Method for producing biodiesel from grease raw material with high acid value
A high acid value oil, biodiesel technology, applied in the biofuel, fuel, petroleum industry and other directions, can solve the problems of air pollution, the limited reduction of the freezing point of biodiesel, the significance of reducing the clean energy of biodiesel, etc. Environmental pollution, beneficial effect of waste utilization
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Embodiment 1
[0034] Weigh 100g of oil raw material with an acid value of 40mgKOH / g, wherein the fatty acid content is 20g, weigh 13.15g of glycerin, and the molar ratio of glycerol to fatty acid is 2: 1; 8% of the mass; 100g of high acid value oil raw material, 13.15g of glycerin and 9.1g of ionic liquid catalyst were added in a 500ml reactor, and the vacuum reaction was carried out at 120°C and a pressure of 10.0KPa for 3 hours; after the reaction, the reaction temperature was lowered to Stand at room temperature and stratify, the upper layer is low acid value oil after esterification, the acid value after detection is 0.5mgKOH / g, and the yield is 103.6g; the lower layer is non-transglycerin and ionic liquid catalyst, which are recycled.
Embodiment 2
[0036]Weigh 100g of oil raw material with an acid value of 80mgKOH / g, wherein the fatty acid content is 40g, weigh 52.57g of glycerin, and the molar ratio of glycerol to fatty acid is 4: 1; 15% of the mass; 100g of high acid value oil raw material, 52.57g of glycerin and 22.89g of ionic liquid catalyst were added in a 500ml reactor, and the vacuum reaction was carried out at 130°C and a pressure of 100.0KPa for 3 hours; after the reaction, the reaction temperature was lowered to Stand at room temperature and stratify, the upper layer is low acid value oil after esterification, the acid value after detection is 0.3mgKOH / g, and the yield is 108.4g; the lower layer is non-transglycerin and ionic liquid catalyst, which are recycled.
Embodiment 3
[0038] Weigh 100g of oil raw material with an acid value of 160mgKOH / g, wherein the fatty acid content is 80g, weigh 157.72g of glycerin, and the molar ratio of glycerol to fatty acid is 6: 1; 30% of the mass; 100g of high acid value oil raw material, 157.72g of glycerin and 77.32g of ionic liquid catalyst were added in a 500ml reactor, and the vacuum reaction was carried out at 140°C and a pressure of 200.0KPa for 3 hours; after the reaction, the reaction temperature was lowered to Stand at room temperature and stratify, the upper layer is low acid value oil after esterification, the acid value after detection is 0.2mgKOH / g, and the yield is 116.3g; the lower layer is non-transglycerin and ionic liquid catalyst, which are recycled.
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