- 专利标题: PROCESS FOR SEPARATING ONE OR MORE ALIPHATIC DIAMINES FROM REDUCTIVE AMINATION REACTION SOLVENTS AND IMPURITIES
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申请号: US13383325申请日: 2010-07-30
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公开(公告)号: US20120116123A1公开(公告)日: 2012-05-10
- 发明人: Stacie Santhany , Patrick Ho Sing Au-Yeung , Gerald W. Dare , Shawn D. Feist , Barry B. Fish , Daniel A. Hickman , David Jean , Erich J. Molitor , Abraham D. Schuitman , Todd William Toyzan
- 申请人: Stacie Santhany , Patrick Ho Sing Au-Yeung , Gerald W. Dare , Shawn D. Feist , Barry B. Fish , Daniel A. Hickman , David Jean , Erich J. Molitor , Abraham D. Schuitman , Todd William Toyzan
- 申请人地址: US MI Midland
- 专利权人: DOW GLOBAL TECHNOLOGIES LLC
- 当前专利权人: DOW GLOBAL TECHNOLOGIES LLC
- 当前专利权人地址: US MI Midland
- 国际申请: PCT/US2010/043915 WO 20100730
- 主分类号: C07C209/86
- IPC分类号: C07C209/86 ; C07C211/09
摘要:
The instant invention provides a process for separating one or more aliphatic diamines from reductive amination reaction solvents and impurities, and aliphatic diamines obtained via such a process. The process for separating one or more aliphatic diamines from reductive amination reaction solvents and impurities according to the instant invention comprises the steps of: (1) feeding one or more cycloaliphatic cyanoaldehydes, hydrogen, ammonia, and optionally one or more solvents into a continuous reductive amination reactor system; (2) contacting said one or more cycloaliphatic cyanoaldehydes, hydrogen, and ammonia with each other in the presence of one or more heterogeneous metal based catalyst systems at a temperature in the range of from 80° C. to about 160° C. and a pressure in the range of from 700 to 3500 psig; (3) thereby forming a product mixture comprising one or more cycloaliphatic diamines, optionally one or more bicyclic by-products, optionally one or more cycloaliphatic aminonitriles, optionally one or more cycloaliphatic aminoalcohols, optionally one or more oligomeric by-products, ammonia, water, hydrogen, and optionally one or more solvents; (4) removing said product mixture from the reactor system; (5) removing at least a portion of said ammonia, said hydrogen, or mixture thereof from said product mixture via distillation; (6) removing at least a portion of said water and said one or more optional solvents via distillation; (7) removing at least a portion of one or more optional bicyclic by-products via distillation; (8) removing one or more optional cycloaliphatic aminonitriles, one or more optional cycloaliphatic aminoalcohols, one or more optional oligomeric by-products via distillation; and (9) thereby separating said one or more cycloaliphatic diamines from said product mixture.
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