A circular economy approach to produce low-cost biodiesel using agro-industrial and packing wastes from Mexico: Valorization, homogeneous and heterogeneous reaction routes and product characterization

被引:0
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作者
Veitia-de-Armas, Liyane [1 ]
Reynel-Avila, Hilda E. [1 ,2 ]
Villalobos-Delgado, Felipe J. [1 ]
Duran-Valle, Carlos J. [3 ]
Adame-Pereira, Marta [3 ]
Bonilla-Petriciolet, Adrian [1 ]
机构
[1] Inst Tecnol Aguascalientes, Ave Adolfo Lopez Mateos 1801 Ote, Aguascalientes 20256, Mexico
[2] CONAHCYT Investigadoras Investigadores Mexico, Ciudad Mexico 03940, Mexico
[3] Univ Extremadura, IACYS, Badajoz 06006, Spain
关键词
Biodiesel; Catalyst synthesis; Tetra pak; Biomass waste; Lipid extraction; Recycling; BIFUNCTIONAL CATALYST; OXIDE CATALYST; ACROCOMIA-ACULEATA; COOKING OIL; TRANSESTERIFICATION; ESTERIFICATION; BIOCHAR; XPS;
D O I
10.1016/j.renene.2024.121684
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This manuscript describes a circular economy approach to produce low-cost biodiesel using Tetra Pak (TP) and Mexican biomass wastes. Lipids were extracted from non-edible biomass with hexane. Corozo seeds contained 53 wt% lipids, while remaining biomass had <5 wt%. Corozo seed oil was selected to produce biodiesel with both homogeneous and heterogeneous reaction systems. A heterogeneous catalyst was synthesized from TP and its performance was compared with KOH in homogeneous systems using corozo and soybean oils. The best reaction conditions were identified through the Signal/Noise ratio analysis. TP catalyst achieved biodiesel yields of 12.7-98.11 % (corozo) and 87.0-98.4 % (soybean), while KOH systems showed 7.2-96.3 % and 64.6-98.5 %, respectively. These reactive systems were endothermic and fit to pseudo-second order kinetic model. Activation energies for KOH-catalyzed systems were 86.89 (corozo) and 43.72 (soybean) kJ/mol, while TP-catalyzed systems showed 78.31 and 105.68 kJ/mol, respectively. TP catalyst reuse was tested, and the loss of catalytic activity was attributed to active sites poisoning. Biomass, catalysts, and reaction products were characterized (e.g., FTIR, ICP, XRD, EDX-SEM, WDXRF, XPS, basicity and nitrogen adsorption-desorption isotherms). The TP catalyst showed competitive performance with respect to KOH, contributing to a sustainable biodiesel production chain viable for commercial implementation in Mexico.
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页数:15
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