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Low-sulfur diesel oil modifier, preparation method and application thereof

A low-sulfur diesel and modifier technology, which is used in the petroleum industry, fuel additives, liquid carbon-containing fuels, etc., can solve the problems that the product performance cannot meet the requirements and the high freezing point of the product, and achieves widening the source of raw materials, dense lubricating film, The effect of increasing the entanglement density

Active Publication Date: 2020-06-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, polyols are used as raw materials for transesterification to easily form a polyester structure, resulting in too high a freezing point of the product, and the performance of the product cannot meet the requirements.

Method used

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  • Low-sulfur diesel oil modifier, preparation method and application thereof
  • Low-sulfur diesel oil modifier, preparation method and application thereof
  • Low-sulfur diesel oil modifier, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Preparation of tung oil methyl ester: Add 800g tung oil, 160g methanol, and 8g potassium hydroxide into a 2L high-pressure reactor, and carry out stirring reaction. The reaction temperature is 60°C, and the reaction time is 20min. Glycerin product 76.2g, then the upper layer product was washed 3 times with 50°C hot water, and the washed product was distilled at 2000Pa and 60°C for 2h to obtain tung oil methyl ester biodiesel.

[0033] 146g of 1,4-diamino-2-butene was added into the autoclave, carbon dioxide was introduced into the autoclave to make the carbon dioxide supercritical, the pressure was controlled at 10.5MPa, the temperature was 45°C, and the stirring was started. Gradually add 500 g of tung oil methyl ester biodiesel to the reactor, so that the addition of tung oil methyl ester biodiesel is completed within 2 hours, and the reaction is continued for 4 hours to end the reaction. The reaction system is passed into the expansion separator, the pressure is redu...

Embodiment 2

[0035] Add 99g of 1,4-diamino-2-butene into the autoclave, and introduce carbon dioxide into the autoclave to make the carbon dioxide supercritical, control the pressure to 13.5MPa, the temperature to 60°C, and start stirring. Gradually add 500 g of tung oil methyl ester biodiesel to the reactor, so that the addition of tung oil methyl ester biodiesel is completed within 1 hour, and continue to react 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 supercritical carbon dioxide is converted into ordinary gas phase carbon dioxide, which is collected and reused after being discharged. The product was distilled under reduced pressure at 200°C for 2 hours at a pressure of 65 Pa to obtain a low-sulfur diesel modifier product. The reaction molecule conversion rate was 77.4%, the freezing point was -20.6°C, and the water layer was not turbid in the demulsification test.

Embodiment 3

[0037] 292g of 1,4-diamino-2-butene was added into the autoclave, carbon dioxide was introduced into the autoclave to make the carbon dioxide supercritical, the pressure was controlled at 7.5MPa, the temperature was 32°C, and stirring was started. Gradually add 500 g of tung oil methyl ester biodiesel to the reactor, so that the addition of tung oil methyl ester biodiesel 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 supercritical carbon dioxide is converted into ordinary gas phase carbon dioxide, which is collected and reused after being discharged. The product was distilled under reduced pressure at 200°C for 2 hours at a pressure of 65 Pa to obtain a low-sulfur diesel modifier product. The molecular conversion rate of the reaction was 78.6%, the freezing point of the product was -22.8°C, and the water layer was not tur...

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Abstract

The invention relates to a low-sulfur diesel oil modifier, a preparation method and application thereof. The preparation method comprises the following steps: adding unsaturated diamine into a high-pressure reactor, introducing carbon dioxide into the reactor, enabling the carbon dioxide to be in a supercritical state, starting stirring, gradually adding tung oil biodiesel, and continuously reacting for a period of time after the addition is finished; and after the reaction is finished, carrying out reduced pressure distillation to obtain the low-sulfur diesel oil modifier. According to the invention, tung oil biodiesel is modified with unsaturated diamine under a supercritical condition, the prepared modifier has the effects of good lubricity, low condensation point, small dosage and detergent, and low-sulfur diesel oil can meet national V lubricity standards and condensation point requirements after blending.

Description

technical field [0001] The invention belongs to the technical field of biodiesel, and in particular relates to a low-sulfur diesel oil modifier and its preparation method and application. Background technique [0002] With the widespread use of diesel engines, the consumption of diesel is increasing year by year. However, a large amount of diesel consumption will inevitably lead to further aggravation of vehicle emissions of harmful substances. Due to the serious impact of emissions on the ecological environment, human health and economic development, governments of various countries have successively formulated strict emission regulations to limit the harmful emissions of diesel vehicles. With the implementation of the National V standard for diesel in my country, the sulfur content of diesel will drop below 10ppm, and desulfurized diesel has been implemented in domestic refineries. At present, sulfur reduction technologies such as hydrotreating and hydrocracking are adop...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10L1/18C10L1/222C10L1/04C10L10/08C10L10/04C10L10/14
CPCC10L1/04C10L1/14C10L1/1802C10L1/2222C10L10/04C10L10/08C10L10/14C10L2270/026
Inventor 李澜鹏李秀峥曹长海王宜迪程瑾
Owner CHINA PETROLEUM & CHEM CORP