Method of producing biological diesel oil using molecular distillation technology
A molecular distillation and biodiesel technology, applied in hydrocarbon distillation, biological raw materials, biofuels, etc., can solve the problems of unsatisfactory product quality, low product purity, waste of water resources, etc., and save water treatment costs and technological processes. Simple, no waste water pollution effect
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Embodiment 1
[0021] Coconut oil and methanol are used for esterification reaction, the esterification reaction product is stratified at rest, and the upper layer (crude methyl ester) is taken into buffer tank 1, such as figure 2 As shown, it then enters the degassing column 2 with a degassing temperature of 60°C and a vacuum degree of 5000 Pa; after degassing, the product enters the first-stage molecular distillation column 3 to separate the remaining methanol from the esterification reaction at a temperature of 80°C and a vacuum degree of 1000Pa; finally enter the second-stage molecular distillation tower 4 to separate the methyl ester, the temperature is 180°C, the vacuum degree is 50Pa, and the remaining impurities are discharged.
Embodiment 2
[0023] Use tallow and ethanol to carry out the esterification reaction, the esterification reaction product is stratified at rest, and the upper layer (crude ethyl ester) is taken into the buffer tank 1, such as figure 2 As shown, it then enters the degassing column 2 for degassing at a temperature of 100°C and a vacuum of 1000 Pa; after degassing, the product enters the first-stage molecular distillation tower 3 to separate the remaining ethanol from the esterification reaction at a temperature of 150°C and a vacuum of 100Pa; finally enter the second-stage molecular distillation tower 4 to separate the ethyl ester, the temperature is 280°C, the vacuum degree is 1Pa, and the remaining impurities are discharged.
Embodiment 3
[0025] Rapeseed oil and methanol are used for the esterification reaction, the esterification reaction product is roughly separated by high-speed centrifugation, and the crude methyl ester is taken into the buffer tank 1, such as figure 2 As shown, it then enters the degassing column 2 and the degassing temperature is 80°C, and the vacuum degree is 3000 Pa; after degassing, the product enters the first-stage molecular distillation column 3 to separate the remaining methanol from the esterification reaction, the temperature is 110°C, and the vacuum degree is 500Pa; finally enter the second-stage molecular distillation tower 4 to separate the methyl ester, the temperature is 230°C, the vacuum degree is 25Pa, and the remaining impurities are discharged.
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