Low-carbon methanol diesel oil and preparation method thereof
A diesel and methanol technology, used in the petroleum industry, liquid carbon-containing fuels, biofuels, etc., can solve the problems of high pollutant emissions, poor low-temperature fluidity, poor power performance, etc., and achieve high calorific value, less exhaust emissions, good fluidity
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Embodiment 1
[0018] Example 1. Weigh 25kg of vegetable oleic acid, 46.5kg of methanol, 5kg of cetyl value improver, 15kg of desulfurized heavy benzene, 5kg of n-butanol, 3kg of 0# diesel oil, and 0.5kg of nano-fuel additive, and pump the above-mentioned raw materials into the pressure-free tank through a metering pump. In the container, an electrically heated static mixer is used to circulate at 20-30° C. for 2 hours, then stand still and filter to obtain the low-carbon methanol diesel of the present invention.
[0019] The above raw materials are all commercially available products, and the nano-fuel additives in it can be commercially available Huasheng AA brand nano-fuel additives or Alexandria nano-fuel additives. Metering pumps and electric heating static mixers used in the preparation process are all conventional commercially available equipment.
Embodiment 2
[0020] Example 2. Weigh 20kg of vegetable oleic acid, 43.5kg of methanol, 8kg of cetane number improver, 18kg of desulfurized heavy benzene, 7kg of n-butanol, 3kg of 0# diesel oil, and 0.5kg of nano fuel additive, and pump the above raw materials into the pressure-free In the container, an electrically heated static mixer is used to circulate at 20-30° C. for 2 hours, then stand still and filter to obtain the low-carbon methanol diesel of the present invention.
Embodiment 3
[0021] Example 3. Weigh 30kg of vegetable oleic acid, 36.4kg of methanol, 9kg of cetane number improver, 13kg of desulfurized heavy benzene, 5kg of 0# diesel oil, 6kg of n-butanol, and 0.6kg of nano fuel additive, and pump the above raw materials into the pressure-free In the container, an electrically heated static mixer is used to circulate at 20-30° C. for 2 hours, then stand still and filter to obtain the low-carbon methanol diesel of the present invention.
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