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Preparation method of quadripolymer diesel pour point depressant

A technology of diesel pour point depressant and tetrapolymer, which is applied in the petroleum industry, fuel additives, liquid carbon-containing fuels, etc., can solve the problem of single component of diesel pour point depressant, unsatisfactory pour point depressant effect, and inability to adapt to different structures Petroleum products and other problems, to achieve the effect of good pour point depressing effect

Active Publication Date: 2016-05-04
LIAONING PETROCCHEM VOCATIONAL & TECH COLLEGE
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The existing diesel pour point depressant has a single component and cannot adapt to petroleum products with different structures, so the pour point depressant effect is not ideal
With the increasing production of waxy crude oil, the existing diesel pour point depressants can no longer meet the needs

Method used

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  • Preparation method of quadripolymer diesel pour point depressant
  • Preparation method of quadripolymer diesel pour point depressant
  • Preparation method of quadripolymer diesel pour point depressant

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] a. Add cetyl alcohol, methacrylic acid and solvent toluene into a three-necked flask equipped with a thermometer, agitator, reflux condenser and water separator, heat the reaction system to 65°C to dissolve them all, and then add the catalyst p-Toluenesulfonic acid. Heat up the reaction system to 110°C and reflux occurs, maintain the reaction temperature at 120°C, and reflux for about 3 hours to obtain cetyl methacrylate; during this process, the chemical reactions occur as follows:

[0026]

[0027] Among them, R represents the alkyl group of sixteen carbon atoms

[0028] b. Add maleic anhydride and cetyl alcohol in turn to a three-necked flask equipped with a thermometer, agitator, reflux condenser, and water separator, add solvent toluene, heat to 60°C to dissolve them all, and then add catalyst p-toluene sulfonic acid. Heat to 110°C and reflux occurs, maintain the reaction temperature at 120°C, and reflux for about 3 hours to obtain cetyl alcohol ester of malei...

Embodiment 2

[0036] a. In a three-necked flask equipped with a thermometer, agitator, reflux condenser and water separator, add tetradecyl alcohol, methacrylic acid and solvent toluene, heat the reaction system to 60°C to dissolve them all, and then add the catalyst p-Toluenesulfonic acid. Heating and heating the reaction system to 110°C to reflux, maintaining the reaction temperature at 130°C, and refluxing for about 2 hours to obtain myristyl methacrylate;

[0037] b. Put maleic anhydride and myristyl alcohol into a three-necked flask equipped with a thermometer, agitator, reflux condenser and water separator in sequence, add solvent toluene, heat to 60°C to dissolve them all, then add catalyst p-toluene sulfonic acid. Heat to 110°C and reflux occurs, maintain the reaction temperature at 130°C, and reflux for about 2 hours to obtain myristyl maleic anhydride;

[0038] c. Distill the myristyl methacrylate obtained in step a under reduced pressure to remove unreacted methacrylic acid and...

Embodiment 3

[0041] a. In a three-necked flask equipped with a thermometer, agitator, reflux condenser and water separator, add stearyl alcohol, methacrylic acid and solvent toluene, heat the reaction system to 70°C to dissolve them all, and then add the catalyst p-Toluenesulfonic acid. Heating and heating the reaction system to 110°C to reflux, maintaining the reaction temperature at 110°C, and refluxing for about 4 hours to obtain stearyl methacrylate;

[0042] b. Add maleic anhydride and stearyl alcohol in sequence to a three-necked flask equipped with a thermometer, agitator, reflux condenser, and water separator, add solvent toluene, heat to 80°C to dissolve them all, and then add catalyst p-toluene sulfonic acid. Heat to 110°C and reflux occurs, maintain the reaction temperature at 110°C, and reflux for about 4 hours to obtain stearyl maleic anhydride;

[0043] c. Distill the stearyl methacrylate obtained in step a under reduced pressure to remove unreacted methacrylic acid and sol...

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Abstract

The invention discloses a preparation method of a quadripolymer diesel pour point depressant. The preparation method at least comprises the following steps: a. under the condition of a solvent, preparing higher alcohol methacrylate by using methacrylic acid and higher alcohols as raw materials and p-toluenesulfonic acid as a catalyst; b. under the condition of a solvent, preparing maleic higher alcohol ester by using maleic anhydride and higher alcohols as raw materials and p-toluenesulfonic acid as a catalyst; c. under the condition of a solvent, preparing the quadripolymer diesel pour point depressant by using higher alcohol methacrylate, maleic higher alcohol ester, vinyl acetate and acrylamide as monomers and then adding an initiator. The preparation method has the beneficial effects that the quadripolymer pour point depressant is adopted instead of existing homopolymer pour point depressants and has obviously better pour point depressing effects than the single component homopolymer pour point depressants.

Description

technical field [0001] The invention relates to the field of diesel pour point depressants, in particular to a preparation method of a tetrapolymer diesel pour point depressant. Background technique [0002] Low-temperature flow improver is a kind of oil additive that can improve the crystallization process of wax in diesel oil and make diesel oil flow continuously at low temperature. It is added in a small amount but has a great effect. According to its function, it can be divided into turbidity reducer, pour point depressant and anti-wax sedimentation agent. Diesel pour point depressant can effectively reduce the freezing point and cold filter point of diesel, so that diesel can meet the performance requirements of low temperature use, thereby increasing the production of diesel and improving the economic benefits of oil refining enterprises. Due to the small amount of addition, low cost and convenient operation, this method has become the first choice to solve the low te...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F220/18C08F218/08C08F220/56C08F222/14C10L1/238C10L10/14
CPCC08F218/08C08F220/18C08F220/1818C10L1/19C10L1/224C10L1/238C10L10/14C08F220/56C08F222/145
Inventor 马超张立新
Owner LIAONING PETROCCHEM VOCATIONAL & TECH COLLEGE
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