Biodiesel preparation method
A biodiesel and oil technology, applied in the fields of biofuel, petroleum industry, liquid carbon-containing fuel, etc., can solve the problems of high equipment investment and energy consumption, high energy consumption, complex catalyst preparation process, etc., to achieve strong adaptability of raw materials, High purity and avoid the accumulation of saponification
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Embodiment 1
[0032] To produce biodiesel by reacting soybean oil with methanol, the process conditions, material input and output are as follows:
[0033] Methanol and soybean oil are fed into a tubular reactor for reaction, and the reaction conditions are: the molar ratio of alcohol to oil is 12:1, adding 2% ZnO / Ca(OH) of soybean oil quality 2 / KF, KF / MMT and Na 2 SiO 3 The mixture is a solid base, the volume space velocity of the reaction solution is 0.5 / h, the reaction temperature is 65°C, and the pressure is 5MPa. The reacted material was depressurized and flashed to remove methanol, then the temperature was lowered to 40°C, and glycerol was centrifuged. In the obtained methyl ester phase, the mass concentration of methyl ester reaches 89%, and the mass concentration of monoglyceride is 5%. Next, after mixing 4% of Span80 (sorbitan monooleate, hydrophilic-lipophilic balance value is about 4.3) in the methyl ester phase, under the transmembrane pressure difference of 0.15MPa, through...
Embodiment 2
[0035] Cottonseed oil with an acid value of 10mgKOH / g is reacted with methanol to produce biodiesel. The process conditions, material input and output are as follows:
[0036] Send methanol and cottonseed oil into a tubular reactor for reaction, the molar ratio of alcohol to oil is 15:1, KOH is 0.3‰ of the mass of soybean oil, and ZnO / Ca(OH) of 3% of the mass of soybean oil is added 2 / KF, KF / MMT and Na 2 SiO 3 The mixture is solid alkali, the volume space velocity of the reaction liquid is 4 / h, the temperature of the reactor is 75°C, and the pressure is 6MPa. After the reaction, the oil conversion rate is about 89%. The reacted material was decompressed and flashed to remove methanol, then the temperature was lowered to 50°C, and glycerin was separated by sedimentation. In the oil phase after separation of glycerin, the mass concentration of monoglycerides is 12%. Next, after mixing 1% Tween80 (polyoxyethylene sorbitan monostearate, hydrophilic-lipophilic balance value is...
Embodiment 3
[0038] Using palm oil to react with methanol to produce biodiesel, the process conditions, material input and output are as follows:
[0039]Methanol and palm oil are fed into a tubular reactor for reaction, the molar ratio of alcohol to oil is 9:1, NaOH is 0.1‰ of soybean oil quality, and ZnO / Ca(OH) of 4% soybean oil quality is added 2 / KF, KF / MMT and Na 2 SiO 3 The mixture is solid alkali, the volume space velocity of the reaction liquid is 1 / h, the temperature of the reactor is 55° C., and the pressure is 3 MPa. After the reaction, the oil conversion rate reaches 87%. The reacted material was depressurized and flashed to remove methanol, then the temperature was lowered to 30°C, and glycerin was separated by sedimentation. In the oil phase after separation of glycerin, the mass concentration of monoglycerides is about 13%. Next, after mixing 2% Pingjia O-25 (high-carbon aliphatic alcohol polyoxyethylene ether, hydrophilic-lipophilic balance value is about 17) in the met...
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