Modelling, optimal solvent screening and separation of 5-hydroxymethylfurfural or furfural from catalytic conversion reactor stream in downstream purification process

被引:9
|
作者
Zilnik, Ljudmila Fele [1 ]
Crnomarkovic, Mladen [2 ]
Novak, Uros [1 ]
Grilc, Miha [1 ]
Likozar, Blaz [1 ]
机构
[1] Natl Inst Chem, Dept Catalysis & Chem React Engn, Hajdrihova 19, Ljubljana 1001, Slovenia
[2] Maturus Optimi Ind Consulting BV, Cornwallpl 23, Sittard, Netherlands
来源
关键词
5-Hydroxymethylfurfural; Furfural; Optimal Solvent Screening; Modelling; Simulation; Downstream Separation Process; LIQUID-LIQUID EQUILIBRIA; BINARY LLE MEASUREMENTS; PHASE-EQUILIBRIA; ACETIC-ACID; PARTITION-COEFFICIENTS; AQUEOUS-SOLUTIONS; LEVULINIC ACID; FORMIC-ACID; PLUS WATER; SYSTEMS;
D O I
10.1016/j.cherd.2023.04.062
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An overall process evaluation-based solvent selection for the biphasic catalytic conversion of the sugars into bio-based 5-hydroxymethylfurfural (5-HMF), furfural (FURF) and for the downstream separation and purification sequence was carried out, which represents an important step in industrial operating procedure. In the chemical process screening for 5-HMF extraction, the various dissolving fluids of different molecular polarity were used, parallel batch experiments were performed, and a few were identified as potential sub-stance solutions for either, 5-HMF or FURF. Criteria were based on the ability to form two liquid phases within an aqueous thermodynamic system, to have fast transport kinetics, and simultaneously extract the 5-HMF and/or FURF with a high partitioning coefficient. The feasibility of the constituents' pure mixture in terms of waste material efficiency, its resource recovery and the purity of both product species were also a part of the criteria. The best solute-partitioning alternatives found, besides an organic benchmark methyl isobutyl ketone (MIBK), were benzyl alcohol, tetrahydrofuran (THF) with an addition of sodium salt and homologues, resulting from the determined efficacy analysis, modelling and optimisation of the continuous purification methodology by means of partition, dis-tillation and thermal heat recuperation. This allows for designing a diluted carbohydrate stream integrated bio refining in the wake of pulping.(c) 2023 Institution of Chemical Engineers. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:376 / 387
页数:12
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