Heterogeneous catalysts for transesterification of triglycerides and preparation methods of same
a technology of heterogeneous catalysts and triglycerides, which is applied in the direction of physical/chemical process catalysts, metal/metal-oxide/metal-hydroxide catalysts, etc., can solve the problems of increasing the price of final products, reducing the production of ester, and introducing problems in the transesterification process using homogeneous catalysts, etc., to achieve attractive production, reduce the industrial cost of production, and improve the effect of quality
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example 1
[0019]Experiment performed in a reactor in batches, with sampling of 2 in 2 hours.
Conditions of the experiment: 100 grams of canola oil; 50 grams of methanol (molar ratio of oil / alcohol, 1 / 15); 1 g of apatite catalyst.
Reaction conditions: 175° C. / 8 hr in a single stage and at self-generated pressure.
Conversion of 95.06% of oil, 88.10% in methyl esters and 2.90% in mono- and diglycerides.
Reference: Conversion of 45.43% of oil, 37.93% in methyl esters and 7.5% in mono- and diglycerides.
example 2
[0020]Experiment performed in a reactor in batches, with sampling of 2 in 2 hours.
Conditions of the experiment: 100 grams of canola oil; 100 grams of methanol (molar ratio of oil / alcohol, 1 / 30); 1 g of apatite catalyst.
Reaction conditions: 175° C. / 8 hr in a single stage and at self-generated pressure.
Conversion of 98.00% of oil, 95.10% in methyl esters and 2.90% in mono- and diglycerides.
example 3
[0021]Experiment performed in a reactor in batches, with sampling of 2 in 2 hours.
Conditions of the experiment: 100 grams of soy oil; 100 grams of methanol (molar ratio of oil / alcohol, 1 / 30); 1 g of apatite catalyst.
Reaction conditions: 175° C. / 8 hr in a single stage and at self-generated pressure.
Conversion of 100% of oil, 98.03% in methyl esters and 1.97% in mono- and diglycerides.
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