2010
DOI: 10.1016/j.supflu.2010.04.001
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Investigations on supercritical transesterification of chicken fat for biodiesel production from low-cost lipid feedstocks

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Cited by 157 publications
(78 citation statements)
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“…The alcohol to oil molar ratio can be reduced to 12:1 and 18:1 for the supercritical methanol (SCM) and supercritical ethanol (SCE) processes at 400°C and 15MPa, respectively. As proposed in some studies (Marulanda et al, 2010;Marulanda et al, 2009), the increase of the operating temperature to 350 °C-400 °C dramatically reduced the molar ratios from 40:1-42:1 to 6:1-12:1 at moderate pressures of 10.0-15.0 MPa. Moreover, this process also resulted in important advantages, most importantly an increase of approximately 5%-10% in fuel yields and a reduction in the alcohol to oil molar ratio.…”
Section: Introductionmentioning
confidence: 69%
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“…The alcohol to oil molar ratio can be reduced to 12:1 and 18:1 for the supercritical methanol (SCM) and supercritical ethanol (SCE) processes at 400°C and 15MPa, respectively. As proposed in some studies (Marulanda et al, 2010;Marulanda et al, 2009), the increase of the operating temperature to 350 °C-400 °C dramatically reduced the molar ratios from 40:1-42:1 to 6:1-12:1 at moderate pressures of 10.0-15.0 MPa. Moreover, this process also resulted in important advantages, most importantly an increase of approximately 5%-10% in fuel yields and a reduction in the alcohol to oil molar ratio.…”
Section: Introductionmentioning
confidence: 69%
“…In this study, the mass balance of the overall theoretical reactions was calculated based on the simple reactions involved in the process, following Marulanda et al(2010). The transesterification reaction of a stoichiometric mixture of triglyceride (TG) and ethanol produces FAEEs and glycerol, as shown in Equation 2.…”
Section: Mass Balancementioning
confidence: 99%
“…Although a distillation tower is the simplest separation unit for handling the glycerol-water stream, it consumes a large amount of energy to operate. The high-temperature process involves increasing the operating temperature to 400 to 450 °C (Marulanda et al, 2009;Marulanda et al, 2010), so that the operating pressure, methanol to oil molar ratio and reaction time for complete conversion are reduced to 10.0 MPa, 6:1 and 4 min, respectively. As expected, the unsaturated fatty acids are partially consumed by thermal degradation but the oxidation resistance or storage stability of the product might be enhanced.…”
Section: The Process Modificationsmentioning
confidence: 99%
“…Since the high-temperature approach, as recently initiated, has evaluated the triglycerides found in soybean oil (Anitescu et al, 2008) and chicken fat (Marulanda et al, 2009;Marulanda et al, 2010) only, then additional research into other triglycerides are needed. In addition, studies on the economical feasibility and environmental impact are also required.…”
Section: The High-temperature Approachmentioning
confidence: 99%
“…The supercritical methanol method is simpler, more environmentally friendly and can reach high conversion (>95%) in a very short time. The presence of high contents of FFAs and water has no effect on the efficiency of this method [17][18][19][20]. In this reaction, a single homogenous phase is formed between methanol and oil.…”
Section: Introductionmentioning
confidence: 99%