Preparation method of iso-fatty acid methyl ester biodiesel
A technology of fatty acid methyl ester and biodiesel, which is applied in the preparation of carboxylate, the preparation of organic compounds, and biofuels, etc., can solve the problems of low temperature crystallization, unusable biodiesel, equipment corrosion, etc., and achieves atomic weight increase, excellent oxidation and The effect of hydrolytic stability
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Embodiment 1
[0023] (1) Preparation of catalyst
[0024] 1mol / L of BF 3 The solution was mixed with phosphotungstic acid at 65°C, BF 3 The molar ratio to phosphotungstic acid is 1:0.1. The mixed solution is loaded on Al2O3, wherein the carrier accounts for 90% by mass. Dry at 120°C for 12 hours, and bake at 450°C for 3 hours to prepare boron-phosphotungstic acid supported catalyst.
[0025] (2) Product synthesis
[0026] 10g cottonseed oil biodiesel and catalyzer are joined in the reactor, and catalyst consumption is 0.5g, feeds methane gas, unsaturated fatty acid methyl ester (methyl oleate, methyl linoleate and 16 carbenoic acid methyl ester) at a molar ratio of 40:1, at a pressure of 6 MPa, at a reaction temperature of 90°C, and for 2 hours to prepare heterogeneous cottonseed oil biodiesel. Using the above synthesis method, 10 g of cottonseed oil biodiesel was replaced with 10 g of soybean oil biodiesel and 10 g of rapeseed oil biodiesel, and other conditions remained unchanged, to...
Embodiment 2
[0030] (1) Preparation of catalyst
[0031] Mix 1mol / L phosphoric acid solution with phosphotungstic acid at 65°C, the molar ratio of phosphoric acid to phosphotungstic acid is 1:0.1. The mixed solution was loaded on diatomaceous earth, wherein the carrier accounted for 90% by mass. Dry at 120°C for 12 hours, and bake at 450°C for 3 hours to prepare the phosphoric acid-phosphotungstic acid supported catalyst.
[0032] (2) Product synthesis
[0033] 10g cottonseed oil biodiesel and catalyzer are joined in the reactor, and catalyst consumption is 0.5g, feeds propane gas, unsaturated fatty acid methyl ester (methyl oleate, methyl linoleate and 16 The molar ratio of methyl carbenoate) was 10:1, the pressure was 6MPa, the reaction temperature was 120°C, and the reaction was performed for 2 hours to obtain isomerized cottonseed oil biodiesel. Using the above synthesis method, 10 g of cottonseed oil biodiesel was replaced with 10 g of soybean oil biodiesel and 10 g of rapeseed oil...
Embodiment 3
[0037] (1) Preparation of catalyst
[0038] 1mol / L of BF 3 The solution is mixed with silicotungstic acid at 65°C, BF 3 The molar ratio to phosphotungstic acid is 1:0.1. The mixed solution was loaded onto silica, wherein the carrier accounted for 80% by mass. Dry at 120°C for 12 hours, and bake at 450°C for 3 hours to prepare boron-silicotungstic acid supported catalyst.
[0039] (2) Product synthesis
[0040] 10g cottonseed oil biodiesel and catalyzer are joined in the reactor, and catalyst consumption is 0.5g, feeds ethane gas, unsaturated fatty acid methyl ester (methyl oleate, linoleate and methyl oleate in methane and cottonseed oil biodiesel 16 decenoic acid methyl ester) with a molar ratio of 20:1, a pressure of 8 MPa, a reaction temperature of 120°C, and a reaction time of 2 hours to obtain isomerized cottonseed oil biodiesel. Using the above synthesis method, 10 g of cottonseed oil biodiesel was replaced with 10 g of soybean oil biodiesel and 10 g of rapeseed oil...
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