Production of biological diesel oil by high-acid value grease
A high acid value oil and biodiesel technology, applied in the preparation of biological raw materials, biofuels, liquid hydrocarbon mixtures, etc., can solve problems such as acid removal, and achieve the effects of improving yield, shortening reaction time, and speeding up production speed
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Embodiment 1
[0017] Weigh 100g of peanut oil leftovers (acid value of 150) and put it into the conical flask, add 40g of methanol and 2 grams of tin tetrachloride, and mix the above-mentioned various substances in the conical flask to carry out pre-esterification reaction; temperature of reaction is 60°C, and the reaction time is 2h. After the reaction was completed, the layers were left to stand for 20 min, and the catalyst and glycerol in the lower layer were removed by centrifugation. After the catalyst KOH was dissolved in methanol, it was added to the reaction kettle together with the remaining oil for esterification. The reaction temperature was 60 ° C, KOH accounted for 1.2% of the weight of the remaining oil, the mass ratio of alcohol to oil was 1:8, and the reaction time was 50 min. . After the reaction was completed, it was left to stand for stratification for 60 min. The upper layer was mainly fatty acid methyl ester and a small amount of methanol, and the lower layer was mainl...
Embodiment 2
[0019] Weigh 100g of waste oil (acid value of 90) and put it into the conical flask, add 50g of methanol and 3 grams of tin tetrachloride, and mix the above-mentioned various substances in the conical flask to carry out pre-esterification reaction; temperature of reaction is 60°C, the reaction time was 3h. After the reaction was completed, the layers were left to stand for 20 min, and the catalyst and glycerol in the lower layer were removed by centrifugation. After the catalyst KOH was dissolved in methanol, it was added to the reaction kettle together with the remaining oil for esterification. The reaction temperature was 60 ° C, KOH accounted for 1.2% of the weight of the remaining oil, the mass ratio of alcohol to oil was 1:8, and the reaction time was 50 min. . After the reaction was completed, it was left to stand for stratification for 60 min. The upper layer was mainly fatty acid methyl ester and a small amount of methanol, and the lower layer was mainly composed of g...
Embodiment 3
[0021] Weigh 200g of frying oil (acid value of 30) and put it into the conical flask, add 80g of methanol and 4 grams of tin tetrachloride, mix the above-mentioned various substances in the conical flask and carry out pre-esterification reaction; is 60°C, and the reaction time is 2h. After the reaction was completed, the layers were left to stand for 20 min, and the catalyst and glycerol in the lower layer were removed by centrifugation. After the catalyst KOH was dissolved in methanol, it was added to the reaction kettle together with the remaining oil for esterification. The reaction temperature was 60 ° C, KOH accounted for 1.2% of the weight of the remaining oil, the mass ratio of alcohol to oil was 1:8, and the reaction time was 50 min. . After the reaction was completed, it was left to stand for stratification for 60 min. The upper layer was mainly fatty acid methyl ester and a small amount of methanol, and the lower layer was mainly composed of glycerol, KOH, and a sma...
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