详细信息
Rigorous Calculation of Greenhouse Gases (GHG) in Sustainable L-lactic Acid Production from Lignocellulosic Biomass based on Advanced Biorefinery Processing Technology ( SCI-EXPANDED收录 EI收录)
文献类型:期刊文献
英文题名:Rigorous Calculation of Greenhouse Gases (GHG) in Sustainable L-lactic Acid Production from Lignocellulosic Biomass based on Advanced Biorefinery Processing Technology
作者:Wang, Ya[1,2];Zhang, Bin[2];Bao, Jie[1,2]
机构:[1]Shihezi Univ, Sch Chem & Chem Engn, Shihezi 832000, Xinjiang, Peoples R China;[2]East China Univ Sci & Technol, State Key Lab Bioreactor Engn, Shanghai 200237, Peoples R China
年份:2025
卷号:13
期号:17
起止页码:6186
外文期刊名:ACS SUSTAINABLE CHEMISTRY & ENGINEERING
收录:;EI(收录号:20251718279924);WOS:【SCI-EXPANDED(收录号:WOS:001471387000001)】;
基金:This research was supported by the National Key R&D Program of China (2023YFA0914400) and the National Natural Science Foundation of China (32301269).
语种:英文
外文关键词:GHG emission; L-lactic acid; cornstover; dry biorefining; wastewater; lignincombustion
摘要:Utilizing lignocellulosic biomass to produce high-purity L-lactic acid as the monomer of poly(lactic acid) (PLA) is an important pathway for reducing greenhouse gas (GHG) emissions. This study developed an Aspen Plus simulation model and a life-cycle assessment model for producing high-purity L-lactic acid using corn stover feedstock based on thermodynamic principles and experimental data. An advanced dry biorefinery technology is selected as the process platform because of its high conversion performance, close to the dry milling of corn, as well as the significantly reduced energy consumption and wastewater generation. The GHG emissions of corn stover during the growth period are not considered due to its agricultural waste property and to prevent double counting from corn. Full evaporation of wastewater is used to provide process water and steam supplies, considering the weak infrastructure for wastewater treatment and the freshwater supply in agricultural regions. The rigorous calculations show that producing one metric ton of purified L-lactic acid consumes 2.87 ton of corn stover as carbohydrate feedstock, 219.3 kWh of electricity, and 2.98 ton of fresh water for process use with the generation of 1.24 ton of wastewater. No external heat energy input is needed, because the lignin residue combustion provides sufficient heat energy for process use. Based on the detailed data, the calculated GHG emissions for producing one kg L-lactic acid by dry biorefining of corn stover is 0.618 kg CO2 equiv which is only 18% of that produced by dry milling of corn. This study provides an important sustainability basis and decision-making support for biobased plastic implementation.
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