Efficient Production of 5-Hydroxymethylfurfural Enhanced by Liquid-Liquid Extraction in a Membrane Dispersion Microreactor

被引:31
|
作者
Zhou, Caijin [1 ]
Shen, Chun [2 ]
Ji, Kaiyue [2 ]
Yin, Jiabin [2 ]
Du, Le [1 ]
机构
[1] Beijing Univ Chem Technol, Beijing Key Lab Membrane Sci & Technol, State Key Lab Chem Resource Engn, 15 North Three Ring East Rd, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, Coll Life Sci & Technol, Natl Energy R&D Ctr Biorefinery, Beijing Key Lab Bioproc, 15 North Three Ring East Rd, Beijing 100029, Peoples R China
来源
关键词
5-Hydroxymethylfwfural production; Fructose dehydrogenation; Membrane dispersion microreactor; Extraction efficiency; BIPHASIC SYSTEM; CATALYTIC DEHYDRATION; PRESSURE CONDITIONS; HIGH-TEMPERATURE; SLUG FLOW; CONVERSION; FRUCTOSE; BIOMASS; DERIVATIVES; CHEMICALS;
D O I
10.1021/acssuschemeng.7b04368
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Aimed at efficient production of 5-hydroxymethylfurfural (HMF) in a green and sustainable way, dehydrogenation of fructose was enhanced by liquid liquid extraction in a membrane dispersion microreactor. On account of the high mass-transfer rate resulted from dripping flow, the obtained HMF was readily extracted from the aqueous phase to the organic phase, effectively preventing the sequence side reaction and leading to high HMF selectivity. Enhanced by efficient extraction, the reaction duration decreased from 60 min in a traditional stirred reactor to 4 min in the microreactor, leading to an increase in the space-time yield by 3 orders of magnitude. The effects of total volume flow rate, droplet size, and phase ratio relating to extraction efficiency and HMF yield were systematically investigated. The highest extraction efficiency of nearly 100% coupled with the HMF yield of 93.0% was achieved at the phase ratio of 2 with volume flow rate of 600 mL/h. Overall, this work not only delineates an efficient strategy for synthesizing HMF but also opens a new avenue for reaction systems with subsequent side reaction, which suffer selectivity of the intermediates due to the in-line separation bottleneck under conditions of limited mass transfer.
引用
收藏
页码:3992 / +
页数:15
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