In a stirred reactor with temperature and pressure monitoring, 96.4 g of a polypropylene glycol allyl ether having a mean molar mass of 1400 g/mol are admixed with 6.43 g of sodium hydroxide at 80° C. with stirring under nitrogen. Subsequently, 19.28 g of butyl chloride are added dropwise within one hour. The reactor is heated to 120° C. for postreaction and stirred at this temperature for another three hours. Subsequently, excess butyl chloride is distilled off and cooled to 90° C. With stirring, exactly the amount of water required to bring the amount of sodium chloride into solution is added.
The procedure is as described in Example 1, with the difference that 50 ppm of a crude oil splitter of the formula 1 (alkoxylated alkylphenol-formaldehyde resin) are added to the aqueous phase separation.
In a stirred reactor with temperature and pressure monitoring, 96.5 g of a polyalkylene glycol allyl ether having a mean molar mass of 1600 g/mol and a mixing ratio of ethylene glycol to propylene glycol of 3 to 1 are admixed with 3.7 g of sodium hydroxide at 80° C. with stirring under nitrogen. Subsequently, 11.6 g of butyl chloride are slowly added dropwise. The reactor is heated to 120° C. for postreaction and stirred at this temperature for three hours. Subsequently, excess butyl chloride is distilled off and the mixture is cooled to 90° C. With stirring, exactly the amount of water required to bring the amount of sodium chloride into solution is added.
The procedure is as described in Example 3, with the difference that 50 ppm of a crude oil splitter of the formula 1 (alkoxylated alkylphenol-formaldehyde resin) are added to the aqueous phase separation.
In a stirred reactor with temperature and pressure monitoring, 99.6 g of a polyalkylene glycol allyl ether having a mean molar mass of 2000 g/mol and a mixing ratio of ethylene glycol to propylene glycol of 1 to 1 are admixed with 0.75 g of sodium hydroxide at 80° C. with stirring under nitrogen. Subsequently, 0.95 g of methyl chloride is slowly added dropwise. The reactor is heated to 120° C. for postreaction and stirred at this temperature for a further three hours. Thereafter, excess butyl chloride is distilled off and the mixture is cooled to 90° C. With stirring, the amount of water required to bring the amount of sodium chloride into solution is added.
The procedure is as described in Example 5, with the difference that 50 ppm of a crude oil splitter of the formula 1 (alkoxylated alkylphenol-formaldehyde resin) are added to the aqueous phase separation.
Results of the phase separation experiments:
To determine the effectiveness of the emulsion breaker, the water separation from the crude product emulsion was determined as a function of time. To this end, in each case 100 ml of the crude product emulsion were introduced into breakage bottles (conical, screw-closeable, graduated glass vessels). Thereafter, the breakage bottles were placed into a temperature-controlled bath and the water separation was monitored at 80° C.
Number | Date | Country | Kind |
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10 2006 038 851.8 | Aug 2006 | DE | national |