2010
DOI: 10.1016/j.biortech.2009.10.034
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Supercritical biodiesel production and power cogeneration: Technical and economic feasibilities

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Cited by 68 publications
(47 citation statements)
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“…The different configurations (flowsheets) are currently assessed by using commercial chemical process simulators and life cycle assessment (Glisic and Skala, 2009;Deshpande et al, 2010;Lee et al, 2011;Kiwjaroun et al, 2009). Lee et al (2011) evaluated three continuous biodiesel processes, including a conventional alkali-catalyzed process using both fresh and waste vegetable oil and a supercritical methanol process using waste vegetable oil as the raw material and reported that the alkali-catalyzed process using fresh vegetable oil had the lowest total capital investment, but the supercritical process was the most economically feasible overall, providing a lower manufacturing cost and higher net present value and a discounted cash flow rate of return.…”
Section: Innovative Technology In Biodiesel Production By Scmmentioning
confidence: 99%
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“…The different configurations (flowsheets) are currently assessed by using commercial chemical process simulators and life cycle assessment (Glisic and Skala, 2009;Deshpande et al, 2010;Lee et al, 2011;Kiwjaroun et al, 2009). Lee et al (2011) evaluated three continuous biodiesel processes, including a conventional alkali-catalyzed process using both fresh and waste vegetable oil and a supercritical methanol process using waste vegetable oil as the raw material and reported that the alkali-catalyzed process using fresh vegetable oil had the lowest total capital investment, but the supercritical process was the most economically feasible overall, providing a lower manufacturing cost and higher net present value and a discounted cash flow rate of return.…”
Section: Innovative Technology In Biodiesel Production By Scmmentioning
confidence: 99%
“…Lee et al (2011) evaluated three continuous biodiesel processes, including a conventional alkali-catalyzed process using both fresh and waste vegetable oil and a supercritical methanol process using waste vegetable oil as the raw material and reported that the alkali-catalyzed process using fresh vegetable oil had the lowest total capital investment, but the supercritical process was the most economically feasible overall, providing a lower manufacturing cost and higher net present value and a discounted cash flow rate of return. Deshpande et al (2010) reported an economic analysis of the proposed supercritical process and found that the biodiesel processing cost through the proposed technology could be half of that of the current conventional methods.…”
Section: Innovative Technology In Biodiesel Production By Scmmentioning
confidence: 99%
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“…Almost all the triglycerides, even from poor quality, can be converted into high quality biodiesel fuel, without significant pre-treatment (Deshpande et al, 2010). According to literature, the conversion yield of waste cooking oil into biodiesel has been reported to be around 80 -90%, depending on the quality of waste cooking oil, the process for refining, technology and practices used during transesterification (Papageorgiou, 2009).…”
Section: Waste Cooking Oilmentioning
confidence: 99%
“…In 2009, carbon dioxide was applied to supercritical transesterification with ethanol to reduce the operating conditions (Bertoldi et al, 2009). From 2007 to 2010, numerous additional studies, such as vapor-liquid equilibria of binary systems (Anitescu et al, 2008;Fang et al, 2008;Shimoyama et al, 2008;Shimoyama et al, 2009;Tang et al, 2006), phase behavior of the reaction mixture (Glišic & Skala, 2010;Hegel et al, 2008;Hegel et al, 2007), thermal stability of unsaturated fatty acids in supercritical methanol (Imahara et al, 2008) and process simulation and economic analysis (Busto et al, 2006;D'Ippolito et al, 2006;Deshpande et al, 2010;Diaz et al, 2009;van Kasteren & Nisworo, 2007) were reported, leading to a better understanding of the supercritical transesterification process.…”
Section: The Chronological Development Of Supercritical Transesterifimentioning
confidence: 99%