A kind of rapid demulsifier suitable for processing polymer-containing production fluid and its preparation method
A technology of liquid treatment and demulsifier, applied in the field of demulsifier and its preparation, rapid demulsifier for the treatment of polymer-containing produced fluid and its preparation, to achieve the effect of rapid demulsification
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0052] Embodiment 1, the preparation of initiator A-9 / 5 / 83
[0053] Add 5g of bisphenol A resin (structural formula as formula II, where x / y=0.5) and 1.47g of potassium hydroxide into the high temperature and high pressure reactor, and seal the reactor well. Before heating up, use nitrogen to purge and replace, then vacuumize, repeat twice, then start stirring and heat up, stop heating when the temperature rises to 120°C, open the feed valve, add 45g of propylene oxide dropwise, and control the reaction temperature. 120°C~140°C (the temperature fluctuates during the reaction process) and the initial pressure is 0.4MPa; after the reaction of the material drops to 0MPa, add 25g of butylene oxide dropwise, and control the initial pressure to 0.4MPa; After the butane reaction is completed and the pressure drops to 0MPa, add 415g of propylene oxide dropwise, and control the reaction temperature to 120°C to 140°C (the temperature fluctuates during the reaction) and the initial press...
Embodiment 2
[0056] Embodiment 2, the preparation of initiator A-9 / 7 / 83
[0057]Add 5g of bisphenol A resin (structural formula as formula II, where x / y=0.5) and 1.5g of potassium hydroxide into a high-temperature and high-pressure reactor, and seal the reactor well. Before heating up, use nitrogen to purge and replace, then vacuumize, repeat twice, then start stirring and heat up, stop heating when the temperature rises to 120°C, open the feed valve, add 45g of propylene oxide dropwise, and control the reaction temperature. 120°C~140°C (the temperature fluctuates during the reaction process) and the initial pressure is 0.4MPa; after the reaction of the material drops to 0MPa, add 35g of butylene oxide dropwise, and control the initial pressure to 0.4MPa; After the butane reaction is completed and the pressure drops back to 0MPa, add 415g of propylene oxide dropwise, and control the reaction temperature at 120°C to 140°C (the temperature fluctuates during the reaction) and the initial pres...
Embodiment 3
[0060] Embodiment 3, the preparation of initiator A-9 / 11 / 83 and A-9 / 15 / 83
[0061] Adopt the method of embodiment 1, and change the amount of butylene oxide to 55g, 75g respectively, obtain two kinds of initiators shown in formula I, mark as A-9 / 11 / 83, A-9 / 15 / 83.
[0062] In the present embodiment, the addition of potassium hydroxide is 0.3% of the total mass of bisphenol A resin, propylene oxide and butylene oxide, and the mass ratio of bisphenol A resin and the propylene oxide added for the first time is 1:9.
[0063] In the initiators A-9 / 11 / 83 and A-9 / 15 / 83 prepared in this example, m:n:p are 9:11:83 and 9:15:83, respectively.
PUM
| Property | Measurement | Unit |
|---|---|---|
| dehydration rate | aaaaa | aaaaa |
| dehydration rate | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 