# US 8,569,550 B2 · Process for the co-production of a stream of a fatty alcohol having a first carbon chain length and a stream of a fatty alcohol having a second carbon length > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 8,569,550 B2 - Document ID: US8569550B2 - Status: Granted - Kind: B2 - Application number: 13/061,904 - Filed: 2010-03-30 - Published: 2012-01-19 - Granted: 2013-10-29 - Earliest claimed: 2009-04-07 - Assignees: Davy Process Technology Limited - Applicants: Donald Hugh McKinley; Andrew George Hiles; Rikard Umberto Andersson; John Richard Hensman - Inventors: Donald Hugh McKinley; Andrew George Hiles; Rikard Umberto Andersson; John Richard Hensman - Web page: https://patentgrep.com/patent/US8569550B2 ## CPC - C07C 29/149: with hydrogen or hydrogen-containing gases - Y02P 20/129: Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines - C07C: ACYCLIC OR CARBOCYCLIC COMPOUNDS - Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS ## Abstract A process for the co-production of a stream of a fatty alcohol having first carbon chain lengths and a stream of a fatty alcohol having a second carbon chain lengths, said second carbon chain lengths being longer than said first carbon chain lengths, said process comprising the steps of: (a) supplying a stream comprising lower alkyl esters of fatty acids having chain lengths comprising the first and second chain lengths to a first vaporization zone and contacting said stream with an amount of hydrogen recycled from step (i) which is sufficient to vaporize the lower alkyl esters of the fatty acids having the first carbon chain lengths into the hydrogen; (b) supplying the hydrogen and the vaporized lower alkyl esters of fatty acids having the first carbon chain lengths to a first reaction zone comprising catalyst and operating under reaction conditions to allow hydrogenation to the desired alcohol having first carbon chain lengths; (c) recovering from the first reaction zone an alcohol product stream having first carbon chain lengths and the hydrogen; (d) supplying the unvaporized lower alkyl esters of the fatty acids having second carbon chain lengths remaining from step (a) to a second vaporization zone; (e) contacting the unvaporized lower alkyl esters having second carbon chain lengths in the second vaporization zone with an amount of hydrogen sufficient to vaporize the lower alkyl esters having fatty acids of the second carbon chain lengths into the hydrogen; (f) supplying the hydrogen and the vaporized lower alkyl esters of fatty acids having second carbon chain lengths to a second reaction zone comprising catalyst and operating under reaction conditions to allow hydrogenation to the desired alcohol having second carbon chain lengths; (g) recovering from the second reaction zone an alcohol product stream having second carbon chain lengths and hydrogen; (h) separating the stream of fatty acid alcohol having the second carbon chain length from hydrogen; and (i) recycling a portion of the hydrogen recovered in step (h) to the first vaporization zone and a portion to the second vaporization zone. ## Claims ### Claim 1 A process for the co-production of a stream of a fatty alcohol having first carbon chain lengths and a stream of a fatty alcohol having second carbon chain lengths, said second carbon chain lengths being longer than said first carbon chain lengths, said process comprising the steps of: (a) supplying a stream comprising lower alkyl esters of fatty acids having chain lengths comprising the first and second chain lengths to a first vaporisation zone and contacting said stream with an amount of hydrogen recycled from step (i) which is sufficient to vaporise the lower alkyl esters of the fatty acids having the first carbon chain lengths into the hydrogen; (b) supplying the hydrogen and the vaporised lower alkyl esters of fatty acids having the first carbon chain lengths to a first reaction zone comprising catalyst and operating under reaction conditions to allow hydrogenation to the desired alcohol having first carbon chain lengths; (c) recovering from the first reaction zone an alcohol product stream having first carbon chain lengths and the hydrogen; (d) supplying the unvaporised lower alkyl esters of the fatty acids having second carbon chain lengths remaining from step (a) to a second vaporisation zone; (e) contacting the unvaporised lower alkyl esters having second carbon chain lengths in the second vaporisation zone with an amount of hydrogen sufficient to vaporise the lower alkyl esters having fatty acids of the second carbon chain lengths into the hydrogen; (f) supplying the hydrogen and the vaporised lower alkyl esters of fatty acids having second carbon chain lengths to a second reaction zone comprising catalyst and operating under reaction conditions to allow hydrogenation to the desired alcohol having second carbon chain lengths; (g) recovering from the second reaction zone an alcohol product stream having second carbon chain lengths and hydrogen; (h) separating the stream of fatty acid alcohol having the second carbon chain length from hydrogen; and (i) recycling a portion of the hydrogen recovered in step (h) to the first vaporisation zone and a portion to the second vapourisation zone. ### Claim 2 (depends on 1) The process according to claim 1 wherein the alcohol product stream recovered in step (c) is separated and the hydrogen is recycled to the second vaporisation zone in step (e). ### Claim 3 A process for the co-production of a stream of a C12/C14 fatty alcohol and a stream of a C16/C18 fatty alcohol comprising the steps of: (a) supplying a stream comprising lower alkyl esters of C12/C18 fatty acids to a first vaporisation zone and contacting said stream with an amount of hydrogen recycled from step (i) which is sufficient to vaporise the lower alkyl esters of the C12/C14 fatty acids into the hydrogen; (b) supplying the hydrogen and the vaporised lower alkyl esters of C12/C14 fatty acids to a first reaction zone comprising catalyst and operating under reaction conditions to allow hydrogenation to the desired C12/C14 alcohol; (c) recovering from the first reaction zone a C12/C14 alcohol product stream and hydrogen; (d) supplying the unvaporised lower alkyl esters of C16/C18 remaining from step (a) to a second vaporisation zone; (e) contacting the unvaporised lower alkyl esters of C16/C18 in the second vaporisation zone with an amount of hydrogen sufficient to vaporise the lower alkyl esters of the C16/C18 fatty acids into the hydrogen; (f) supplying the hydrogen and the vaporised lower alkyl esters of C16/C18 fatty acids to a second reaction zone comprising catalyst and operating under reaction conditions to allow hydrogenation to the desired C16/C18 alcohol; (g) recovering from the second reaction zone a C16/C18 alcohol product stream and hydrogen; (h) separating the stream of fatty acid alcohol having the second carbon chain length from hydrogen; and (i) recycling a portion of the hydrogen recovered in step (h) to the first vaporisation zone. ### Claim 4 (depends on 3) The process according to claim 3 wherein the alcohol product stream recovered in step (c) is separated and the hydrogen is recycled to the second vaporisation zone in step (e). ### Claim 5 (depends on 3) The process according to claim 3 wherein the stream of hydrogen from the first reaction zone is combined with the additional hydrogen in the second vaporisation zone. ### Claim 6 (depends on 3) The process according to claim 3 wherein the stream of hydrogen from the first reaction zone is combined with the additional hydrogen prior to the second vaporisation zone such that a single hydrogen stream is supplied to the second vaporisation zone. ### Claim 7 (depends on 1) The process according to claim 1 wherein a purge is taken to prevent the build-up of undesirable material in the system. ### Claim 8 (depends on 1) The process according to claim 1 wherein the first and second vaporisation zones are separate zones in the same vaporiser. ### Claim 9 (depends on 1) The process according to claim 1 wherein the first and second vaporisation zones are separate vaporisers. ### Claim 10 (depends on 1) The process according to claim 1 wherein the first and second reaction zones are separate zones in the same reactor. ### Claim 11 (depends on 1) The process according to claim 1 wherein the first and second reaction zones are in separate reactors.