Vacuum pressure application in biodiesel production from refined bleached deodorized palm olein

Q1 Chemical Engineering
International Journal of Thermofluids Pub Date : 2026-03-01 Epub Date: 2026-01-26 DOI:10.1016/j.ijft.2026.101571
Rondang Tambun, Bode Haryanto, Juan Surya Manurung, Nicholas, Vikram Alexander, Anggara Dwita Burmana, Ulfatunnisa
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引用次数: 0

Abstract

Many developments in biodiesel production have been carried out to streamline costs and energy required. Studying biodiesel production at vacuum pressure aims to save energy by operating at lower temperatures than non-vacuum methods. This research aims to produce biodiesel from Refined Bleached Deodorized Palm Olein (RBDPO) under vacuum pressure conditions. In this research, RBDPO was methanolyzed using KOH as a catalyst. The process consists of several stages, namely making a methoxy solution, conducting the transesterification process, and purifying the methyl ester. This research is conducted using a sequential experimental design, following a one factor at a time approach. The first phase involves varying the operating pressure (650 mbar, 750 mbar, 850 mbar, and 950 mbar) while keeping the molar ratio of methanol to raw materials at 10:1, the reaction time at 60 min, the catalyst amount at 1%, and the reaction temperature at 50 °C. After identifying the highest conversion based on operating pressure, the second phase explores variations in the amount of catalyst (1%, 2%, 3%, and 4%). The third phase focuses on the molar ratio of methanol to raw materials (10:1, 12:1, 14:1, and 16:1). The fourth phase involves varying the reaction time (60, 70, 80, and 90 min). Finally, the reaction temperature is varied in the fifth phase (45 °C, 50 °C, 55 °C, and 60 °C). In this study, the highest biodiesel conversion obtained is 97.86% at a pressure of 750 mbar, reaction time of 60 min, catalyst amount of 1%, mole ratio of 14:1, and reaction temperature of 55 °C. The results of gas chromatography analysis show that C16 and C18 esters are the most common components in the raw materials and biodiesel produced. The results of the physical properties of biodiesel obtained are ester content of 97.53%, density (40 °C) of 879 kg/m3, kinematic viscosity (40 °C) of 3.920 cSt, flash point of 150 °C, and water content of 0 mg/kg, which meet ASTM D-6751, EN 14214, and Indonesian National Standard 7182:2015. This study demonstrates that applying vacuum conditions during transesterification not only enhances biodiesel conversion but has lower process energy.
真空压力在精制漂白脱臭棕榈油生产生物柴油中的应用
生物柴油生产的许多发展已经进行,以简化成本和能源需求。研究在真空压力下生产生物柴油的目的是通过在比非真空方法更低的温度下操作来节省能源。本研究以精制漂白脱臭棕榈油(RBDPO)为原料,在真空条件下制备生物柴油。本研究以KOH为催化剂对RBDPO进行甲醇分解。该工艺包括制备甲氧基溶液、进行酯交换过程和纯化甲酯几个阶段。本研究采用顺序实验设计,遵循一次一个因素的方法。第一阶段包括改变操作压力(650 mbar, 750 mbar, 850 mbar和950 mbar),同时保持甲醇与原料的摩尔比为10:1,反应时间为60 min,催化剂用量为1%,反应温度为50℃。在确定了基于操作压力的最高转化率之后,第二阶段探索催化剂用量的变化(1%、2%、3%和4%)。第三阶段的重点是甲醇与原料的摩尔比(10:1,12:1,14:1和16:1)。第四阶段包括改变反应时间(60、70、80和90分钟)。最后,反应温度在第五相(45°C, 50°C, 55°C, 60°C)变化。在本研究中,在压力750 mbar,反应时间60 min,催化剂用量1%,摩尔比14:1,反应温度55℃的条件下,生物柴油的最高转化率为97.86%。气相色谱分析结果表明,C16和C18酯是原料和生产的生物柴油中最常见的成分。所得生物柴油的物理性能为酯含量为97.53%,密度(40℃)为879 kg/m3,运动粘度(40℃)为3.920 cSt,闪点为150℃,含水量为0 mg/kg,符合ASTM D-6751, EN 14214和印度尼西亚国家标准7182:2015。本研究表明,在酯交换过程中采用真空条件不仅提高了生物柴油的转化率,而且降低了过程能量。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
International Journal of Thermofluids
International Journal of Thermofluids Engineering-Mechanical Engineering
CiteScore
10.10
自引率
0.00%
发文量
111
审稿时长
66 days
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