Central Composite Design of Biodiesel Production from Waste Cooking Oil using Tympanotonus fuscatus (Periwinkle) Shells as Catalyst

Ubani O. Amune, Shegun K. Otoikhian
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Abstract

Biodiesel has been generally accepted as an environmentally – safer alternative to fossil based fuels. However, concerns of the cost of production, use of acid catalysts leading to corrosion, and recovery of homogenous catalyst remain. This study therefore seeks to optimize the transesterification process parameters in the conversion of waste cooking oil (WCO) using waste Tympanotonus fuscatus shell (WTFS). The catalysts were characterized using XRD, FTIR, and XRF. Temperatures ranging from 30°C to 90°C, catalyst loading from 1 to 10% by weight, and reaction durations from 30 to 180 minutes were examined for the transesterification technique. The physiochemical properties of the waste cooking oil revealed a high acid value (10.02mgKOH/g), kinematic viscosity of 13.30 mm2/s, pour point, 156oC, flash point of 104oC, Calorific value of 34.78 MJ/kg, carbon content of 2.65% m/m, among other parameters while the GCMS analysis indicated the presence of C16 to C21. The biodiesel however showed an acid value of 0.416 mgKOH/g, viscosity of 4.638 mm2/s, pour point of 0.3oC, flash point of 104oC, calorific value of 40.17 MJ/kg, and carbon content of 0.019% m/m which were in agreement with the EU and American standards. The elemental composition and crystalline structure of the catalyst revealed a considerable concentration of CaO, MgO, Al2O3, SiO2, and other metal oxides. The CCD approach used to design the experiments was significant (p <0.0001) and the biodiesel synthesis which resulted in a maximum yield of 91.70% was obtained with 5.5% WFTS, 105 minutes of reaction time, 65 oC, and a 1:7 oil–Methanol ratio. The operating parameters of temperature (p <0.0001), catalyst load (p = 0.00713), and time (p = 0.0288) all had significant effects on biodiesel yield; however, temperature had a stronger influence than the other process variables. The ANOVA results showed that the factors were extremely significant while Fit statistics and model comparison revealed a coefficient of determination of 97.66%, with the predicted value of 84.68% and the adjusted value of 95.00%. The biodiesel produced met the biodiesel standards.
以长春花壳为催化剂从废食用油生产生物柴油的中心复合设计
生物柴油已被普遍认为是一种对环境更安全的化石燃料替代品。然而,生产成本、酸性催化剂的使用导致腐蚀以及均相催化剂的回收等问题仍然存在。因此,本研究旨在优化利用褐鼓黄废壳(WTFS)转化废食用油(WCO)的酯交换工艺参数。采用XRD、FTIR和XRF对催化剂进行了表征。温度范围为30°C至90°C,催化剂负载为重量的1%至10%,反应持续时间为30至180分钟。废油的理化性质为高酸值(10.02mgKOH/g),运动粘度为13.30 mm2/s,倾点为156℃,闪点为104℃,发热量为34.78 MJ/kg,碳含量为2.65% m/m, GCMS分析表明存在C16 ~ C21。该生物柴油的酸值为0.416 mgKOH/g,粘度为4.638 mm2/s,倾点为0.3oC,闪点为104oC,发热量为40.17 MJ/kg,含碳量为0.019% m/m,符合欧美标准。催化剂的元素组成和晶体结构表明,催化剂中含有大量的CaO、MgO、Al2O3、SiO2等金属氧化物。采用CCD方法设计实验具有显著性(p <0.0001),在wft为5.5%、反应时间为105 min、温度为65℃、油-甲醇比为1:7的条件下,生物柴油的最大产率为91.70%。温度(p <0.0001)、催化剂负载(p = 0.00713)和时间(p = 0.0288)对生物柴油产率均有显著影响;然而,温度的影响比其他工艺变量更大。方差分析结果显示各因素极显著,拟合统计和模型比较的决定系数为97.66%,预测值为84.68%,调整值为95.00%。生产的生物柴油符合生物柴油标准。
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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