# US 2025/0050319 A1 · Catalytic composition in the form of a pickering emulsion > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 2025/0050319 A1 - Document ID: US20250050319A1 - Status: Published application - Kind: A1 - Application number: 18/721,931 - Filed: 2022-12-12 - Published: 2025-02-13 - Earliest claimed: 2021-12-21 - Assignees: Ifp Energies Nouvelles - Applicants: Ifp Energies Nouvelles - Inventors: Corinne BURNICHON; Christine DALMAZZONE; Cyril DARTIGUELONGUE; Severine FORGET; Lionel MAGNA - Web page: https://patentgrep.com/patent/US20250050319A1 ## CPC - B01J 31/0271: {also containing elements or functional groups covered by B01J31/0201 - B01J31/0231} - B01J 35/27: in a liquid or molten state - B01J 13/06: by phase separation - B01J 31/0224: {being perfluorinated, i.e. comprising at least one perfluorinated moiety as substructure in case of polyfunctional compounds} - B01J 31/0225: {comprising sulfonic acid groups or the corresponding salts} - B01J 31/0235: {Nitrogen containing compounds} - B01J 31/0277: {comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature} - B01J 31/0279: {the cationic portion being acyclic or nitrogen being a substituent on a ring} - B01J 31/0284: {of an aromatic ring, e.g. pyridinium} - B01J 31/0285: {also containing elements or functional groups covered by B01J31/0201 - B01J31/0274} - B01J 31/0288: {Phosphorus} - B01J 31/0289: {Sulfur} - B01J 31/0298: {the ionic liquids being characterised by the counter-anions} - B01J 35/40: characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) - B01J 21/08: Silica - B01J 31/0294: {by polar or ionic interaction with the substrate, e.g. glass} - B01J 35/45: Nanoparticles - B01J 2231/323: Hydrometalation, e.g. bor-, alumin-, silyl-, zirconation or analoguous reactions like carbometalation, hydrocarbation - B01J 2523/51: Phosphorus - B01J 2523/62: Sulfur - B01J 2531/98: Phase-transfer catalysis in a mixed solvent system containing at least 2 immiscible solvents or solvent phases - B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS ## Abstract The present invention relates to a catalytic composition in the form of what is known as a Pickering emulsion, said composition comprising a first non-aqueous liquid phase L1 comprising hydrocarbon compounds, within which droplets of a second liquid phase L2 are stabilized by solid particles, said second liquid phase L2 comprising at least one ionic liquid of formula Q+A−, Q+ being an organic cation and A− being an anion, and in which a Brønsted acid HB is dissolved. ## Claims ### Claim 1 A catalytic composition in the form of what is known as a Pickering emulsion, said composition comprising a first non-aqueous liquid phase L1 comprising hydrocarbon compounds, within which droplets of a second liquid phase L2 are stabilized by solid particles, said second liquid phase L2 comprising at least one ionic liquid of formula Q+A−, Q+ being an organic cation and A being an anion, and in which a Brønsted acid HB is dissolved. ### Claim 2 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the organic cation Q+ is a quaternary ammonium and/or a quaternary phosphonium and/or a trialkylsulfonium, and in that the anion A− is an anion that forms with the cation Q+ a salt which is liquid below 150° C. ### Claim 3 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the anion A− is chosen from the anions tetrafluoroborate, tetraalkylborate, hexafluorophosphate, hexafluoroantimonate, alkylsulfonate, in particular methylsulfonate, perfluoroalkylsulfonate, in particular trifluoromethylsulfonate, fluorosulfonate, sulfate, phosphate, perfluoroacetate, in particular trifluoroacetate, perfluorosulfonamide, in particular bis-trifluoromethanesulfonyl amide (CF3SO2)2N—, fluorosulfonamide, perfluorosulfomethide, in particular tris-trifluoromethanesulfonyl methide (CF3SO2)3C− and carboranes. ### Claim 4 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the cation Q+ is chosen from the following compounds for which R1, R2, R3, R4, R5 and R6 are identical or different, bonded together or not, and represent hydrogen or hydrocarbyl groups having from 1 to 12 carbon atoms, in particular saturated or unsaturated alkyl groups, or cycloalkyl groups or aromatic, aryl or aralkyl, groups, comprising from 1 to 12 carbon atoms. ### Claim 5 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the Brønsted acid HB comprises an anion B chosen from the anions tetrafluoroborate, tetraalkylborates, hexafluorophosphate, hexafluoroantimonate, alkylsulfonates, in particular methylsulfonate, perfluorosulfonate, in particular trifluoromethylsulfonate, fluorosulfonate, sulfate, phosphate, perfluoroacetate, in particular trifluoroacetate, perfluorosulfonamide, in particular bis-trifluoromethanesulfonyl amide (CF3SO2)2N—, fluorosulfonamide, perfluorosulfomethide, in particular tris-trifluoromethanesulfonyl methide (CF3SO2)3C− and carborane. ### Claim 6 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the Brønsted acid HB has the formula Q2+A2−, in which Q2+ represents an organic cation comprising at least one sulfonic acid or carboxylic acid function, and A2− represents an anion, in particular the same anion as the anion A− of the ionic liquid. ### Claim 7 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the first liquid phase L1 comprises one or more saturated hydrocarbons, in particular of linear or cyclic alkane type, and/or one or more unsaturated hydrocarbons, in particular of olefin or aromatic compound type, said hydrocarbon or hydrocarbons preferably having between 3 and 20 carbon atoms. ### Claim 8 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the solid particles are chosen from: silica particles, preferably functionalized with hydrophobic hydrocarbon groups, clay particles, preferably modified with organic or amphiphilic molecules, magnetic nanoparticles, in particular of Fe3O4, carbon nanotubes, particles of graphene oxides, particles of synthetic polymers, particles of a material of natural origin preferably chosen from hydroxyapatite, chitosan, cyclodextrin, dextran, particles in the form of cellulose nanocrystals or nanofibers, particles of biological material, in particular of food grade, preferably chosen from starch, zein, soy proteins, bacteria and yeasts, with the optional addition to the particles of at least one surfactant. ### Claim 9 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the largest dimension of the droplets is between 1 μm and 1000 μm, preferably between 2 μm and 100 μm, in particular between 10 μm and 50 μm. ### Claim 10 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the content of solid particles relative to the second liquid phase L2 is from 0.1% to 10% by weight, in particular from 0.5% to 5% by weight, preferably from 1% to 3% by weight. ### Claim 11 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the ratio by volume between the second liquid phase L2 and the first liquid phase L1 is between 2:1 and 1:10, preferably between 1:1 and 1:5. ### Claim 12 (depends on 1) The catalytic composition as claimed in claim 1, characterized in that the concentration of Brønsted acid HB within the second liquid phase L2 is between 0.05% and 40.0% by weight, preferably between 0.1% and 5% by weight. ### Claim 13 (depends on 1) A process for preparing the catalytic composition as claimed in claim 1, characterized in that it comprises the following steps: dispersing solid particles in the first liquid phase L1, with stirring, in particular with magnetic or mechanical stirring, preparing the second liquid phase L2 by adding Brønsted acid to the ionic liquid comprising at least one organic cation Q+ and one anion A−, adding the second liquid phase L2 to the first liquid phase L1 with the supply of dispersive energy, in particular by mechanical stirring means, a colloid mill, a membrane system, an ultrasonic stirring means, a microfluidic system. ### Claim 14 An acid catalysis process, characterized in that a catalytic composition in the form of what is known as a Pickering emulsion is used, said composition comprising a first non-aqueous liquid phase L1 comprising hydrocarbon compounds, within which droplets of a second liquid phase L2 are stabilized by solid particles, said second liquid phase L2 comprising at least one ionic liquid of formula Q+A−, Q+ being an organic cation and A− being an anion, and in which a Brønsted acid HB is dissolved. ### Claim 15 (depends on 14) The process as claimed in claim 14, characterized in that it is a process of alkylation of aromatic hydrocarbons, of oligomerization of olefins, of dimerization of isobutene, of isomerization of n-olefins to isoolefins, of isomerization of n-paraffins to isoparaffins, and of alkylation of isobutane by olefins.