Extraction of Crude Rubber Oil from Rubber Seed and Production of Biodiesel

M. Hossain, Moniruzzaman, S. Sujan, Mosharof Hossain, Jamal
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引用次数: 2

Abstract

Biodiesel is a mono alkyl ester of long chain fatty acids derived from renewable feed stocks, such as vegetable oils or animal fats, for using in compression ignition engine. Studies were carried out to extract non-edible crude rubber oil from rubber seed and to produce potential biodiesel from it. Crude rubber oil was extracted by Soxhlet extraction process with n-hexane solvent and also mechanically extracted by using continuous screw expeller. Due to its high free fatty acid (3.89% FFA) content, the crude rubber oil was processed in two steps. The acid-catalyzed esterification and followed by the base catalyzed transesterification. The acid-catalyzed esterification reaction was carried out with concentrated H2SO4 acid and ethanol-to-oil ratio. The production of biodiesel involved the transesterification of treated rubber oil with ethanol in the presence of a base catalyst (KOH) to yield ethyl ester as a product and glycerine as a by-product. The first step reduces the FFA level from 3.89% to 1.1% in one hour at 50oC for 40% w/w ethanol-to-oil ratio with 1% w/w H2SO4. After the reaction the mixture was stagnated for an hour and ethanol-water upper layer was discarded. The second step convert the product into biodiesel and glycerol through transesterification using 30% w/w ethanol-to-oil and 0.8% w/w KOH to oil at 65oC. The maximum biodiesel yield achieved at rate of 89.36% within one hour and the glycerol concentration in the by-product (glycerol layer) obtained after duel step transesterification was found 18.82%.
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橡胶籽中粗橡胶油的提取及生物柴油的生产
生物柴油是从可再生原料(如植物油或动物脂肪)中提取的长链脂肪酸的单烷基酯,用于压燃发动机。研究了从橡胶种子中提取不可食用的橡胶粗油,并将其用于生产生物柴油。采用正己烷溶剂索氏萃取法提取粗橡胶油,并采用连续螺杆挤出机进行机械萃取。由于橡胶粗油游离脂肪酸含量较高(3.89% FFA),采用两步法加工。先是酸催化的酯化反应,然后是碱催化的酯交换反应。在浓硫酸和乙醇油比条件下进行了酸催化酯化反应。生物柴油的生产涉及处理过的橡胶油与乙醇在碱催化剂(KOH)存在下的酯交换反应,产物为乙酯,副产物为甘油。第一步是在50℃、乙醇油比40%、H2SO4 w/w为1%的条件下,在1小时内将FFA水平从3.89%降至1.1%。反应结束后,将混合物静置1小时,丢弃上层乙醇-水。第二步,在65℃的温度下,用30% w/w的乙醇制油和0.8% w/w的KOH制油,通过酯交换反应将产物转化为生物柴油和甘油。1 h内最大生物柴油收率为89.36%,双步酯交换副产物(甘油层)的甘油浓度为18.82%。
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