Antioxidant for hydraulic oil and preparation and application thereof
A technology of hydraulic oil and antioxidant, applied in the direction of additives, petroleum industry, lubricating composition, etc., to achieve excellent high-temperature anti-oxidation stability and improve long-term high-temperature anti-oxidation stability
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Embodiment 1
[0066] The preparation of embodiment 1 antioxidant
[0067] Antioxidant was prepared according to the formula in parts by weight in Table 1.
[0068] Preparation method: Mix the raw materials evenly according to the proportion.
[0069] Table 1
[0070]
[0071] The structural formula of thiocarbamate in table 1 is (C 4 h 9 ) 2 NCS 2 CS 2 CN(C 4 h 9 ) 2 .
Embodiment 2
[0072] The performance of embodiment 2 antioxidant
[0073] Adopt neopentyl polyol dibasic acid complex ester (1# formula in embodiment 3) to mix as base oil and various antioxidants in the following table, wherein said base oil accounts for 98wt%, the amount of antioxidant The total amount accounts for 2 wt%. Mix the raw materials according to the ratio and stir evenly.
[0074] Table 2
[0075]
[0076] Note: the total amount of antioxidants is 2.0%, wherein, the structural formula of thiocarbamate is (C 4 h 9 ) 2 NCS 2 CS 2 CN(C 4 h 9 ) 2 .
[0077] As can be seen from the data in Table 2, the present invention selects the antioxidant compound 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 anti-oxidation stability of oil products.
Embodiment 3
[0078] The preparation of embodiment 3 neopentyl polyol dibasic acid double ester
[0079] The preparation process is as follows:
[0080] 1. Select a dibasic acid with a carbon number of 5 to 12, add a mixed alcohol consisting of neopentyl glycol, trimethylolpropane and neopentylthritol 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% tetraoctyl zirconate and 1.9-2.1% p-toluenesulfonic acid as a catalyst, and the reaction is stirred at a temperature of 160-180°C for 140-180 minutes to complete the first step Esterification reaction.
[0081] 2. The amount of the added substance is more than 4 times of the mixed dibasic acid, and the monobasic fatty acid with a carbon number of 14 to 20, (the monobasic fatty acid should be in excess, so that the second step of the esterification reaction is complete), at a temperature of 200-220 ° C Stir the reaction for 100 to 120 minutes to complete the second ...
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