Model-based process intensification of dilute acid pre-hydrolysis of oil palm empty fruit bunch biomass for pretreatment and furfural production

被引:6
|
作者
Ouyang, Denghao [1 ,2 ]
Liu, Tongxin [1 ,2 ]
Astimar, Abdul Aziz [3 ]
Teh, Soek Sin [3 ]
Nursyairah, Jalil [3 ]
Liu, Dehua [1 ,2 ]
Zhao, Xuebing [1 ,2 ]
机构
[1] Tsinghua Univ, Key Lab Ind Biocatalysis, Minist Educ, Beijing 100084, Peoples R China
[2] Tsinghua Univ, Inst Appl Chem, Dept Chem Engn, Beijing 100084, Peoples R China
[3] Malaysian Palm Oil Board, Engn & Proc Div, 6 Persiaran Inst, Kajang 43000, Selangor, Malaysia
关键词
Oil palm biomass; Hydrolysis of hemicelluloses; Non -isothermal kinetic modeling; Dehydration of xylose; Enzymatic hydrolysis of cellulose; SULFURIC-ACID; SUGARCANE BAGASSE; KINETIC-MODEL; LIGNIN; JET; OPTIMIZATION; DIFFUSION; IMPACTS; DIESEL;
D O I
10.1016/j.biortech.2023.128626
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
A novel process for simultaneous production of furfural and pretreatment of oil palm empty fruit bunch (EFB) by dilute acid pre-hydrolysis was developed based on non-isothermal kinetic modeling. Mass transfer analysis suggested that the internal diffusion could be neglected as diffusion time of sulfuric acid in EFB particles was significantly shorter than the pre-hydrolysis period, whereas the heating stage could not be neglected due to a significant part of xylan was solubilized at the stage. A strategy for increasing furfural yield was developed by intermittent discharging of steam, resulting in 71.4 % furfural yield. The pretreated solids showed good enzy-matic digestibility. 136.3 g/L glucose corresponding to 81.6 % yield was obtained by high-solid loading hy-drolysis. 95.4 g furfural and 212 g glucose could be obtained from 1 kg dry EFB. Therefore, non-isothermal effects on polysaccharide hydrolysis and pentose decomposition should be considered carefully for an efficient process design of EFB biorefining.
引用
收藏
页数:10
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