186/1754-6834-7-86
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
Background: Ionic liquid (IL) pretreatment could enable an economically viable route to produce biofuels by providing efficient means to extract sugars and lignin from lignocellulosic biomass. However, to realize this, novel IL-based processes need to be developed in order to minimize the overall production costs and accelerate commercial viability. In this study, two variants of IL-based processes are considered: one based on complete removal of the IL prior to hydrolysis using a water-wash (WW) step and the other based on a "one-pot" (OP) process that does not require IL removal prior to saccharification. Detailed techno-economic analysis (TEA) of these two routes was carried out to understand the cost drivers, economic potential (minimum ethanol selling price, MESP), and relative merits and challenges of each route. Results: At high biomass loading (50%), both routes exhibited comparable economic performance with an MESP of $6.3/gal. With the possible advances identified (reduced water or acid/base consumption, improved conversion in pretreatment, and lignin valorization), the MESP could be reduced to around $3/gal ($3.2 in the WW route and $2.8 in the OP route). Conclusions: It was found that, to be competitive at industrial scale, lowered cost of ILs used and higher biomass loadings (50%) are essential for both routes, and in particular for the OP route. Overall, while the economic potential of both routes appears to be comparable at higher biomass loadings, the OP route showed the benefit of lower water consumption at the plant level, an important cost and sustainability consideration for biorefineries.
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页数:11
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