Method for preparing biodiesel with low sulfur content from gutter oil
A technology for biodiesel and waste oil, which is applied in the fields of biofuel, fatty acid preparation/refining, petroleum industry, etc., can solve the problems of reducing environmental burden, environmental pollution, and generating a large amount of waste sulfuric acid, so as to reduce production costs, reduce extraction operations, The effect of simplifying the production process
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Embodiment 1
[0029] The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Apparently, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
[0030] In an embodiment of the present invention, a method for preparing low-sulfur biodiesel from waste oil comprises:
[0031] (1) Pretreatment
[0032] Precipitate waste oil to remove mechanical impurities, and after coarse filtration, vacuum dehydrate at a temperature of 80°C-120°C to obtain raw oil;
[0033] (2) Esterification reaction
[0034] Take 628g of the above-mentioned raw material oil (acid value 113mgKoH / g, sulfur content 212ppm) into a 1000ml three-necked fl...
Embodiment 2
[0046] A method for preparing low-sulfur biodiesel from waste oil, comprising:
[0047] (1) Pretreatment
[0048] Precipitate waste oil to remove mechanical impurities, and after coarse filtration, vacuum dehydrate at a temperature of 80°C-120°C to obtain raw oil;
[0049] (2) Esterification reaction
[0050]The waste oil is coarsely filtered and vacuum dehydrated (80-120°C); 10.5 tons of the above waste oil (acid value 107mgKoH / g, sulfur content 198ppm) are measured and added to a 20m3 stainless steel reaction kettle, and then 714kg of 6.8% glycerin of waste oil quality is added, Stir and heat up the reaction, the temperature is controlled at 180-230°C, the vacuum degree is controlled at 0.02-0.05Mpa, and the reaction is carried out for 2-3.5 hours, and the acid value of the reaction solution is reduced from 107mgKOH / g to 2.81mgKOH / g.
[0051] (3) High vacuum impurity removal
[0052] Maintain the reaction temperature, increase the vacuum degree of the reactor to 0.090-0.0...
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