Method for extracting and removing nitrogen from fuel oil by using succinimide compound-triethylene glycol mixed solvent
A technology of succinimide and bromosuccinimide, which is applied in the fields of petrochemical and environmental protection, can solve the problems of denitrification effect to be improved, acidity is not strong enough, etc., and achieve a good industrial application prospect, moderate cost and mild conditions Effect
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Embodiment 1
[0019] Extractant: a mixture of chlorosuccinimide and triethylene glycol, wherein the mass fraction of chlorosuccinimide is 0.95%.
[0020] Fuel: simulated gasoline formed by mixing pyridine and n-octane, with an initial nitrogen content of 500 μg / g.
[0021] Process conditions: extraction temperature is 30°C, extraction time is 30 minutes, and the mass ratio of extraction agent to fuel oil is 1. Stir continuously during the extraction process so that the two are fully mixed evenly. After the extraction, stand still for stratification and liquid-liquid separation to obtain a denitrified oil phase and a nitrogen-enriched extraction phase.
[0022] After the above extraction operation, the nitrogen content in the fuel is 0.43 μg / g, the calculated denitrification rate is 99.91%, and the mass distribution coefficient is 1124.
Embodiment 2
[0024] Extractant: a mixture of chlorosuccinimide and triethylene glycol, wherein the mass fraction of chlorosuccinimide is 0.95%.
[0025] Fuel: simulated gasoline formed by mixing acridine and n-octane, with an initial nitrogen content of 500 μg / g.
[0026] Process conditions: extraction temperature is 30°C, extraction time is 30 minutes, and the mass ratio of extraction agent to fuel oil is 1. Stir continuously during the extraction process so that the two are fully mixed evenly. After the extraction, the liquid and liquid are separated after standing and stratifying to obtain a denitrified oil phase and a nitrogen-enriched extraction phase.
[0027] After the above extraction operation, the nitrogen content in the fuel is 0.06 μg / g, the calculated denitrification rate is 99.99%, and the mass distribution coefficient is 7852.
Embodiment 3
[0029] Extractant: a mixture of chlorosuccinimide and triethylene glycol, wherein the mass fraction of chlorosuccinimide is 0.48%.
[0030] Fuel: simulated gasoline formed by mixing indole and n-octane, with an initial nitrogen content of 500 μg / g.
[0031] Process conditions: extraction temperature is 30°C, extraction time is 30 minutes, and the mass ratio of extraction agent to fuel oil is 1. Stir continuously during the extraction process so that the two are fully mixed evenly. After the extraction, the liquid and liquid are separated after standing and stratifying to obtain a denitrified oil phase and a nitrogen-enriched extraction phase.
[0032] After the above extraction operation, the nitrogen content in the fuel is 2.94 μg / g, the calculated denitrification rate is 99.41%, and the mass distribution coefficient is 166.
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