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Preparation method of liquid hindered phenol carboxylic ester antioxidant

A phenol carboxylate and antioxidant technology, which is applied in the field of preparation of liquid antioxidants, can solve the problems of complex post-treatment process, loss of raw material alcohol, environmental problems, etc., and achieves simplified product post-treatment process, reduced reaction time, The effect of avoiding environmental problems

Active Publication Date: 2014-05-28
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The above preparation method can obtain a higher reaction conversion rate, but using LiOH and KOH as catalysts may cause part of the raw material alcohol to be lost due to the reaction to generate soap, and it is difficult to obtain a higher reaction conversion rate, and the reaction temperature is higher and the reaction time Longer and no nitrogen protection leads to darker product color. In addition, due to the production of soap, the post-treatment process is more complicated and environmental problems
Using titanium tetraisopropoxide as the catalyst requires water washing in the post-treatment stage, resulting in complicated post-treatment process and environmental problems caused by organic wastewater.

Method used

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  • Preparation method of liquid hindered phenol carboxylic ester antioxidant
  • Preparation method of liquid hindered phenol carboxylic ester antioxidant
  • Preparation method of liquid hindered phenol carboxylic ester antioxidant

Examples

Experimental program
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preparation example Construction

[0017] The preparation method of the solid base catalyst is as follows: uniformly mix magnesium oxide powder and NaY zeolite in a predetermined ratio, irradiate at a microwave frequency of 1000-3000 MHz for 10-60 minutes, and then activate at 180-300 ° C, and the activation time is preferably 1-5 minutes. hours, a solid base catalyst was obtained.

[0018] The solid base catalyst can continue to be used after being regenerated. The regeneration method is to wash the reacted catalyst with ethanol, filter it, and then activate it at 180-300° C., and the activation time is preferably 1-5 hours.

[0019] The present invention will be described in detail below by examples, but the present invention is not limited thereto.

example 1

[0021] Weigh 160g of decanol, 7g of KOH and 0.6g of nickel powder into a 250ml three-necked reaction bottle with stirring and water separator, stir well and heat up to 230°C, during the reaction process, the water produced by the reaction is continuously removed by the water separator The reaction system was separated, the reaction was carried out for 60 minutes, and the reaction was terminated. After the reactant was cooled, it was filtered. The filtrate is distilled under reduced pressure to obtain C with a purity of more than 95% by mass. 20 Guerbert ol.

[0022] The magnesium oxide powder and NaY zeolite were uniformly mixed at a mass ratio of 1:5.7, irradiated at a microwave frequency of 2000MHz for 30min, and then activated at 200°C for 3 hours to obtain a solid base catalyst A, wherein the MgO content was 15% by mass.

[0023] 149g (0.5mol) C 20 Grignard alcohol, 146g (0.5 mole) (3,5-di-tert-butyl-4-hydroxyphenyl) methyl propionate and 1.25g solid base catalyst A wer...

example 2

[0026] Weigh 160g of octanol, 7g of KOH and 0.4g of nickel powder into a 250ml three-necked reaction bottle with stirring and water separator, stir well and raise the temperature to 220°C. The reaction system was separated, the reaction was carried out for 50 minutes, and the reaction was terminated. After the reactant was cooled, it was filtered. The filtrate is subjected to vacuum distillation to obtain C with a purity of more than 95% by mass. 16 Guerbert ol.

[0027] The magnesium oxide powder and NaY zeolite were uniformly mixed at a mass ratio of 1:11.5, irradiated at a microwave frequency of 1200MHz for 20min, and then activated at 180°C for 2 hours to obtain a solid base catalyst B, wherein the MgO content was 8% by mass.

[0028] 121g (0.5mol) C 16 Grignard alcohol, 146g (0.5 mole) (3,5-di-tert-butyl-4-hydroxyphenyl) methyl propionate and 1.5g solid base catalyst B were added to the reaction system with a water separator, stirred and heated . Under the protection...

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Abstract

A preparation method of liquid hindered phenol carboxylic ester antioxidant includes steps of: reacting hindered phenol carboxylic-acid methyl ester in formula (I) with branched fatty alcohol of C10-C36 under the presence of solid alkaline catalyst, wherein the solid alkaline catalyst is NaY zeolite carrying magnesium oxide, the catalyst contains 1-50% of the magnesium oxide by mass, the formula (I) is shown in the description, and in the equation (I), R1 and R2 are C1-C8 alkyl, and R3 is C1-C5 alkylene. By using the inventive method, productivity is improved, reaction temperature is reduced, reaction time is shortened, and the color of products is modified.

Description

technical field [0001] The invention relates to a preparation method of a liquid antioxidant, in particular to a preparation method of a liquid hindered phenol carboxylate antioxidant. Background technique [0002] Antioxidants are essential additives for lubricating oil, fuel oil and plastic rubber processing industries. There are many types of antioxidants, mainly including phenolic type, amine type, phenolic ester type, thioester type, phosphite type, etc. Among them, hindered phenolic acid ester antioxidants are widely used because of their excellent antioxidative effect. The production process of hindered phenolic carboxylate antioxidants is simple, but the molecular weight is relatively low, and most of them are solids, which affects their use in high-performance and high-demand lubricating oils. [0003] The preparation of high molecular weight liquid hindered phenolic acid ester antioxidants by transesterification is known. CN1611563A discloses a kind of preparatio...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C67/03C07C69/732
Inventor 陈晓伟梁兵梁宇翔
Owner CHINA PETROLEUM & CHEM CORP