Synthetic method of water insoluble polyether synthetic base oil
A technology for synthesizing base oils and synthesis methods, which is applied in the field of synthesis of water-insoluble polyether synthetic base oils, can solve problems such as poor emulsification performance, insufficient compatibility, and insufficient lipophilicity, and achieve good compatibility, Strong lipophilicity and no irritating odor effect
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Embodiment 1
[0027] In the first step, n-butanol is pretreated. In the reaction vessel, put 10-20g 3A molecular sieve per 1kg of n-butanol, stir evenly, let it stand for 24 hours to filter out the molecular sieve, then put in the same fresh molecular sieve, repeat this process three times before use.
[0028] The second step is the preparation of intermediates. Put 2Kg of n-butanol and 1.75g of polymetallic catalyst into the reaction kettle, vacuumize to make the pressure reach -0.092MPa; when the temperature does not exceed 40°C, feed nitrogen into the reaction kettle to raise the pressure to 0.1Mpa, and then Vacuumize to reduce the pressure to -0.092MPa, repeat three times, raise the temperature of the reactor to 120-130°C to initiate the reaction; after the reaction, slowly add 7Kg of propylene oxide to the reactor, control the reaction temperature at 140-160°C No more than 0.2 Mpa, and the reaction time is controlled at 1.5 hours; after the dropwise addition, keep warm for 30 minute...
Embodiment 2
[0031] In the first step, n-butanol is pretreated. In the reaction vessel, put 10-20g 3A molecular sieve per 1kg of n-butanol, stir evenly, let it stand for 24 hours to filter out the molecular sieve, then put in the same fresh molecular sieve, repeat this process three times before use.
[0032] The second step is the preparation of intermediates. Put 2.5Kg of treated n-butanol and 2.2g of polymetallic catalyst into the reactor, vacuumize to make the pressure reach -0.092MPa; when the temperature does not exceed 40°C, feed nitrogen into the reactor to raise the pressure to 0.1Mpa, Vacuum again to reduce the pressure to -0.092MPa, repeat three times, raise the temperature of the reactor to 120-130°C to initiate the reaction; after the reaction, slowly add 7.5Kg of propylene oxide to the reactor, and control the reaction temperature at 140-160°C , the pressure does not exceed 0.2 Mpa, and the reaction time is controlled at 1.5 hours; after the dropwise addition, keep warm for ...
Embodiment 3
[0035] In the first step, n-butanol is pretreated. In the reaction vessel, put 10-20g 3A molecular sieve per 1kg of n-butanol, stir evenly, let it stand for 24 hours to filter out the molecular sieve, then put in the same fresh molecular sieve, repeat this process three times before use.
[0036] The second step is the preparation of intermediates. Put 3Kg of treated n-butanol and 3.0g of polymetallic catalyst into the reactor, vacuumize to make the pressure reach -0.092MPa; when the temperature does not exceed 40°C, feed nitrogen into the reactor to raise the pressure to 0.1Mpa, and then Vacuumize to reduce the pressure to -0.092MPa, repeat three times, raise the temperature of the reactor to 120-130°C to initiate the reaction; after the reaction, slowly add 9Kg propylene oxide to the reactor, control the reaction temperature at 140-160°C, No more than 0.2 Mpa, and the reaction time is controlled at 1.5 hours; after the dropwise addition, keep warm for 30 minutes, and the in...
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