Esterification of Levulinic Acid to Ethyl Levulinate Using Liquefied Oil Palm Frond-Based Carbon Cryogel Catalyst

被引:0
作者
Muzakkir Mohammad Zainol
Nor Aishah Saidina Amin
Mohd Asmadi
Nur Aainaa Syahirah Ramli
机构
[1] Universiti Teknologi Malaysia,Chemical Reaction Engineering Group (CREG), School of Chemical and Energy Engineering, Faculty of Engineering
[2] Malaysian Palm Oil Board,Advanced Oleochemical Technology Division
来源
BioEnergy Research | 2019年 / 12卷
关键词
Oil palm frond; Biomass; Liquefaction; 1-Butyl-3-methylimidazole hydrogen sulfate; Carbon cryogel; Ethyl levulinate;
D O I
暂无
中图分类号
学科分类号
摘要
Oil palm biomass, which is abundantly available in Malaysia, has many types of applications in various industries. In this study, oil palm frond (OPF) was liquefied with 1-butyl-3-methylimidazole hydrogen sulfate ([BMIM][HSO4]) ionic liquid (IL) at optimum conditions. The liquefied OPF-ionic liquid (LOPF-IL) was mixed with furfural at a ratio of 0.8 (w/w), water-to-feedstock ratio of 0.125 (w/w), and sulfuric acid loading of 0.5 mL at 100 °C for 1 h to form a gel. Carbon cryogel liquefied oil palm frond (CCOPF) was prepared using a freeze-dryer followed by calcination. CCOPF was further characterized using N2 sorption, NH3-TPD, TGA, XRD, FTIR, and FESEM to determine its physical and chemical properties. The thermally stable CCOPF exhibited a large total surface area (578 m2/g) and high total acidity (17.6 mmol/g). Next, CCOPF was tested for levulinic acid catalytic esterification by varying the parameters including ethanol-to-levulinic acid molar ratio, catalyst loading, and reaction time at 78 °C. At the optimum conditions, the conversion of levulinic acid and ethyl levulinate yield was 70.9 and 71.7 mol%, respectively. CCOPF was reusable up to five runs with no significant conversion drop. Accordingly, CCOPF is conferred as a potential biomass-derived acid catalyst for ethyl levulinate production.
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页码:359 / 369
页数:10
相关论文
共 196 条
[1]  
Akhtar J(2010)Liquefaction of empty palm fruit bunch (EPFB) in alkaline hot compressed water Renew Energy 35 1220-1227
[2]  
Kuang SK(2010)Liquefaction of bio-mass in hot-compressed water for the production of phenolic compounds Bioresour Technol 101 2483-2490
[3]  
Amin NS(2017)Hydrothermal liquefaction of biomass: influence of temperature and biomass composition on the bio-oil production Fuel 208 618-625
[4]  
Tymchyshyn M(2018)Reactivity of solid residue from hydrothermal liquefaction of diatom in oxidizing atmosphere J Taiwan Inst Chem Eng 90 68-78
[5]  
Xu C(2009)Liquefaction of oil palm empty fruit bunch (EFB) into phenol and characterization of phenolated EFB resin Ind Crop Prod 30 54-58
[6]  
de Caprariis B(2014)Physico-mechanical properties of resol phenolic adhesives derived from liquefaction of oil palm empty fruit bunch fibres Ind Crop Prod 62 119-124
[7]  
De Filippis P(2006)Liquefaction of grapevine cane (Vitis vinisera L.) waste and its application to phenol–formaldehyde type adhesive Ind Crop Prod 24 171-176
[8]  
Petrullo A(2013)Optimization of lignin production from empty fruit bunch via liquefaction with ionic liquid Bioresour Technol 135 690-696
[9]  
Scarsella M(2015)Ionic liquids: not always innocent solvents for cellulose Green Chem 17 231-243
[10]  
Fushimi C(2017)Pretreatment of lignocellulosic biomass with ionic liquids and ionic liquid-based solvent systems Molecules 22 490-2499