Gasoline engine oil composition and preparation method thereof
A technology of gasoline engine oil and composition, applied in the directions of lubricating composition, petroleum industry, additives, etc., can solve the problems of non-optimal formula performance and large amount of addition, etc.
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Embodiment 1
[0101] The preparation of embodiment 1 dispersion type ethylene-propylene copolymer viscosity index improver DOCP-1
[0102] In a 500 ml pressure reactor with temperature control, water cooling and stirring, add 10 grams of ethylene-propylene copolymer (Mw=182000, (0.000055mol) ethylene content 58%, purchased from China Petroleum Jilin Petrochemical Company), cut into 0.5 cm 3 Then add 90 grams of 150SN (produced by Sinopec Gaoqiao Petroleum Company), and add 1.137 mg (0.001mol) of tetrakis(pentafluorophenyl)phenylferric chloride porphyrin (M=1136.7) (dissolved in 2 g In acetonitrile), after adding, the temperature was raised to 100°C, and air was introduced to keep the reaction pressure at 0.2MPa. After 6 hours of constant temperature reaction, the oxidation reaction was stopped, and the catalyst was separated by filtration to obtain a mixture of the oxidative degradation product of the copolymer and 150SN. The weight-average molecular weight of the oxidative degradation pro...
Embodiment 2
[0103] Embodiment 2 Preparation of dispersed ethylene-propylene copolymer viscosity index improver DOCP-2
[0104] In a 500 ml pressure reactor with temperature control, water cooling and stirring, add 10 grams of ethylene-propylene copolymer (Mw=182000, ethylene content 58%, purchased from China Petroleum Jilin Petrochemical Company), cut into 0.5cm 3 Then add 90 grams of 150SN (produced by Sinopec Gaoqiao Petroleum Company), add 0.7 mg of tetraphenylporphyrin ferric chloride (M=704.02, 0.001mol) (dissolved in 1.5 grams of acetonitrile), and heat up to 110 ℃, feed air, keep the reaction pressure at 0.3 MPa, keep the temperature for 4 hours, stop the oxidation reaction, filter and separate the catalyst to obtain a mixture of the oxidative degradation product of the copolymer and 150SN, and the weight average molecular weight of the oxidative degradation product is measured as 110600 , the acid value is 0.20mgKOH / g. Add 0.034 g of p-diphenylamine (M=169.22) to the mixture of t...
Embodiment 3
[0105] Embodiment 3 Preparation of dispersed ethylene-propylene copolymer viscosity index improver DOCP-3
[0106] In a 500 ml pressure reactor with temperature control, water cooling and stirring, add 10 grams of ethylene-propylene copolymer (Mw=182000, ethylene content 58%, purchased from China Petroleum Jilin Petrochemical Company), cut into 0.5cm 3 Then add 90 grams of 150SN (produced by Sinopec Gaoqiao Petroleum Company), and add 1.5 mg (0.0013mol) of tetrakis(pentafluorophenyl)phenylferric chloride porphyrin (M=1136.7) (dissolved in 3 g in acetonitrile), heated up to 100°C, and fed air, kept the reaction pressure at 0.4MPa, kept at a constant temperature for 7 hours, stopped the oxidation reaction, filtered out the catalyst, and obtained a mixture of the oxidative degradation product of the copolymer and 150SN, and measured the oxidized The weight average molecular weight of the degradation product is about 123000, and the acid value is 0.15.mgKOH / g. Add 0.022 g of p-hy...
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