Method for separating and purifying biodiesel
A biodiesel, separation and purification technology, applied in the preparation of biofuels, biomaterials, liquid hydrocarbon mixtures, etc., can solve the problems of long production cycle, low recovery rate, pollution, etc., and achieves low equipment cost and energy consumption. Simple process and the effect of reducing production costs
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Examples
Embodiment 1
[0071] Example 1. Separation and purification of biodiesel
[0072] The specific method includes the following steps:
[0073] 1) Separation and purification: the crude biodiesel product is degassed and distilled with a thin film evaporator to obtain biodiesel with a methyl ester content of 96%:
[0074] a) Separation and purification object: lipase catalyzes the crude biodiesel product obtained by the esterification reaction of soybean oil (raw oil) with methanol. The by-product glycerin (lower layer) is removed by standing or high-speed centrifugation, and the supernatant is collected (the main component is Crude fatty acid methyl ester) as the object of separation and purification in the next step;
[0075] b) Falling film evaporation: Pass the supernatant obtained in step a) through the falling film evaporator at a vacuum of -0.06MP and a temperature of 120°C for degassing to remove the components at the outlet of the falling film evaporator (in the crude product) Low boiling poi...
Embodiment 2-5
[0090] Example 2-5. Separation and purification of biodiesel using different deacidification agents
[0091] The same method as in Example 1, wherein the dosage of alkaline solution and alkaline soil is changed to obtain purified biodiesel whose acid value meets national standards. The results are shown in Table 3.
[0092] Table 3 Results of Examples 2-5
[0093] Variation factors
Embodiment 6-9
[0094] Example 6-9. Separation and purification of biodiesel from different raw materials
[0095] Such as figure 1 As shown, the method of the present invention is used to separate and purify biodiesel. The specific method is the same as that of Example 1, except that the feedstock oil for producing crude methyl ester is changed. The important indicators of purified biodiesel are shown in Table 4.
[0096] Table 4 Results of Examples 6-9
[0097] project name
Example 6
Example 7
Example 8
Example 9
Feedstock oil for producing crude methyl ester
Acidified oil
Rapeseed oil
Tung oil
Rotating scraper thin film evaporation
Parameters
Vacuum 60Pa
Temperature 160℃
Scraper speed
130rpm
Vacuum 130Pa
Temperature 180℃
Scraper speed
135rpm
Vacuum 70Pa
Temperature 165℃
Scraper speed
140rpm
Vacuum 110Pa
Temperature 175℃
Scraper speed
130rpm
Density (20℃)
842
874
856
847
Kinematic viscosity (40℃)
3.21
3.92
2.78
...
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