Bioprocess development for levulinic acid production using sugarcane biomass

被引:6
|
作者
dos Santos, Miqueias Gomes [1 ]
Fogarin, Henrique Maziero [1 ]
da Silva, Debora Danielle Virginio [2 ]
Dussan, Kelly Johana [1 ,3 ,4 ]
机构
[1] Sao Paulo State Univ, Inst Chem, Dept Engn Phys & Math, BR-14801309 Araraquara, SP, Brazil
[2] Sao Paulo State Univ UNESP, Inst Chem, Dept Biochem & Organ Chem, Araraquara, SP, Brazil
[3] Sao Paulo State Univ Unesp, Bioenergy Res Inst IPBEN, Araraquara, SP, Brazil
[4] Inst Chem UNESP, Ctr Monitoring & Res Qual Fuels, Biofuels Crude Oil & Derivat CEMPEQC, Araraquara, SP, Brazil
来源
关键词
Lignin-based catalyst; Levulinic acid; Straw; sugarcane bagasse; Sulfonated catalyst; LIGNIN PRECIPITATION; CATALYTIC CONVERSION; CELLULOSE; GLUCOSE; HYDROLYSIS; STRAW; ESTERIFICATION; CARBONS;
D O I
10.1016/j.scp.2023.101085
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Developing technologies for converting lignocellulosic biomass to products such as energy, fuels, and value-added chemicals is an important step in making biorefineries a feasible alternative to the current oil-based productive system. In this study, the conversion of lignocellulosic biomass composed of a mixture of bagasse and sugarcane straw into a cellulose pulp and a sulfonated car-bonaceous solid catalyst synthesized from lignin fraction were investigated, as well as the use of this solid acid catalyst to convert cellulose to levulinic acid, an important chemical platform. To overcome this challenge, firstly, the fractionation of lignocellulosic biomass was optimized. Then, tests were carried out to find the best condition for isolation of the soluble lignin from black liquor produced in the optimal condition of delignification. The lignin precipitate was subjected to carbonization tests followed by functionalization tests with concentrated sulfuric acid to syn-thesize the catalyst. This catalyst was then used to convert cellulose into levulinic acid (LA). The experimental design for cellulose recovery and lignin removal showed that under relatively mild reaction conditions of 110 degrees C, 117 min, and a solid/NaOH (4.4% w/v) ratio of 1:20, more than 91% of the lignin was dissolved into the black liquor, recovering a solid with a cellulose content higher than 78%. Lignin was fully recovered in the form of precipitate by simply reducing the pH of the black liquor to 3 (under this condition 11 g of precipitate were recovered per liter of liquor). Having the recovered lignin, it was then possible to synthesize a solid carbonaceous cata-lyst with a total acid site density of 1.48 mmol/g which was able to convert up to 17.11% of the cellulose and obtain yields of up to 38.55% of levulinic acid when a catalyst/cellulose ratio of only 8:10 (w/w) was used. Overall, the future of LA production using carbonaceous acid catalysts looks promising. As research in this area continues, there is the potential to further improve the production process and make it more cost-effective and sustainable. This could lead to wider adoption of this technology and increased use of levulinic acid in various industrial applications, including as a platform chemical to produce a range of chemicals and materials.
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页数:16
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