# US 4,392,948 A · Process for removing the nitrogen impurities from a hydrocarbon mixture > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 4,392,948 A - Document ID: US4392948A - Status: Granted - Kind: A - Application number: 06/318,408 - Filed: 1981-11-05 - Granted: 1983-07-12 - Earliest claimed: 1979-07-06 - Assignees: Labofina, S.A. - Inventors: Guy F. S. Debande - Web page: https://patentgrep.com/patent/US4392948A ## CPC - C10G 17/04: Liquid-liquid treatment forming two immiscible phases - C10G: CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION (cracking to hydrogen or synthesis gas C01B; cracking or pyrolysis of hydrocarbon gases to individual hydrocarbons or mixtures thereof of definite or specified constitution C07C; cracking to cokes C10B); RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES ## Abstract Process for removing the nitrogen impurities from a liquid hydrocarbon mixture comprising introducing into a low volume mixer the hydrocarbons to be treated together with a dilute aqueous acid solution to form an emulsion, withdrawing said emulsion into a decantation zone where it breaks and recycling to the low volume mixer from 80 to 95% by volume of the aqueous acid solution coming from the decantation zone, so as to maintain in said low volume mixer a volume ratio of the hydrocarbons to the aqueous acid solution from about 0.3 to about 13, preferably from about 0.5 to about 4, and the pH of the aqueous acid solution from about 0.1 to about 1.5. ## Claims ### Claim 1 A process for removing nitrogen impurities from a mixture of liquid hydrocarbons containing polymerizable unsaturated hydrocarbons, which process comprises the steps of: continuously introducing a dilute aqueous acid solution into a low volume mixer, said solution having an acid concentration of from 0.01 to 5 volume percent; continuously introducing the mixture of liquid hydrocarbons into said mixer, the volume ratio of the amount of liquid hydrocarbons to the amount of aqueous acid solution being from about 0.3 to about 13; forming in the mixer an emulsion of the hydrocarbons in said aqueous acid solution by mixing during a period of time not exceeding 2 seconds the acid solution and the hydrocarbons, thereby extracting the major part of the nitrogen impurities; withdrawing the resultant emulsion into a decantation zone where the emulsion breaks and phase separation occurs; recovering the hydrocarbon phase containing not more than 2 ppm of basic nitrogen impurities from the decantation zone; recycling from 80 to 95% by volume of the used aqueous acid solution phase to the low volume mixer; withdrawing the remainder of said used aqueous acid solution phase as a purge; and adding a sufficient volume of fresh acid solution in order to maintain in the low volume mixer the volume ratio of the liquid hydrocarbon mixture to the aqueous acid solution at its initial value, the concentration of said fresh acid solution being such that the pH of the aqueous acid solution is from about 0.1 to about 1.5. ### Claim 2 (depends on 1) A process according to claim 1, wherein the liquid hydrocarbon mixture comprises hydrocarbons having a boiling point in the range from 30.degree. to 300.degree. C. ### Claim 3 (depends on 1, 2) A process according to claim 1 or 2, wherein the hydrocarbon mixture is a straight run distillate. ### Claim 4 (depends on 1, 2) A process according to claim 1 or 2, wherein the hydrocarbon mixture is obtained by thermal or catalytic cracking of heavier hydrocarbons. ### Claim 5 (depends on 4) A process according to claim 4, wherein the hydrocarbon mixture contains unsaturated hydrocarbons and has a boiling point in the gasoline range. ### Claim 6 (depends on 1) A process according to claim 1, wherein the hydrocarbon mixture is treated by means of an aqueous solution of an acid selected from the group consisting of hydrochloric acid, hydrobromic acid, hydrofluoric acid, hydroiodic acid, sulfuric acid, phosphoric acid, boric acid, fluorosulfuric acid, trifluoroacetic acid, trichloroacetic acid, formic acid, alkane sulfonic acids and alkyl benzene sulfonic acids. ### Claim 7 (depends on 6) A process according to claim 6, wherein the aqueous solution has an acid concentration of from 0.01 to 2.5% by volume. ### Claim 8 (depends on 1) A process according to claim 1, wherein from 90 to 93 volume percent of the used aqueous acid solution is recycled to the low volume mixer. ### Claim 9 (depends on 1, 8) A process according to claim 1 or 8, wherein the pH of the aqueous acid solution introduced into the mixer is maintained from about 0.5 to about 1. ### Claim 10 (depends on 1, 8) A process according to claim 1 or 8, wherein the volume ratio of the liquid hydrocarbon mixture to the aqueous acid solution is from about 0.5 to about 4. ### Claim 11 (depends on 6) A process according to claim 6, wherein said acid is selected from the group consisting of sulfuric acid and hydrochloric acid. ### Claim 12 (depends on 1) A process according to claim 1 further comprising the step of subjecting the hydrocarbon phase recovered from the decantation zone to hydrogenation treatment to remove residual nitrogen impurities. ### Claim 13 (depends on 1) A process according to claim 1, wherein said low volume mixer comprises a centrifugal pump. ### Claim 14 (depends on 1) A process according to claim 1, wherein said low volume mixer comprises a static mixer.