Environment friendly process for biodiesel
A biodiesel and environmentally friendly technology, applied in the field of biodiesel, can solve the problems of unavailable diesel, inability to form continuous large-scale operations, and poor continuous output capacity, so as to avoid secondary oxidation and processing loss, and realize continuous large-scale production. Large-scale flow production and the effect of reducing pollution emissions
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Embodiment 1
[0020] 1. Preparation of raw materials: Heat palm fatty acid at 50-60°C and acid value of 195mgkoh / g, anhydrous methanol esterification agent and sulfuric acid catalyst with a mass concentration of more than 98%, according to the mass ratio of 83:15:2 in the Tubular static mixer mixing;
[0021] 2. Pre-esterification: Put the mixed material in the previous step into the reaction kettle, and carry out the esterification reaction for 30 minutes under the reaction conditions: temperature of 65°C, pressure of 3Mpa and stirring speed of 60 rpm, and the product after the reaction enters the liquid separation tank Separation is carried out to obtain the upper material;
[0022] 3. Refined esterification: the material obtained in the previous step is repeated in step 2 to obtain a material with an acid value of 3.4 mgkoh / g;
[0023] 4. Washing to remove sulfur and esterification: add methanol detergent with 10% mass of the material to the material obtained in the previous step, mix i...
Embodiment 2
[0029] 1. Raw material preparation: heat the cottonseed fatty acid with an acid value of 210mgkoh / g to 50-60°C, anhydrous methanol esterification agent and sulfuric acid catalyst with a mass concentration of 98% or more, according to the mass ratio of 84:15:1 in the Tubular static mixer mixing;
[0030] 2. Pre-esterification: Put the mixed material in the previous step into the reaction kettle, and carry out the esterification reaction for 30 minutes under the reaction conditions: temperature of 65°C, pressure of 3Mpa and stirring speed of 60 rpm, and the product after the reaction enters the liquid separation tank Separation is carried out to obtain the upper material;
[0031] 3. Refined esterification: Repeat step 2 with the material obtained in the previous step to obtain a material with an acid value of 4.5 mgkoh / g;
[0032] 4. Washing to remove sulfur and esterification: add methanol detergent with 10% of the mass of the material in the upward step to obtain the materia...
Embodiment 3
[0038] 1. Raw material preparation: Soybean fatty acid heated to 50-60°C and acid value 203mgkoh / g, anhydrous methanol esterification agent and sulfuric acid catalyst with a mass concentration of more than 98% are mixed according to the mass ratio of 83.5:15:1.5 Tubular static mixer mixing;
[0039] 2. Pre-esterification: Put the mixed material in the previous step into the reaction kettle, and carry out the esterification reaction for 30 minutes under the reaction conditions: temperature of 65°C, pressure of 3Mpa and stirring speed of 60 rpm, and the product after the reaction enters the liquid separation tank Separation is carried out to obtain the upper material;
[0040] 3. Refined esterification: Repeat step 2 with the material obtained in the previous step to obtain a material with an acid value of 5.1 mgkoh / g;
[0041] 4. Washing to remove sulfur and esterification: add methanol detergent with 10% of the mass of the material in the upward step to obtain the material, m...
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