Antioxidant for hydraulic cylinder and preparation and application thereof
An antioxidant, hydraulic oil technology, used in additives, petroleum industry, lubricating compositions, etc., to achieve the effect of improving long-term high temperature antioxidant stability and excellent high temperature antioxidant stability
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Example 1 Antioxidant preparation
The antioxidant is prepared according to the formula in parts by weight in Table 1.
Preparation method: Mix the raw materials evenly according to the proportion.
Table 1
The structural formula of thiocarbamate in Table 1 is (C4H9)2NCS2CS2CN(C4H9)2.
Example Embodiment
Example 2 Antioxidant performance
Adopt neopentyl polyol dibasic acid complex ester (1# formula in Example 3) as the base oil and mix with various antioxidants in the table below, wherein the base oil accounts for 98wt%, and the antioxidant The total amount is 2wt%. Mix the raw materials according to the proportion and stir evenly.
Table 2
Note: The total amount of antioxidants is 2.0%, and the structural formula of thiocarbamate is (C4H9)2NCS2CS2CN(C4H9)2.
It can be seen from the data in Table 2 that the present invention selects an antioxidant compounded by diisooctyl diphenylamine, phenyl-α-naphthylamine, 2,6 di-tert-butylphenol and thiocarbamate It achieves the complementary performance advantages of various antioxidants and greatly improves the long-term high temperature oxidation stability of oil products.
Example Embodiment
Example 3 Preparation of neopentyl polyol dibasic acid double ester
The preparation process is as follows:
1. Choose a dibasic acid with carbon number of 5-12, add a mixed alcohol composed of neopentyl glycol, trimethylolpropane and neopentyl erythritol in an amount twice the amount of the dibasic acid, and then add the substance The amount of the mixed dibasic acid is 0.95-1.05% of tetraoctyl zirconate and 1.9-2.1% of p-toluenesulfonic acid as a catalyst. The reaction is stirred for 140-180 minutes at a temperature of 160-180°C to complete the first step. Esterification reaction.
2. The amount of the added substance is 4 times of the mixed dibasic acid and the monobasic fatty acid with carbon number of 14 to 20, (the monobasic fatty acid should be excessive in order to complete the second step of esterification), at a temperature of 200-220 ℃ The reaction is stirred for 100-120 minutes to complete the second step of esterification reaction.
3. The reaction product is subjec...
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