Prepn process of calcium alkyl salicylate
A technology of base value calcium alkyl salicylate and alkylphenol calcium salt, which is applied in the field of lubricating oil, can solve problems such as lack of control means, high cost, and inability to adapt to production development, so as to achieve good social and economic benefits and improve The effect of lubricating oil acid neutralization ability and good high temperature detergency
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Embodiment 1
[0017] Embodiment 1: drop into 300.0 gram alkylphenols (ortho position about 60%, para position about 40%), 400.0 gram nonylphenol ( The ortho position is about 5%, the para position is about 95%), 51.0 grams of calcium hydroxide, and 72.0 grams of 300ZN base oil are added at the same time, the stirring is started, 54.0 grams of ethylene glycol is added, the temperature is raised to about 110 ° C, and N 2 , react at 120-130°C, 2.0Mpa for 3 hours. Cool down to about 80°C, move the crude product to a 2000ml three-necked flask with a condensation dehydrator and distill under reduced pressure to 230°C (residual pressure 2.0Kpa) to remove the water, ethylene glycol and most of the unreacted nonyl Base phenol, obtain neutral alkyl phenol calcium salt product (base number 139mgKOH / g, calcium content is 4.87%).
[0018] Move the above-mentioned alkylphenol calcium salt product into an autoclave and heat up to about 160°C, introduce carbon dioxide gas, react at 170-180°C, 2.0Mpa for 4...
Embodiment 2
[0020] Embodiment 2: drop into 300.0 gram alkylphenols (ortho position about 60%, para position about 40%), 400.0 gram dodecyl phenols in the 2000ml autoclave that has agitator, condenser, gas inlet pipe and thermometer socket Phenol (ortho position is about 5%, para position is about 95%), 51.0 grams of calcium hydroxide, and 72.0 grams of 300ZN base oil are added at the same time, stirring is started, 54.0 grams of ethylene glycol is added, the temperature is raised to about 110 ° C, and N 2 , react at 120-130°C, 2.0Mpa for 3 hours. Cool down to about 80°C, move the crude product to a 2000ml three-necked flask with a condensation dehydrator and distill under reduced pressure to 230°C (residual pressure 2.0Kpa) to remove the water, ethylene glycol and most of the unreacted nonyl Base phenol, obtain neutral alkyl phenol calcium salt product (base number 129mgKOH / g, calcium content is 4.62%).
[0021] Move the above-mentioned alkylphenol calcium salt product into an autoclave ...
Embodiment 3
[0023] Embodiment 3: drop into 300.0 gram alkylphenols (ortho position about 60%, para position about 40%), 400.0 gram dodecyl phenols in the 2000ml autoclave that has stirrer, condenser, gas inlet pipe and thermometer socket Phenol (ortho position is about 5%, para position is about 95%), 51.0 grams of calcium hydroxide, and 72.0 grams of 300ZN base oil are added at the same time, stirring is started, 54.0 grams of ethylene glycol is added, the temperature is raised to about 110 ° C, and N 2 , react at 120-130°C, 2.0Mpa for 3 hours. Cool down to about 80°C, move the crude product to a 2000ml three-necked flask with a condensation dehydrator and distill under reduced pressure to 230°C (residual pressure 2.0Kpa) to remove the water, ethylene glycol and most of the unreacted nonyl Base phenol, obtain neutral alkyl phenol calcium salt product (base number 129mgKOH / g, calcium content is 4.62%).
[0024] Move the above-mentioned alkylphenol calcium salt product into an autoclave a...
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