Method for dewaxing mineral oil compositions

1. A process for reducing a paraffin content of a mineral oil composition, the process comprising:

adding a dewaxing aid to a mineral oil composition to obtain a mixture,

cooling the mixture to form a paraffin precipitate, and

at least partly removing the paraffin precipitate,

wherein

the dewaxing aid is a copolymer mixture comprising at least four copolymers,

the copolymers of the copolymer mixture differ in composition of repeat units,

and have repeat units derived from one or more alkyl methacrylates having 16 to 18 carbon atoms, and repeat units derived from one or more alkyl acrylates having 19 to carbon atoms,

wherein the copolymer mixture is obtained by copolymerization of a monomer mixture consisting of at least one alkyl acrylate and at least one alkyl methacrylate in one polymerization step.

2. The process of claim 1 , wherein the copolymer mixture comprises at least five copolymers which differ in composition of repeat units.

3. The process of claim 2 , wherein a proportion of any copolymer in the copolymer mixture is not more than 50% by weight.

4. The process of claim 1 , wherein:

at least three of the copolymers comprise at least two different repeat units derived from alkyl (meth)acrylates having 16 to 18 carbon atoms and repeat units derived from alkyl acrylates having 19 to 22 carbon atoms;

at least one first copolymer having a higher proportion of repeat units derived from alkyl acrylates having 19 to 22 carbon atoms in an alkyl radical than at least two of the other copolymers;

at least one second copolymer has a higher proportion of repeat units derived from alkyl methacrylates having 16 to 18 carbon atoms in an alkyl radical than at least two of the other copolymers; and

at least one third copolymer has repeat units deprived from alkyl acrylates having 19 to 22 carbon atoms in an alkyl radical and having repeat units derived from alkyl methacrylates having 16 to 18 carbon atoms in an alkyl radical,

the proportion in the third copolymer of repeat units derived from alkyl acrylates having 19 to 22 carbon atoms in the alkyl radical being lower than the proportion of these repeat units in the first copolymer, and

the proportion in the third copolymer of repeat units derived from alkyl methacrylates having 16 to 18 carbon atoms in the alkyl radical being lower than a proportion of these repeat units in the second copolymer.

5. The process of claim 4 , wherein a proportion of any copolymer in the copolymer mixture is not more than 50% by weight.

6. The process of claim 1 , wherein a proportion of any copolymer in the copolymer mixture is not more than 50% by weight.

7. The process of claim 1 , wherein the copolymer mixture has a crystallization transition in a range from 30° C. to 50° C.

8. The process of claim 1 , wherein the copolymer mixture has a crystallization transition whose half-height width is at least 8° C.

9. The process of claim 1 , wherein a copolymer of the copolymer mixture comprises at least 30% by weight of repeat units derived from the alkyl acrylates having 19 to 22 carbon atoms.

10. The process of claim 1 , wherein the copolymer mixture has a weight-average molecular weight in a range from 200 000 to 500 000 g/mol.

11. The process of claim 1 , wherein the process is performed in the presence of a solvent.