2011
DOI: 10.1016/j.fuel.2011.05.020
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Rubber seed oil as a potential source for biodiesel production in Bangladesh

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Cited by 166 publications
(80 citation statements)
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References 17 publications
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“…Flash Point ˚C 120 73 [13] 130 [15] Saponification Number -188 185.7 [14] 192 [16] Acid Value mgKOH/g oil 0.452 0.738 [13] 0.118 [15] Iodine Value g Iodine/100 g 102 99 [13] 132 [16] Calorific Value MJ/kg 37 38.72 [13] 36.50 [15] Moisture Content % 0.007 0.004 [13] 0.08 [16] Pour Point ˚C −14 −10 [13] −8 [15] mode with Arrhenius activation energy was about 23.93 kJmol However, this experimental work produced biodiesel which has lower pour point than that of both JC-Bio and HB-Bio.…”
Section: Resultsmentioning
confidence: 99%
“…Flash Point ˚C 120 73 [13] 130 [15] Saponification Number -188 185.7 [14] 192 [16] Acid Value mgKOH/g oil 0.452 0.738 [13] 0.118 [15] Iodine Value g Iodine/100 g 102 99 [13] 132 [16] Calorific Value MJ/kg 37 38.72 [13] 36.50 [15] Moisture Content % 0.007 0.004 [13] 0.08 [16] Pour Point ˚C −14 −10 [13] −8 [15] mode with Arrhenius activation energy was about 23.93 kJmol However, this experimental work produced biodiesel which has lower pour point than that of both JC-Bio and HB-Bio.…”
Section: Resultsmentioning
confidence: 99%
“…Required amount of raw oil was reacted with different stoichiometric amounts of alcoholic sodium hydroxide solution [16]. Take certain amount of oil in a three-necked flask and mix different stoichiometric amount of alcoholic sodium hydroxide solution.…”
Section: Three-step Methodmentioning
confidence: 99%
“…The mixture was heated under reflux with vigorous stirring at temperature of 65 0 C for different time. After saponification, the soap solution was treated with concentrated hydrochloric acid at a temperature of 60 -70 0 C with vigorous stirring [16]. After dissolving the soap the fatty acid contents were separated in separatory funnel.…”
Section: Three-step Methodmentioning
confidence: 99%
“…To reduce FFA, different pretreatment methods were applied previously. Among them steam distillation, utilization of solid base catalyst, extraction by alcohol and acid catalyst esterification were investigated (Morshed et al, 2011;Xu et al, 2007). Comparing different aforementioned pretreatment methods, acid catalyst esterification is preferable one.…”
Section: Introductionmentioning
confidence: 99%
“…Steam distillation is also not viable for high temperature operation. For the low solubility of FFA in alcohol, the alcohol extraction process is an expensive method (Morshed et al, 2011).…”
Section: Introductionmentioning
confidence: 99%