2014
DOI: 10.4236/wjet.2014.23020
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Preparation of KOH/CaO/C Supported Biodiesel Catalyst and Application Process

Abstract: KOH/CaO/C supported catalyst was prepared via incipient wetness impregnation and used in synthesis of biodiesel. First, the effects of carrier/active components mass ratio, calcination temperature and calcination time on catalytic activity were investigated aiming at biodiesel yield, and the optimal process conditions for preparation of KOH/CaO/C catalysts were: mass ratio of C/CaO was 4:6; KOH solution (mass concentration) was 25%; impregnation time was 24 h; drying temperature was 105˚C and time was 4 h; cal… Show more

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Cited by 17 publications
(10 citation statements)
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“…44 However, there was a declining trend in the catalytic activity after 5 h of reaction time since the longer the reaction time, the higher the amount of products that would be absorbed by the catalyst, thus yielding more by-products. 45,46 More importantly, this study endured a shorter reaction time for the reaction to be completed than that reported by Nakatani et al The authors reported less than 80% of biodiesel yield only after 5 h of reaction. 42…”
Section: Effects Of Reaction Timementioning
confidence: 59%
See 1 more Smart Citation
“…44 However, there was a declining trend in the catalytic activity after 5 h of reaction time since the longer the reaction time, the higher the amount of products that would be absorbed by the catalyst, thus yielding more by-products. 45,46 More importantly, this study endured a shorter reaction time for the reaction to be completed than that reported by Nakatani et al The authors reported less than 80% of biodiesel yield only after 5 h of reaction. 42…”
Section: Effects Of Reaction Timementioning
confidence: 59%
“…Journal of Physical Science, Vol. 31(1),[37][38][39][40][41][42][43][44][45][46][47][48][49][50][51][52][53][54][55] 2020 …”
unclassified
“…For CaO catalyst, the reaction reached its optimum value (62.07 ± 4.30%) after 4 h of reaction time (Supplementary material Figure S5b). The reaction rate dropped drastically when reaction time was increased to 6 h since more by-products and soap were produced due the extended reaction time (Eevera et al 2009;Freedman et al 1984;Leung & Guo 2006;Zhang & Meng 2014). Meanwhile, other studies by Birla et al (2012) and Boro et al (2011) required 8 h and 6 h of reaction time in order to obtain the complete reaction, which is a much longer than the time needed in this study.…”
Section: X-ray Diffraction Analysismentioning
confidence: 78%
“…Ali et al, [41] obtained 84% biodiesel yield from transesterification of waste cooking oil using calcined goat bones as catalysts. One major problem associated with the use of heterogeneous catalyst is its low surface area, but this can usually be increased by supporting it with compounds such as activated carbon or nanotubes or impregnating it with base solution [31,32,42,43] However, activated carbon is preferred as heterogeneous catalyst supporter because of its large surface area and its ease of separation from the product [42,44]. Hadiyanto et al, [32] obtained a 95% biodiesel yield using heterogeneous synthesized from green mussel shells calcined at 900 o C for 3hrs supported with activated carbon and impregnated in concentrated sodium hydroxide.…”
Section: Introductionmentioning
confidence: 99%