Al2O3-supported alkali and alkali earth metal oxides for transesterification of palm kernel oil and coconut oil.

Abstract Transesterification of palm kernel oil (PKO) and coconut oil (CCO) with methanol was investigated under a heterogeneous catalysis system. Various Al 2 O 3 -supported alkali and alkali earth metal oxides prepared via an impregnation method were applied as solid catalysts. The supported alkali metal catalysts, LiNO 3 /Al 2 O 3 , NaNO 3 /Al 2 O 3 and KNO 3 /Al 2 O 3 , with active metal oxides formed at calcination temperatures of 450–550 °C, showed very high methyl ester (ME) content (>93%). XRF analysis suggests this is likely to be due to a homogeneous catalysis of dissoluted alkali oxides. On the other hand, Ca(NO 3 ) 2 /Al 2 O 3 calcined at 450 °C yielded the ME content as high as 94% with only a small loss of active oxides from the catalyst, whereas calcined Mg(NO 3 ) 2 /Al 2 O 3 catalyst possessed an inactive magnesium-aluminate phase, resulting in very low ME formation. At calcination temperatures of >650 °C, alkali metal- and alkali earth metal-aluminate compounds were formed. Whilst the water-soluble alkali metal aluminates formed over NaNO 3 /Al 2 O 3 and KNO 3 /Al 2 O 3 were catalytically active, the aluminate compounds on LiNO 3 /Al 2 O 3 and Ca(NO 3 ) 2 /Al 2 O 3 are less soluble, giving very low ME content. The suitable conditions for heterogeneously catalyzed transesterification of PKO and CCO over Ca(NO 3 ) 2 /Al 2 O 3 are the methanol/oil molar ratio of 65, temperature of 60 °C and reaction time of 3 h, with 10 and 15–20% (w/w) catalyst to oil ratio for PKO and CCO, respectively. Some important physical and fuel properties of the resultant biodiesel products meet the standards of diesel fuel and biodiesel issued by Department of Energy Business, Ministry of Energy, Thailand.

[1]  H. Hattori Heterogeneous Basic Catalysis , 1995 .

[2]  Dere A. Okiy,et al.  Recovery of oil via acid-catalyzed transesterification , 2003 .

[3]  Hak Joo Kim,et al.  TRANSESTERIFICATION OF VEGETABLE OIL TO BIODIESEL USING HETEROGENEOUS BASE CATALYST , 2004 .

[4]  J. F. González,et al.  Biodiesel Fuels from Vegetable Oils: Transesterification of Cynara cardunculus L. Oils with Ethanol , 2002 .

[5]  Wenlei Xie,et al.  Alumina-supported potassium iodide as a heterogeneous catalyst for biodiesel production from soybean oil , 2006 .

[6]  Wenlei Xie,et al.  Transesterification of soybean oil catalyzed by potassium loaded on alumina as a solid-base catalyst , 2006 .

[7]  H. Noureddini,et al.  Kinetics of transesterification of soybean oil , 1997 .

[8]  Ramón Moreno-Tost,et al.  Potassium leaching during triglyceride transesterification using K/γ-Al2O3 catalysts , 2007 .

[9]  T. Baba,et al.  Selective transesterification of triolein with methanol to methyl oleate and glycerol using alumina loaded with alkali metal salt as a solid-base catalyst , 2005 .

[10]  S. Gryglewicz Rapeseed oil methyl esters preparation using heterogeneous catalysts , 1999 .

[11]  R. Feuge,et al.  Modification of vegetable oils. VII. Alkali catalyzed interesterification of peanut oil with ethanol , 1949 .

[12]  Alberto Marinas,et al.  Magnesium-containing mixed oxides as basic catalysts: base characterization by carbon dioxide TPD–MS and test reactions , 2004 .

[13]  Sanjib Kumar Karmee,et al.  Preparation of biodiesel from crude oil of Pongamia pinnata. , 2005, Bioresource technology.

[14]  E. H. Pryde,et al.  Transesterification kinetics of soybean oil 1 , 1986 .

[15]  G. Knothe,et al.  Alternative Diesel Fuels from Vegetable Oils and Animal Fats , 2001 .

[16]  Kinya Kobayashi,et al.  Estimation of the Solubility Dependence of Aluminate Salts of Alkali Metals on Ion Radii of Alkali Metals by LDF Molecular Orbital Calculations , 1996 .

[17]  G. Busca,et al.  Surface basicity of mixed oxides: magnesium and zinc aluminates , 1991 .

[18]  Kanit Krisnangkura,et al.  Continuous transmethylation of palm oil in an organic solvent , 1992 .

[19]  G. Suppes,et al.  Calcium carbonate catalyzed alcoholysis of fats and oils , 2001 .

[20]  A. S. Ramadhas,et al.  Biodiesel production from high FFA rubber seed oil , 2005 .