A low-sulfur diesel lubricity improver and its synthesis method
A low-sulfur diesel oil and improver technology, applied in the petroleum industry, fuel additives, liquid carbon-containing fuels, etc., can solve the problems of increasing the risk of clogging the filter screen of the engine fuel supply pump, losing fluidity of diesel oil, high acid value and freezing point, etc. To achieve the effect of broadening the source of raw materials, dense lubricating film, and no discharge of three wastes
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Embodiment 1
[0032] Add 129g of 3-n-butenol into the autoclave, feed carbon dioxide into the autoclave to make the carbon dioxide supercritical, control the pressure to 8.0MPa, the temperature to 45°C, and start stirring. Gradually add 500 g of tungoleic acid (Anhui Ruifengde Oil Deep Processing Co., Ltd., model: T160) into the reaction kettle, and the dropping rate is basically uniform, so that the addition of tungoleic acid is completed within 2 hours. After the addition, continue to react for 4 hours to end the reaction. The reaction system is passed into the expansion separator, the pressure is reduced to normal pressure, and the phase state of supercritical carbon dioxide is transformed into ordinary gaseous carbon dioxide, which is collected and reused after being discharged. The residue was distilled under reduced pressure at 65Pa and 200°C for 2h to obtain the improver product. After calculation, the conversion rate of reaction molecules (conversion rate of carbon-carbon conjugated...
Embodiment 2
[0034] 86g of 3-butenol was added into the autoclave, and carbon dioxide was introduced into the autoclave to make the carbon dioxide in a supercritical state. The pressure was controlled at 8.5MPa, the temperature was 60°C, and the stirring was started. Gradually add 500 g of tungoleic acid to the reaction kettle, the rate of addition is substantially uniform, so that the addition of tungoleic acid is completed within 1 hour, and the reaction is continued for 3 hours to end the reaction. The reaction system is passed into the expansion separator, the pressure is reduced to normal pressure, and the phase state of supercritical carbon dioxide is transformed into ordinary gaseous carbon dioxide, which is collected and reused after being discharged. The residue was distilled under reduced pressure at 65Pa and 200°C for 2h to obtain the improver product. The reaction molecular conversion rate is 78.4%, the acid value of the product is 123.8mgKOH / g, and the freezing point is -21.9°...
Embodiment 3
[0036] Add 259g of 3-n-butenol into the autoclave, feed carbon dioxide into the autoclave to make the carbon dioxide supercritical, control the pressure to 7.5MPa, the temperature to 32°C, and start stirring. Gradually add 500 g of tungoleic acid to the reaction kettle, the rate of addition is basically uniform, so that the addition of tungoleic acid is completed within 3 hours, and the reaction is continued for 5 hours to end the reaction. The reaction system is passed into the expansion separator, the pressure is reduced to normal pressure, and the phase state of supercritical carbon dioxide is transformed into ordinary gaseous carbon dioxide, which is collected and reused after being discharged. The residue was distilled under reduced pressure at 65Pa and 200°C for 2h to obtain the improver product. The reaction molecular conversion rate is 79.2%, the acid value of the product is 120.5mgKOH / g, and the freezing point is -23.8°C.
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