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蓖麻籽油一锅法酯交换制备生物柴油的工艺优化及技术经济评估

Process optimization and technoeconomic assessment of biodiesel production by one-pot transesterification of Ricinus communis seed oil.

作者信息

Sangeetha Baskaran, Mohana Priya Srinivasan, Pravin Ravichandran, Tamilarasan Krishnamurthi, Baskar Gurunathan

机构信息

Department of Biotechnology, St. Joseph's College of Engineering, Chennai 600119, India.

Department of Chemical Engineering, SRM Institute of Science and Technology, Chennai 603203, India.

出版信息

Bioresour Technol. 2023 May;376:128880. doi: 10.1016/j.biortech.2023.128880. Epub 2023 Mar 13.

Abstract

In the present study, Ricinus communis seed oil with high free fatty acid content was utilized for the one-pot biodiesel production using 1-(2,3-dihydroxy)-propyl-3-methylimidazolium hydroxide, a basic ionic liquid catalyst. The 97.83% biodiesel yield was obtained at the optimized conditions of 6.26 % (w/w) of catalyst concentration, 10.51:1 M ratio of methanol to oil, 57.87 °C temperature and reaction time of 61.01 min. The transesterification of Ricinus communis seed oil to biodiesel exhibited an activation energy of 37.60 kJ/mol. The technoeconomic analysis, the profitability and the sensitivity analysis were investigated for the simulated process design. The technoeconomic analysis reported a total revenue of 20,455,431 $/yr, with gross margins, ROI, payback period, IRR, and NPV of 23.54%, 35.72%, 2.8 years, 28.20%, and 19,287,000 $, respectively. According to the sensitivity analysis, the two most important factors determining the economic viability of the simulated process are Ricinus communis seed oil cost and biodiesel selling price.

摘要

在本研究中,使用碱性离子液体催化剂1-(2,3-二羟基)丙基-3-甲基咪唑氢氧化合物,将游离脂肪酸含量高的蓖麻籽油用于一锅法生物柴油生产。在催化剂浓度为6.26%(w/w)、甲醇与油的摩尔比为10.51:1、温度为57.87°C和反应时间为61.01分钟的优化条件下,生物柴油产率达到97.83%。蓖麻籽油向生物柴油的酯交换反应表现出37.60kJ/mol的活化能。针对模拟工艺设计进行了技术经济分析、盈利能力分析和敏感性分析。技术经济分析报告称,年总收入为20,455,431美元,毛利率、投资回报率、回收期、内部收益率和净现值分别为23.54%、35.72%、2.8年、28.20%和19,287,000美元。根据敏感性分析,决定模拟工艺经济可行性的两个最重要因素是蓖麻籽油成本和生物柴油销售价格。

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