A kind of deep eutectic solvent for extraction and denitrification of fuel oil and its application method
A low eutectic solvent, fuel oil technology, applied in chemical instruments and methods, processing hydrocarbon oil, petroleum industry, etc., can solve the problems of easily polluted oil, insufficient acidity of extractant Bronsted, and poor removal effect of non-basic nitrogen, etc. , to achieve the effect of simple separation, high oil yield and good industrial application potential
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Embodiment 1
[0018] Extractant composition: polyethylene glycol dicarboxylic acid (dcPEG-250) with a molecular weight of 250, tetraethylammonium chloride (TEACl), wherein the molar ratio of TEACl to dcPEG-250 is 1:1. The model fuel is mixed with indole (500μg / g), toluene (25wt%) and n-octane.
[0019] Extraction and denitrification operating conditions: the mass ratio of extractant to oil is 1:1, the extraction temperature is 30°C, and the extraction stirring time is 15 minutes. After detecting and calculating the denitrified oil phase obtained by extraction, it can be known that the denitrification rate is 98.5%, and the distribution coefficient D N was 63, and the oil yield was 96.9%.
Embodiment 2
[0021] Extractant composition: dcPEG-250, TEACl, wherein the molar ratio of TEACl to dcPEG-250 is 0.5:1. The model fuel is mixed with indole (500μg / g), toluene (25wt%) and n-octane.
[0022] Extraction and denitrification operating conditions: the mass ratio of extractant to oil is 1:1, the extraction temperature is 21°C, and the extraction stirring time is 15 minutes. After detecting and calculating the denitrified oil phase obtained by extraction, it can be known that the denitrification rate is 98.8%, and the distribution coefficient D N was 82, and the oil yield was 97.1%.
Embodiment 3
[0024] Extractant composition: dcPEG-250, TEACl, wherein the molar ratio of TEACl to dcPEG-250 is 0.5:1. The model fuel oil was mixed with quinoline (500μg / g), toluene (25wt%) and n-octane.
[0025] Extraction and denitrification operating conditions: the mass ratio of extractant to oil is 1:1, the extraction temperature is 30°C, and the extraction stirring time is 15 minutes. After detecting and calculating the denitrified oil phase obtained by extraction, it can be known that the denitrification rate is 99.1%, and the distribution coefficient D N was 108, and the oil yield was 97.0%.
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