CATALYST CONSISTING OF GRAPHENE-SUPPORTED NANOPARTICLES FOR SELECTIVE OIL HYDROGENATION AIMED AT THE PRODUCTION OF CIS-OLEIC ACID AND THE REDUCTION OF TRANS-OLEIC ACID

1 . A nano-catalyst suitable for processes of vegetable oil hydrogenation for producing bio-lubricants or biodegradable plastics for producing copolymers, the nano-catalyst comprising an active phase composed of nickel, palladium and ruthenium, dispersed on a support consisting of graphene layers with a thickness less than 1 micron, the outer surface of which is covered with surfactant chains, which selectively hydrogenate triglycerides and enrich oil in monounsatured cis-isomers, due to steric hindrances, where the active phase has a Ni/(Pd+Ru) ratio between 1% by weight and 5% by weight.

2 . The nano-catalyst according to claim 1 , wherein the thickness of said graphene layers is between 1 nanometer and 1 micron.

3 . The nano-catalyst according to claim 1 , wherein said steric hindrances causes a surface functionalization which allows specific double bonds to access the active surface and prevents the total hydrogenation.

4 . The nano-catalyst according to the claim 1 , wherein the active phase has a Ni/(Pd+Ru) ratio equal to 2.5%, wherein the addition of palladium to nickel allows increasing the catalyst activity due to the greater palladium activity and to the heterogenization between the two metals, and wherein the presence of ruthenium results in a further heterojunction between the metals, which is capable of shifting the transformation reaction towards the production of isomers with cis-configuration.

5 . The nano-catalyst according to claim 1 , wherein the presence of graphene:

stabilizes the catalyst avoiding the aggregation of the nano-particles and connecting them electrically;

promotes the separation of the nano-catalyst from the reaction products;

pre-concentrates the reagents, namely hydrogen and triglycerides, by utilizing the absorbent properties of said graphene which contrast the diffusion phenomena and allow always having available molecules to be converted.

6 . The nano-catalyst according to the claim 1 , wherein said surfactant chains are molecules of oleic acid, linoleic acid, stearic acid, lauric acid or thiols.

7 . The nano-catalyst according to claim 1 , wherein the nano-catalyst is regenerable by washing in a solvent by centrifugation and usable in multiple processing cycles without showing activity or selectivity loss.

8 . A catalytic process of vegetable oil hydrogenation for producing a final product comprising bio-lubricants or biodegradable plastics for producing copolymers, the process comprising dispersing the nano-catalyst of claim 1 in reaction reagents comprising vegetable oils in a liquid phase and gaseous hydrogen, and separating the nano-catalyst from the reaction liquid products by filtration, wherein the bio-lubricants or biodegradable plastics consists of fat acids having a high percentage of cis-9-octadecenoic acid (cis-oleic acid), in order to reduce the formation of trans isomers of 9-octadecenoic acid (trans-oleic acid).

9 . A catalytic process of vegetable oil hydrogenation for producing bio-lubricants or biodegradable plastics for producing copolymers, the process comprising dispersing the nano-catalyst of claim 1 in reaction reagents comprising vegetable oils in a liquid phase and gaseous hydrogen, and separating the nano-catalyst from the reaction liquid products by filtration, wherein said nano-catalyst operates in a temperature range between 80° C. and 220° C.

10 . A catalytic process of vegetable oil hydrogenation for producing bio-lubricants or biodegradable plastics for producing copolymers, the process comprising dispersing the nano-catalyst of claim 1 in reaction reagents comprising vegetable oils in a liquid phase and gaseous hydrogen, and separating the nano-catalyst from the reaction liquid products by filtration, wherein said catalyst operates in a pressure range between 1 barg and 30 barg.

11 . A catalytic process of vegetable oil hydrogenation for producing bio-lubricants or biodegradable plastics for producing copolymers, the process comprising dispersing the nano-catalyst of claim 1 in reaction reagents comprising vegetable oils in a liquid phase and gaseous hydrogen, and separating the nano-catalyst from the reaction liquid products by filtration, wherein said catalyst is added to an initial oil mass in an amount between 0.2% and 10% by weight with respect to the oil forming the mass.

12 . A catalytic process of vegetable oil hydrogenation, the process comprising dispersing the catalyst in reagents consisting of vegetable oils in a liquid phase, and gaseous hydrogen, and separating the nano-catalyst from the reaction liquid products by filtration, wherein said catalyst is usable for several processing cycles after regeneration.

13 . A method for producing the nano-catalyst according to claim 1 , the method comprising:

Forming a precursor consisting of the active phase, composed of nickel, palladium and ruthenium;

Forming the formation of an activated complex between said precursor and the surfactant molecules determined by the interaction of the metal ions with the polar head of the surfactant, wherein the surfactant molecules are selected between oleic acid, linoleic acid, stearic acid, lauric acid or thiols;

Forming the formation of micelles, in a non-polar medium, and the progressive aggregation and growth of nano-particles consisting of the activated complex, the surface of which is conjugated with the surfactant molecules; and

dispersing the nano-particles thus obtained on a support consisting of graphene.

14 . The method according to claim 13 wherein said graphene support consists of a plurality of layers, the thickness of which is less than 1 micron.

15 . The nano-catalyst according to claim 1 , wherein the thickness of said graphene layers is between 1 nanometer and 10 nanometers.

16 . The process of claim 10 , wherein the catalyst operates at a pressure of 10 barg.

17 . The nano-catalyst according to claim 2 , wherein the presence of graphene:

stabilizes the catalyst avoiding the aggregation of the nano-particles and connecting them electrically;

promotes the separation of the nano-catalyst from the reaction products;

pre-concentrates the reagents, namely hydrogen and triglycerides, by utilizing the absorbent properties of said graphene which contrast the diffusion phenomena and allow always having available molecules to be converted.

18 . The nano-catalyst according to claim 3 , wherein the presence of graphene:

stabilizes the catalyst avoiding the aggregation of the nano-particles and connecting them electrically;

promotes the separation of the nano-catalyst from the reaction products;

pre-concentrates the reagents, namely hydrogen and triglycerides, by utilizing the absorbent properties of said graphene which contrast the diffusion phenomena and allow always having available molecules to be converted.

19 . The nano-catalyst according to claim 4 , wherein the presence of graphene:

stabilizes the catalyst avoiding the aggregation of the nano-particles and connecting them electrically;

promotes the separation of the nano-catalyst from the reaction products;

pre-concentrates the reagents, namely hydrogen and triglycerides, by utilizing the absorbent properties of said graphene which contrast the diffusion phenomena and allow always having available molecules to be converted.

20 . The nano-catalyst according to claim 2 , wherein the nano-catalyst is regenerable by washing in a solvent by centrifugation and usable in multiple processing cycles without showing activity or selectivity loss.