期刊
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
卷 61, 期 37, 页码 13877-13885出版社
AMER CHEMICAL SOC
DOI: 10.1021/acs.iecr.2c02934
关键词
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资金
- National Key R&D Program of China [2021YFC2101800]
- Zhejiang Science and Technology Plan Project [2022C01060]
- ZJU-Hengyi Global Innovation Research Center
This work presents experimental and kinetic modeling studies on fructose dehydration to 5-hydroxymethylfurfural (HMF) in the solution of mixed acetone and water, catalyzed by hydrochloric acid (HCl). A reaction scheme that added an intermediate was proposed. The established kinetic model considered various parameters and achieved a high yield under the optimized condition.
This work presents experimental and kinetic modeling studies on fructose dehydration to 5-hydroxymethylfurfural (HMF) in the solution of mixed acetone and water, catalyzed by hydrochloric acid (HCl). A reaction scheme that added an intermediate was proposed. A corresponding kinetic model that considered the parameters, including temperature (383-423 K), initial substrate concentration (10-100 g/L), and catalyst concentration (5-60 mmol/L), was established, and the influence of solvent ratio (3-19) was also studied. The maximum yield was 91% in the ideal plug flow reactor under the optimized condition (T = 383 K, C-F0 = 10 g/L, C-HCl = 10 mmol/L). The model can well support the delicate reactor design since an industrially accessible HMF production process was proposed in this work.
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