Production process of biological diesel oil and apparatus
A biodiesel and production method technology, applied in the preparation of biological raw materials, biofuels, liquid hydrocarbon mixtures, etc., can solve the problems of unfavorable continuous production of biodiesel, low catalytic efficiency of solid catalysts, etc., achieve rapid production, reduce difficulty, The effect of reducing usage
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Embodiment 1
[0031] The raw material oil of the present invention is made from animal and vegetable fats and oils, and its acid value is less than 2mgKOH / g raw material oil. The production method of present embodiment biodiesel comprises the steps:
[0032] (1) After mixing the anhydrous methanol and KOH solution, they are mixed with the raw material oil and pumped into the mixer for full mixing, wherein the molar ratio of anhydrous methanol to the raw material oil is 4:1, and the weight ratio of KOH to the raw material oil is 0.1%; ( 2) The above mixture is input into a tubular plug flow reactor with a temperature of 40° C. (the length and diameter ratio of the plug flow reactor is greater than 50), and the tubular plug flow reactor is contained within the scope of the ultrasonic generating device (3) anhydrous methanol and feedstock oil undergo transesterification in a tubular plug flow reactor under the action of a liquid alkaline catalyst to generate crude biodiesel and glycerol, and g...
Embodiment 2
[0037] In this embodiment, the reaction temperature in the plug flow reactor is 55° C., the liquid alkaline catalyst is NaOH solution, its weight ratio to raw oil is 0.3%, and the molar ratio of anhydrous methanol to raw oil is 6:1. The reaction conditions are adopted to ensure the rapid progress of the chemical reaction, and the content of methanol is also appropriate, which can not only drive the reaction well, but also facilitate the recovery of methanol.
[0038] Other features of this embodiment are the same as those of Embodiment 1, and will not be described in detail here.
Embodiment 3
[0040] In this embodiment, the reaction temperature in the plug flow reactor is 62°C, the liquid alkaline catalyst is NaOH solution, its weight ratio to raw oil is 0.4%, and the molar ratio of anhydrous methanol to raw oil is 10:1.
[0041] Other features of this embodiment are the same as those of Embodiment 1, and will not be described in detail here.
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