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Utilization of waste coral for biodiesel production via transesterification of soybean oil.

机译:利用废珊瑚通过大豆油的酯交换反应生产生物柴油。

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In the present study, the waste coral was utilized as a source of calcium oxide for transesterification of soybean oil into biodiesel (methyl esters). Characterization results revealed that the main component of the waste coral is calcium carbonate which transformed into calcium oxide when calcined above 700 degrees C. The Box-Behnken design of experiment was carried out, and the results were analyzed using response surface methodology. Calcination temperature, methanol- soybean oil molar ratio and catalyst concentration were chosen as variables. The methyl ester content (wt%) was response which must be maximized. A second-order model was obtained to predict methyl ester content as a function of these variables. Each variable was placed in the three low, medium and high levels (calcination temperature of 700, 800 and 900 degrees C; catalyst concentration of 3, 6 and 9 wt%; methanol-to-oil ratios of 12:1, 18:1 and 24:1). The optimum conditions from the experiment were found that the calcination temperature of 900 degrees C, catalyst concentration of 6 wt% and methanol-to-oil ratio of 12:1. Under these conditions, methyl ester content reached to 100 wt%. The waste catalyst was capable of being reused up to 4 times without much loss in the activity.
机译:在本研究中,废弃的珊瑚被用作氧化钙的来源,用于将大豆油酯交换生成生物柴油(甲酯)。表征结果表明,废珊瑚的主要成分是碳酸钙,当在700摄氏度以上煅烧时会转化为氧化钙。进行了Box-Behnken实验设计,并使用响应面方法对结果进行了分析。选择煅烧温度,甲醇-豆油摩尔比和催化剂浓度作为变量。甲酯含量(wt%)是必须最大化的响应。获得了用于预测作为这些变量的函数的甲酯含量的二阶模型。将每个变量分为三个低,中和高水平(煅烧温度为700、800和900摄氏度;催化剂浓度为3、6和9重量%;甲醇与油的比例为12:1、18:1和24:1)。实验的最佳条件是,煅烧温度为900℃,催化剂浓度为6 wt%,甲醇与油的比例为12:1。在这些条件下,甲酯含量达到100重量%。废催化剂可以重复使用多达4次,而不会损失很多活性。

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