Production process of biological diesel oil
A production method, biodiesel technology, applied to the preparation of biological raw materials, biofuels, liquid hydrocarbon mixtures, etc., can solve the problems of low reaction rate, poor mutual solubility, etc., achieve simplified process flow, high conversion rate, and avoid catalyst separation Effect
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[0027] Example 1
[0028] Add cottonseed oil to storage tank E, and add methanol to storage tank F. The molar ratio of methanol to cottonseed oil is 10, and the feed rate of cottonseed oil and methanol is equal to the impinging stream reaction volume (that is, the feed volume space velocity is 1h- 1. The reaction time is 1h). Pump cottonseed oil and methanol into the intermediate tank C respectively, pre-mix with the circulating materials in the intermediate tank, and then pump into the impinging stream reactor, and transesterification occurs through the impingement. For the reaction, the amount of recycled materials is 95% of the feed rate. The reaction temperature was controlled to 130°C and the reaction pressure was 0.8MPa. The reaction product flowing out of the static mixer outlet was separated by standing to obtain the fatty acid ester phase (upper layer), which was analyzed by Agilent’s 6890N gas chromatograph. The fatty acid triglyceride conversion rate was 100%, and the c...
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[0029] Example 2
[0030] According to the method of Example 1, except that the feed rate is one-half of the impinging stream reactor, the amount of circulating material is 75% of the feed rate. The reaction product flowing out of the discharge port of the impinging stream reactor was separated by standing to obtain the fatty acid ester phase (upper layer), which was analyzed by Agilent’s 6890N gas chromatograph. The conversion rate of fatty acid triglyceride was measured to be 100%. The content of methyl ester in the ester phase is 93.8%.
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[0031] Example 3
[0032] According to the method of Example 1, the feed rate is a ratio of a quarter of the volume of the impinging stream reactor, and the circulating material rate is 150% of the feed amount. The reaction product flowing out of the discharge port of the impinging stream reactor was separated by standing to obtain the fatty acid ester phase (upper layer), which was analyzed by Agilent’s 6890N gas chromatograph. The conversion rate of fatty acid triglyceride was measured to be 100%. The content of methyl ester in the ester phase is 94.5%.
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