A kind of preparation method of low-sulfur biodiesel
A technology of biodiesel and glycerol, which is applied to the preparation of low-sulfur biodiesel and the field of low-sulfur biodiesel, can solve the problems of high rectification cost, excessive waste water, and large equipment investment, so as to reduce the production of soap and avoid foaming. , the effect of reducing costs
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Embodiment 1
[0029] The crude biodiesel raw material used in embodiment 1 is waste oil (waste oil), and its fatty acid methyl ester content distribution is as shown in table 1:
[0030] Table 1 Contents of fatty acid methyl esters in biodiesel prepared from waste oil
[0031]
[0032] Such as figure 1 As shown, heat exchange between the raw oil and the oil after flash distillation 4 1, then preheat 2 to 240°C, add glycerin for glycerin esterification 3 (add fresh glycerin in the first production, add back to use glycerin later), glyceride The temperature of compound 3 is controlled at 240°C, the reaction time is 3 hours, and then flashing 4 is carried out (the steamed product of flashing 4 can be reused for the next glycerol esterification reaction), the top temperature of flashing 4 is 191°C, and the operating absolute pressure is 500Pa, heat exchange between oil after flashing 4 and raw oil 1 recover heat and then cool 5 to 60°C, refuel with 40% methanol and 1% KOH for transesterific...
Embodiment 2
[0036] The raw material of crude glycerol used in Example 2 is the crude glycerin obtained by transesterification and sedimentation after transesterification in the process of glycerol esterification to prepare biodiesel. Take 60.1 g of crude glycerol, and directly rectify it at an absolute pressure of 500 Pa and a top gas phase temperature of 161°C without any treatment. The composition and distillation data are shown in Table 3. It can be seen from Table 3 that the crude glycerol obtained by this process can be directly distilled without the traditional acidification and soap removal process, and the recovery rate of glycerin has reached 97.4%, which avoids the problem of acidic wastewater produced by acidification in the recovery process of glycerin.
[0037] Table 3 raw material composition and rectification data
[0038]
[0039]
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