生物燃料
生物净化
玉米秸秆
生物炼制
生物过程
制浆造纸工业
木质纤维素生物量
生物量(生态学)
生物能源
原材料
发酵
乙醇燃料
厌氧消化
废物管理
碳纤维
化学
沼气
沼渣
生化工程
环境科学
生物技术
纤维素酶
产甲烷
洗手液
乙醇发酵
可再生能源
过程(计算)
生物制品
玉米乙醇
作者
Tianjie Ao,Yiping Luo,Javier Remón,Jie Wu,Fang Deng,Dong Li,Chen‐Guang Liu,Feng‐Wu Bai
标识
DOI:10.1021/acs.est.5c14410
摘要
Conventional biorefining of lignocellulosic biomass, such as corn stover (CS), is hampered by poor carbon efficiency, as nearly half of the substrate carbon is lost as CO2 during ethanol fermentation. This study presents a holistically integrated cascade process designed to capture and valorize all major carbon streams. The system synergistically couples three stages: (1) high-productivity ethanol fermentation (1.68 g/L/h) using the engineered yeast Saccharomyces cerevisiae CE10; (2) anaerobic digestion of the resulting stillage, which efficiently converted residual organics into methane (171 L/kg COD) with ca. 80% COD removal; and (3) cultivation of the cyanobacterium Desertifilum tharense BERC03 using the nutrient-rich digestate and captured fermentation CO2. This integrated approach boosted the carbon utilization from a baseline of 48% to 62%. A comprehensive techno-economic analysis of an industrial-scale (2000 t/d) facility projected a Minimum Ethanol Selling Price (MESP) of $2.44 per gallon, a value approaching current market competitiveness. The analysis identified the feedstock (30%) and cellulase (17%) as the primary cost drivers. These findings demonstrate a validated biorefinery model that significantly enhances carbon recovery and outlines a viable pathway for the coproduction of multiple biofuels from lignocellulosic resources.
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