Method for preparing second-generation biodiesel from acid oil
A second-generation biodiesel and acidified oil technology, which is applied in the field of acidified oil to prepare second-generation biodiesel, can solve the problems of difficult large-scale industrialization and application, easy pulverization and deactivation of the catalyst bed, and large acid value, etc. The effect of large-scale industrialization promotion and application, stable and reliable production process, and high utilization rate of raw materials
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Embodiment 1
[0047] like figure 1 As shown, the present embodiment provides a method for preparing second-generation biodiesel from acidified oil, comprising the following steps:
[0048] S1. Pass the acidified oil raw material into the filter 1, filter and remove the solid impurities at a temperature of 100 ° C and an operating pressure of 1.0 MPa, then mix it with methanol and a liquid acid catalyst and pass it into the pre-esterification reactor 2, where the liquid acid catalyst Under the action of the pre-esterification reaction, a pre-esterification mixture is generated. Wherein, the molar ratio of methanol to acidified oil raw material is 1.25:1, the mass ratio of liquid acid catalyst to acidified oil raw material is 0.2:1, the operating temperature of pre-esterification reactor 2 is 90℃, the operating pressure is 0.12MPa, adding The liquid acid catalyst is concentrated sulfuric acid.
[0049] S2. Mix the pre-esterified mixture with water in a volume ratio of 1:1 and then pass it i...
Embodiment 2
[0055] like figure 1 As shown, the present embodiment provides a method for preparing second-generation biodiesel from acidified oil, comprising the following steps:
[0056] S1, pass the acidified oil raw material into the filter 1, filter and remove the solid impurities at a temperature of 150 ° C and an operating pressure of 2 MPa, then mix with isopropanol and p-toluenesulfonic acid and pass into the pre-esterification reactor 2, in the liquid The pre-esterification reaction is carried out under the action of an acid catalyst to generate a pre-esterified mixture. The molar ratio of isopropanol to acidified oil raw material is 1.1:1, the mass ratio of p-toluenesulfonic acid to acidified oil raw material is 0.5:1, the operating temperature of pre-esterification reactor 2 is 100°C, and the operating pressure is 0.1 MPa.
[0057] S2. Mix the pre-esterified mixture with water in a volume ratio of 0.8:1 and then pass it into the liquid-liquid separator 3, carry out liquid-liqu...
Embodiment 3
[0063] like figure 1 As shown, the present embodiment provides a method for preparing second-generation biodiesel from acidified oil, comprising the following steps:
[0064] S1. Pass the acidified oil raw material into the filter 1, filter and remove the solid impurities at a temperature of 80 ° C and an operating pressure of 0.5 MPa, then mix with ethanol and a liquid acid catalyst and pass it into the pre-esterification reactor 2, where the liquid acid catalyst Under the action of the pre-esterification reaction, a pre-esterification mixture is generated. Wherein, the molar ratio of ethanol to acidified oil raw material is 1.5:1, the mass ratio of liquid acid catalyst to acidified oil raw material is 1:1, the operating temperature of pre-esterification reactor 2 is 90 °C, the operating pressure is 0.15 MPa, adding The liquid acid catalyst is a low corrosive Bronsted acid ionic liquid.
[0065] S2. Mix the pre-esterified mixture with water in a volume ratio of 1.2:1 and th...
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