Liquid-liquid extraction of levulinic acid from aqueous solutions using hydrophobic tri-n-octylamine/alcohol-based deep eutectic solvent

被引:8
作者
Mai, Yinglin [1 ]
Xian, Xiaoling [1 ]
Hu, Lei [1 ]
Zhang, Xiaodong [1 ]
Zheng, Xiaojie [1 ]
Tao, Shunhui [1 ]
Lin, Xiaoqing [1 ,2 ,3 ]
机构
[1] Guangdong Univ Technol, Sch Chem Engn & Light Ind, Guangzhou 510006, Peoples R China
[2] Guangdong Univ Technol, Guangdong Prov Key Lab Plant Resources Biorefinery, Guangzhou 510006, Peoples R China
[3] Guangdong Univ Technol, Guangzhou Key Lab Clean Transportat Energy Chem, Guangzhou 510006, Peoples R China
来源
CHINESE JOURNAL OF CHEMICAL ENGINEERING | 2023年 / 54卷
基金
中国国家自然科学基金;
关键词
Extraction; Separation; Levulinic acid; Deep eutectic solvents; Hydrophobic; Aqueous solution; FIXED-BED COLUMN; REACTIVE EXTRACTION; FORMIC-ACID; SEPARATION; ADSORPTION; BUTANOL; OPTIMIZATION; EQUILIBRIUM; HYDROLYSATE; BIOBUTANOL;
D O I
10.1016/j.cjche.2022.10.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Levulinic acid (LA) is one of the top-12 most promising biomass-based platform chemicals, which has a wide range of applications in a variety of fields. However, separation and purification of LA from aqueous solution or actual hydrolysate continues to be a challenge. Among various downstream separation tech-nologies, liquid-liquid extraction is a low-cost, effective, and simple process to separate LA. The key breakthrough lies in the development of extractants with high extraction efficiency, good hydrophobicity, and low cost. In this work, three hydrophobic deep eutectic solvents (DESs) based on tri-n-octylamine (TOA) as hydrogen bond acceptor (HBA) and alcohols (butanol, 2-octanol, and menthol) as hydrogen bond donors (HBDs) were developed to extract LA from aqueous solution. The molar ratios of HBD and HBA, extraction temperature, contact time, solution pH, and initial LA concentration, DES/water volume ratios were systematically investigated. Compared with 2-octanol-TOA and menthol-TOA DES, the butanol- TOA DES exhibited the superior extraction performance for LA, with a maximum extraction efficiency of 95.79 +/- 1.4%. Moreover, the solution pH had a great impact on the LA extraction efficiency of buta-nol-TOA (molar ratio = 3:1). It is worth noting that the extraction equilibrium time was less than 0.5 h. More importantly, the butanol-TOA (3:1) DES possesses good extraction abilities for low, medium, and high concentrations of LA. (c) 2022 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
引用
收藏
页码:248 / 256
页数:9
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