Key Laboratory for Industrial Biocatalysis, Ministry of Education of China, Institute of Applied Chemistry, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China.
School of Chemistry and Chemical Engineering, Guangxi University for Nationalities, Nanning, Guangxi 530006, China.
Bioresour Technol. 2018 Aug;261:52-61. doi: 10.1016/j.biortech.2018.03.140. Epub 2018 Apr 5.
A shrinking-layer model by modification of classical shrinking-core model was developed based on cell wall multi-layered structure for delignification of sugarcane bagasse with sulfuric acid (SA) catalyzed atmospheric acetic acid (AA) fractionation. The general model for overall rate of delignification was obtained and further employed to evaluate the mass transfer effects on delignification. It was found that the external diffusion could be neglected under the studied fractionation conditions, while the internal diffusion appeared to play an important role. The effective diffusion coefficient for lignin within the biomass was estimated as 6.7 × 10-1.6 × 10 m/s depending on temperature, solid content in the system and molecular weight of lignin. However, surface reaction also seems to be a limiting step to the overall rate of delignification. At the early stage of delignification, both internal diffusion and reaction were controlling steps, while at the late stage reaction seems to be the controlling step.
基于细胞壁多层结构,针对甘蔗渣的亚硫酸氢盐-乙酸法(SA-AA)分步蒸煮脱木质素过程,开发了一种改进的收缩核模型。得到了整体脱木质素速率的通用模型,并进一步用于评价传质对脱木质素的影响。结果表明,在所研究的分步蒸煮条件下,可以忽略外扩散,而内扩散似乎起着重要作用。根据温度、体系中固含量和木质素分子量,生物质内木质素的有效扩散系数估计为 6.7×10-1.6×10-6m/s。然而,表面反应似乎也是整体脱木质素速率的限制步骤。在脱木质素的早期阶段,内扩散和反应都是控制步骤,而在后期反应似乎是控制步骤。