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Production method of high-purity dioctyl diphenylamine antioxidant

A technology of dioctyldiphenylamine and its production method, which is applied in the direction of additives, amino compound purification/separation, condensation/addition reaction to prepare amino compounds, etc., to achieve the effects of low temperature, low corrosion, and mild reaction conditions

Active Publication Date: 2020-12-15
银川兰达化工科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] At present, there are few domestic reports about the production method of high-purity alkyl diphenylamine antioxidant additives, especially the method of catalytically synthesizing alkyl diphenylamine antioxidants with cheap aluminum chloride complexes has not been reported

Method used

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  • Production method of high-purity dioctyl diphenylamine antioxidant
  • Production method of high-purity dioctyl diphenylamine antioxidant
  • Production method of high-purity dioctyl diphenylamine antioxidant

Examples

Experimental program
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Effect test

Embodiment 1

[0037] 600g of nitromethane was added into a four-necked flask with a thermometer, a stirrer, a reflux condenser and a cold bath, and N 2 , under the condition of room temperature and temperature control, slowly add 300g of anhydrous aluminum trichloride while stirring, stir until completely dissolved, obtain 900g of anhydrous aluminum trichloride complex catalyst, pour it into a brown narrow mouth bottle, Cap the bottle and set aside.

[0038] Add 169g of diphenylamine and 50.7g of aluminum trichloride complex catalyst into a 2L stainless steel reaction kettle, cover the lid of the kettle, install the thermocouple and stir, then turn on the heating switch, raise the temperature to 100°C, stir for 1 hour, and then once 784g of diisobutene was pumped in, and the reaction was continued at 100°C for 8 hours with constant stirring. Then cool down to room temperature, pour the material into a separatory funnel, let stand to separate layers, and separate and remove the lower cataly...

Embodiment 2

[0040] Add 169g of diphenylamine and 50.7g of the aluminum trichloride complex catalyst prepared in Example 1 into a 2L stainless steel reaction kettle, cover the gland, install the thermocouple, stir, turn on the heating switch, and raise the temperature to 100°C , stirred for 1 h, and then pumped 784 g of diisobutylene in one go, and continued to react at a constant temperature of 100 ° C for 8 h. Then cool down to room temperature, pour the material into a separatory funnel, let stand to separate layers, and separate and remove the lower catalyst layer. The crude product in the upper layer was washed and separated in a separatory funnel according to the crude product:water mass ratio of 100:20, and washed with hot water. The washing temperature was controlled at 60°C and washed 3 times with water. At 80°C and -0.06~-0.08MPa, the crude product after washing and separation was subjected to vacuum distillation in a three-neck flask for 2 hours. The gas-phase condensed componen...

Embodiment 3

[0042] Add 169g of diphenylamine and 50.7g of the aluminum trichloride complex catalyst prepared in Example 1 into a 2L stainless steel reaction kettle, cover the gland, install the thermocouple, stir, turn on the heating switch, and raise the temperature to 100°C , stirred for 1 h, and then pumped 784 g of diisobutylene in one go, and continued to react at a constant temperature of 100 ° C for 8 h. Then cool down to room temperature, pour the material into a separatory funnel, let stand to separate layers, and separate and remove the lower catalyst layer. Put the crude product in the upper layer into a 2L stainless steel reaction kettle, add 10g of activated clay, cover the gland, install the thermocouple, stir, turn on the heating switch, raise the temperature to 110°C, and stir for 1h to decolorize. Then cool down to 80°C, heat filter the decolorized crude product, wash and separate the filtrate in a separatory funnel according to the mass ratio of filtrate:water 100:20, wa...

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Abstract

The invention discloses a production method of a high-purity dioctyl diphenylamine antioxidant, and belongs to the field of lubricating oil and synthetic rubber. The method comprises the following steps: (1) reaction: adding diphenylamine and an anhydrous aluminum trichloride complex catalyst into a reaction kettle at normal temperature, performing heating to 50-200 DEG C, performing stirring for0.5-5 hours, pumping octene, and continuously performing stirring at constant temperature of 50-200 DEG C for 2-20 hours to finish alkylation reaction, wherein the molar ratio of the diphenylamine tothe octene to the anhydrous aluminum trichloride is 1: (2-20): (0.05-0.5); (2) separation: after the reaction is finished, transferring the material into a separation tank, standing for layering, andremoving a catalyst layer at the lower layer; (3) decolorization: after removing the catalyst layer, transferring the crude product into a stirring kettle; According to the invention, the anhydrous aluminum trichloride complex catalyst used in the method is high in activity, strong in selectivity and low in cost, the adopted production process is simple, the conditions are mild, the equipment requirement is low, and the obtained product is high in purity, light in color and good in high-temperature oxidation resistance.

Description

technical field [0001] The invention relates to a production technology of an amine antioxidant for lubricating oil and rubber, in particular to an industrial production technology of a high-purity dioctyl diphenylamine antioxidant. The antioxidant is used in lubricating oil, which can improve the anti-oxidation performance of lubricating oil, effectively delay the oxidation of oil products, and prolong the service life of oil products; used in synthetic rubber, it has a good aging protection effect and can prevent rubber thermal oxygen aging And flex cracking, and enhance the anti-ozone effect. Background technique [0002] Oxidation resistance is one of the important indicators of lubricating oil and synthetic rubber. Oxidation of lubricating oil will cause the viscosity of the oil to increase, the acid value will increase, the color will deepen, and in serious cases, paint film or other insoluble solid deposits will be formed, which will cause lubrication equipment. Corr...

Claims

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Application Information

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IPC IPC(8): C07C209/60C07C211/54C07C209/82C10M133/12C10N30/10
CPCC07C209/60C07C209/82C10M133/12C10M2215/064C07C211/54
Inventor 张卫杰陈艳梅田学刚陈其顺陈文明郑来昌
Owner 银川兰达化工科技有限公司