Method for producing biological clean fuel
A technology for clean fuels and production methods, applied in biofuels, fuels, liquid carbon-containing fuels, etc., can solve the problems of inability to save oil resources and high investment costs of engine equipment, achieve huge social and economic benefits, rich returns, and less equipment investment Effect
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Embodiment 1
[0010] Embodiment 1: Take 100Kg of rapeseed oil deodorization distillate, 45kg of methanol, and 1.5kg of sulfuric acid, mix them into the esterification kettle, and carry out the low-carbon esterification reaction of the rapid pressurized reaction method. The pressure is 0.8MPa, and the pressure is maintained for 2 hours to obtain Mix fatty acid methyl esters; pump the obtained material into a water washing tank, wash and neutralize it to a pH value of 7; put the material into a cold analysis tank, gradually cool down and freeze to 2°C, and crystallize; filter the frozen liquid to obtain crude by-products For sterols, pump the filtrate into the methanol distillation tower, heat to 105°C for 1 hour, distill and recover excess methanol and water; pump the remaining liquid into the vacuum ester still, evacuate to 0.9KPa, and heat up to 220 °C, about 60kg of bio-clean fuel (fatty acid methyl ester) was obtained.
Embodiment 2
[0011] Example 2: Take 100kg of acidified oil, 130kg of methanol, and 1kg of sulfuric acid obtained by saponification, water washing, and acidification of peanut oil soapstock, and mix them into the esterification kettle to carry out the low-carbon esterification reaction of reflux esterification method, heat up to 80°C, and reflux the esterification Mixed fatty acid methyl esters were obtained by melting for 2 hours; the obtained materials were pumped into a water washing tank, washed and neutralized to a pH value of 7; the materials were placed in a cold analysis tank, and the temperature was gradually lowered to 1°C, and crystals were precipitated; filtered and frozen liquid to obtain crude sterol as a by-product; pump the filtrate into a methanol distillation tower, heat it to 80°C for 1 hour, and recover excess methanol and water by distillation; kPa, the temperature is raised to 200° C. to obtain about 82 kg of bio-clean fuel (fatty acid methyl ester).
Embodiment 3
[0012] Example 3: Take 100 kg of deodorized distillate in the soybean oil refining process, 350 kg of methanol, and 2 kg of sulfuric acid, and mix them into the esterification kettle to carry out the low-carbon esterification reaction of the reflux esterification method. The temperature is raised to 70 ° C, and the reflux esterification time is 2 hours, to obtain mixed fatty acid methyl esters; pump the resulting material into a washing tank, wash and neutralize to a pH value of 7; put the material into a cold analysis tank, gradually cool down to 1 °C, and crystals are precipitated; filter the frozen liquid , to obtain crude sterols as by-products; pump the filtrate into a methanol distillation tower, heat to 100°C, and process for 1 hour to recover excess methanol and water by distillation; pump the remaining liquid into a vacuum ester still, and vacuumize to 2.5 KPa, the temperature is raised to 200° C. to obtain about 70 kg of biological clean fuel (fatty acid methyl ester)...
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