从辣木树叶灰烬中提取的基础催化剂在低级巴厘岛马拉帕里油生物柴油转化中的高性能表现

IF 1.7 4区 化学 Q4 CHEMISTRY, PHYSICAL Reaction Kinetics, Mechanisms and Catalysis Pub Date : 2024-04-30 DOI:10.1007/s11144-024-02637-7
Triyono, Wega Trisunaryanti, Serisya Inier Aksanti, Jason Purbonegoro
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摘要

这项研究的目的是从辣木树叶的灰烬中开发出一种具有高性能生物柴油生产的基础催化剂。将辣木树叶洗净、烘干,然后捣碎成粉末状灰烬。煅烧辣木树叶灰烬时使用了三种温度变化:700 °C (MA-700)、800 °C (MA-800) 和 900 °C (MA-900)。低级巴厘岛马拉帕里油(LMO)通过加热脱胶,然后用 85% 的 H3PO4 溶液处理,称为 DMO。DMO 油使用甲醇和浓 H2SO4 进行酯化(EDMO)。由于 MA-900 含有最高浓度的 CaO,因此被选为催化剂。在以下条件下使用 MA-900 生产生物柴油:反应温度(55、60 和 65 °C);油与甲醇的摩尔比(1:3、1:6 和 1:9);催化剂与油的重量比变量(3 wt%、6 wt% 和 9 wt%);以及反应时间(60、90、120 和 150 分钟)。利用傅立叶变换红外光谱和气相色谱-质谱对生物柴油产品进行了分析。催化剂可用性测试在最佳条件下进行了三次运行循环。在 60 °C 反应温度下,油:甲醇摩尔比为 1:6,催化剂/油重量比为 3%,反应持续 120 分钟,生物柴油产量最高,达到 87.2%,选择性为 100%。对 MA-900 催化剂进行的可用性测试表明,经过三个运行周期后,生物柴油的产量分别为 87.2%、86.4% 和 84.8%。
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High performance of a base catalyst from Moringa leaves ash for biodiesel conversion of low-grade Bali Malapari oil

This research was aimed at developing a base catalyst from the ash of moringa leaves that has high-performance biodiesel production. The moringa leaves were washed, dried, and then pounded into powder ash. Three temperature variations were used to calcinate the moringa leaves ash: 700 °C (MA-700), 800 °C (MA-800), and 900 °C (MA-900). Low-grade Bali Malapari oil (LMO) was degummed by heating and then treated with an 85% H3PO4 solution, which was referred to as DMO. The DMO oil was esterified using methanol and concentrated H2SO4 (EDMO). Because MA-900 contained the highest concentration of CaO, it was chosen to serve as the catalyst. The MA-900 was used in the production of biodiesel under the following conditions: temperature of reaction (55, 60, and 65 °C); oil-to-methanol mole ratio (1:3, 1:6, and 1:9); catalyst-to-oil weight ratio variables (3 wt%, 6 wt%, and 9 wt%); and reaction times (60, 90, 120, and 150 min). The biodiesel products were analyzed using FTIR and GC–MS. The best-performing conditions were conducted for catalyst usability test for three-run cycles. The highest biodiesel yield was achieved using a 1:6 oil:methanol mole ratio and a 3% catalyst/oil weight ratio at 60 °C reaction temperature, which lasted for 120 min and resulted in a biodiesel yield of 87.2wt% with 100% selectivity. The usability test performed on the MA-900 catalyst resulted in a biodiesel yield that was 87.2%, 86.4%, and 84.8% after three-run cycles.

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来源期刊
CiteScore
3.30
自引率
5.60%
发文量
201
审稿时长
2.8 months
期刊介绍: Reaction Kinetics, Mechanisms and Catalysis is a medium for original contributions in the following fields: -kinetics of homogeneous reactions in gas, liquid and solid phase; -Homogeneous catalysis; -Heterogeneous catalysis; -Adsorption in heterogeneous catalysis; -Transport processes related to reaction kinetics and catalysis; -Preparation and study of catalysts; -Reactors and apparatus. Reaction Kinetics, Mechanisms and Catalysis was formerly published under the title Reaction Kinetics and Catalysis Letters.
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