Surface-active compounds, a process for their preparation and their use

Claim 2

A surface-active compound which has been prepared by reacting (a) a block polymer of propylene oxide and ethylene oxide, having an average molecular weight of 1,650 to 7,000 and containing 10 to 50% by weight of ethylene oxide units and 50 to 90% by weight of propylene oxide units, the percentages by weight being relative to the block polymer, and (b) an oxyalkyleneated alkylphenol/aldehyde resin which has been prepared by reaction of para-alkylphenols and/or ortho-alkylphenols having 1 to 18 carbon atoms in the alkyl group, with an aliphatic aldehyde having 1 to 4 carbon atoms, in the molar ratio 1:0.5 to 2, and oxyethyleneation and/or oxypropyleneation of the reaction product with 1 to 40 moles of epoxide per phenolic hydroxyl group, with (c) formaldehyde, component (a) being used in an amount of 1 to 100 parts by weight, relative to one part by weight of component (b), and the formaldehyde being used in a 0.5-fold to 2-fold stoichiometric amount, relative to the amount of hydroxyl groups in (a) and (b), and the reaction being carried out in the presence of acid catalysts, at a temperature of 50° to 180° C.

Claim 3

A compound as claimed in claim 1, wherein component (a) is a block polymer of propylene oxide and ethylene oxide having an average molecular weight of 1,900 to 3,800 and containing 10 to 30% by weight of ethylene oxide units and 70 to 90% by weight of propylene oxide units, and component (b) is an oxyalkyleneated alkylphenol/aldehyde resin which has been prepared by reaction of para-alkylphenols and/or ortho-alkylphenols having 4 to 12 carbon atoms in the alkyl group, with formaldehyde in the molar ratio 1:0.8 to 1.3, and oxyethyleneation and/or oxypropyleneation of the reaction product with 2 to 20 moles of epoxide per phenolic OH group, and, in the reaction with formaldehyde, component (a) is used in an amount of 10 to 40 parts by weight, relative to one part by weight of component (b), and the formaldehyde is used in a 0.8-fold to 1.5-fold stoichiometric amount, relative to the amount of hydroxyl groups in (a) and (b), and the reaction temperature is 80° to 160° C.

Claim 4

A compound as claimed in claim 1, wherein component (a) is a block polymer of propylene oxide and ethylene oxide which has been prepared by adding 10 to 50% by weight of ethylene oxide, relative to the block polymer, onto a polypropylene glycol having an average molecular weight of 1,500 to 3,500, in the presence of alkaline catalysts.

Claim 5

A compound as claimed in claim 1, wherein component (b) is an oxyalkyleneated alkylphenol/aldehyde resin which has been prepared by reacting the alkylphenol and the aldehyde at a temperature of 90° to 180° C., under acid catalysis, and the oxyethyleneation and/or oxypropyleneation of the alkylphenol/aldehyde resin is carried out at a temperature of 100° to 180° C., under alkaline catalysis.

Claim 6

A process for the preparation of a compound as claimed in claim 1, which comprises reacting (a) a block polymer of propylene oxide and ethylene oxide, having an average molecular weight of 1,650 to 7,000 and containing 10 to 50% by weight of ethylene oxide units and 50 to 90% by weight of propylene oxide units, the percentages by weight being relative to the block polymer, and (b) an oxyalkyleneated alkylphenol/aldehyde resin which has been prepared by reaction of para-alkylphenols and/or ortho-alkylphenols having 1 to 18 carbon atoms in the alkyl group, with an aliphatic aldehyde having 1 to 4 carbon atoms, in the molar ratio 1:0.5 to 2, and oxyethyleneation and/or oxypropyleneation of the reaction product with 1 to 40 moles of epoxide per phenolic hydroxyl group, with (c) formaldehyde, component (a) being used in an amount of 1 to 100 parts by weight, relative to one part by weight of component (b), and the formaldehyde being used in a 0.5-fold to 2-fold stoichiometric amount, relative to the amount of hydroxyl groups in (a) and (b), and the reaction being carried out in the presence of acid catalysts, at a temperature of 50° to 180° C.

Claim 7

The process as claimed in claim 5, wherein a block polymer of propylene oxide and ethylene oxide having an average molecular weight of 1,900 to 3,800 and containing 10 to 30% by weight of ethylene oxide units and 70 to 90% by weight of propylene oxide units is used as component (a), and an oxyalkyleneated alkylphenol/aldehyde resin which has been prepared by reaction of para-alkylphenols and/or ortho-alkylphenols having 4 to 12 carbon atoms in the alkyl group, with formaldehyde in the molar ratio 1:0.8 to 1.3, and oxyethyleneation and/or oxypropyleneation of the reaction product with 2 to 20 moles of epoxide per phenolic hydroxyl group, is used as component (b), and, in the reaction with formaldehyde, component (a) is used in an amount of 10 to 40 parts by weight, relative to one part by weight of component (b), and the formaldehyde is used in a 0.8-fold to 1.5-fold stoichiometric amount, relative to the amount of hydroxyl groups in (a) and (b), and the reaction is carried out at a temperature of 80° to 160° C.

Claim 8

The process as claimed in claim 5, wherein a block polymer of propylene oxide and ethylene oxide which has been prepared by adding 10 to 50% by weight of ethylene oxide, relative to the block polymer, onto a polypropylene glycol having an average molecular weight of 1,500 to 3,500, in the presence of alkaline catalysts, is used as component (a).

Claim 9

The process as claimed in claim 5, wherein an oxyalkyleneated alkylphenol/aldehyde resin which has been prepared by reacting the alkylphenol and the aldehyde at a temperature of 90° to 180° C., under acid catalysis, is used as component (b), and the oxyethyleneation and/or oxypropyleneation of the alkylphenol/aldehyde resin is carried out at a temperature of 100° to 180° C., under alkaline catalysis.

Claim 10

A process for the separation of petroleum emulsions of the water-in-oil type, which comprises adding an effective amount of a compound as claimed in claim 1 to the petroleum emulsions.

Claim 11

The process as claimed in claim 9, wherein the compound is added in an amount of 5 to 100 ppm.

Claim 12

A process for the separation of petroleum emulsions of the water-in-oil type, which comprises adding an effective amount of a compound of claim 2 to the petroleum emulsions.

Claim 13

A process for the separation of petroleum emulsions of the water-in-oil type, which comprises adding an effective amount of a compound of claim 3 to the petroleum emulsions.

Claim 14

A process for the separation of petroleum emulsions of the water-in-oil type, which comprises adding an effective amount of a compound of claim 4 to the petroleum emulsions.