초록 ▼

The subject of the disclosure concerns C8 or higher, linear or branched fatty chain (meth)acrylic polymers possibly containing at least one ethylene unsaturation, having a weight average molecular weight Mw of less than 20,000 g/mole, free of sulphur-containing, metallic and halogenated compounds an

The subject of the disclosure concerns C8 or higher, linear or branched fatty chain (meth)acrylic polymers possibly containing at least one ethylene unsaturation, having a weight average molecular weight Mw of less than 20,000 g/mole, free of sulphur-containing, metallic and halogenated compounds and with a residual monomer content measured by GPC of no more than 10% by weight, preferably no more than 7% by weight. A further subject of the disclosure is the synthesis method and the uses of these polymers.

대표청구항 ▼

1. A method for synthesizing C8 or higher, linear or branched fatty chain alkyl polyacrylates comprising at least one ethylene unsaturation, of weight average molecular weight Mw of less than 20,000 g/mole, free of sulphur-containing metallic and halogenated compounds, by radical polymerization in s

1. A method for synthesizing C8 or higher, linear or branched fatty chain alkyl polyacrylates comprising at least one ethylene unsaturation, of weight average molecular weight Mw of less than 20,000 g/mole, free of sulphur-containing metallic and halogenated compounds, by radical polymerization in solution and whose residual monomer content measured by GPC is no more than 10 by weight, wherein the method comprises: (a) to a reactor, a starter being added consisting of the entirety of the acrylates monomer(s) either alone or optionally in solution in an organic solvent, and the reaction medium being placed under agitation(b) the starter derived from step (a) being brought to the polymerization temperature;(c) at the polymerization temperature, a radical initiator being continuously added optionally in solution in an organic solvent;(d) the reaction medium derived from step (c) is held at the polymerization temperature for several tens of minutes;(e) the reaction medium being cooled down to a temperature of between 50 and 60° C., and at least one polymerization inhibitor being added; and(f) the polymer in solution in the organic solvent being collected. 2. The method according to claim 1, wherein the acrylate monomer(s) comprise a linear or branched chain comprising 12 to 50 carbon atoms. 3. The method according to claim 1, wherein the content of radical initiator is between 2 and 14% by weight relative to the monomers. 4. The method according to claim 1, wherein the radical initiator is an organic peroxide. 5. The method according to claim 1, wherein the radical initiator is combined with a decomposition accelerator in solution in an organic solvent, the said decomposition accelerator being added to the reaction medium simultaneously with the initiator or separately. 6. The method according to claim 5, wherein the decomposition accelerator is an aromatic amine derivative. 7. The method according to claim 1, wherein at step (e) the reaction medium is cooled down to a temperature of between 50 and 60° C. in an oxidizing atmosphere. 8. The method according to claim 1, wherein at step (f) the polymer in solution in the organic solvent is collected after filtering the impurities present in the reaction medium. 9. The method according to claim 1, wherein the polymers have a residual monomer content measured by GPC of less than 7% by weight. 10. The method according to claim 1, wherein the polymers have a linear or branched chain comprising from 16 to 40 carbon atoms. 11. The method according to claim 3, wherein the content of radical initiator is between 2 and 6% by weight relative to the monomers. 12. A method of synthesizing solvated acrylic resins with high dry extract comprising the addition of C8 or higher, linear or branched fatty chain (meth)acrylic polymers comprising at least one ethylene unsaturation, of weight average molecular weight Mw less than 20,000 g/mole, free of sulphur-containing, metallic and halogenated compounds and with a residual monomer content measured by GPC of no more than 10% by weight said polymer being obtained by radical polymerization process in solution consisting of: (a) to a reactor, a starter being added consisting of the entirety of the acrylates monomer(s) either alone or optionally in solution in an organic solvent, and the reaction medium being placed under agitation;(b) the starter derived from step (a) being brought to the polymerization temperature;(c) at the polymerization temperature, a radical initiator being continuously added optionally in solution in an organic solvent;(d) the reaction medium derived from step (c) is held at the polymerization temperature for several tens of minutes;(e) the reaction medium being cooled down to a temperature of between 50 and 60° C., and at least one polymerization inhibitor being added; and(f) the polymer in solution in the organic solvent being collected. 13. A method of adding polymers to oil formulations such as formulations of lubricants, fuels or hydrocarbons, the method comprising adding C8 or higher, linear or branched fatty chain (meth)acrylic polymers comprising at least one ethylene unsaturation, of weight average molecular weight Mw less than 20,000 g/mole, free of sulphur-containing, metallic and halogenated compounds and with a residual monomer content measured by GPC of no more than 10% by weight, said polymer being obtained by radical polymerization process comprising: (a) to a reactor, a starter being added consisting of the entirety of the acrylates monomer(s) either alone or optionally in solution in an organic solvent, and the reaction medium being placed under agitation(b) the starter derived from step (a) being brought to the polymerization temperature;(c) at the polymerization temperature, a radical initiator being continuously added optionally in solution in an organic solvent;(d) the reaction medium derived from step (c) is held at the polymerization temperature for several tens of minutes;(e) the reaction medium being cooled down to a temperature of between 50 and 60° C., and at least one polymerization inhibitor being added; and(f) the polymer in solution in the organic solvent being collected. 14. The method according to claim 13, further comprising providing hydrocarbon distillates having a boiling point of between 150 and 450° C., to enhance the efficiency of filterability additives added to the said distillates, containing co- and/or terpolymers of ethylene, C3-C5 carboxylic acid vinyl ester and mono-alcohol comprising 1 to 10 carbon atoms. 15. A C8 or higher, linear or branched fatty chain alkyl polyacrylates possibly containing at least one ethylene unsaturation, of weight average molecular weight Mw less than 20,000 g/mole, free of sulphur-containing, metallic and halogenated compounds and with a residual monomer content measured by GPC of no more than 10% by weight, said polymers being obtained by radical polymerization process solution wherein: (a) to a reactor, a starter is added consisting of the entirety of the acrylate monomer(s) either alone or optionally in solution in an organic solvent; the reaction medium is placed under agitation;(b) the starter derived from step (a) is brought to the polymerizaiton temperature;(c) at the polymerization temperature, a radical initiator is continuously added optionally in solution in an organic solvent;(d) the reaction medium derived from step (c) is held at the polymerization temperature for several tens of minutes;(e) the reaction medium is cooled down to a temperature of between 50° C. and 60° C., at least one polymerization inhibitor is added; and(f) the polymer in solution in the organic solvent is collected.