发明名称 Method for producing n-propyl acetate and method for producing allyl acetate
摘要 Provided is a method for producing n-propyl acetate, which is capable of obtaining high-purity allyl acetate with a low amount of coexisting water and is capable of producing n-propyl acetate with a high yield. The method includes an extraction process of subjecting a raw material liquid containing allyl acetate and water to an extraction operation using water as an extraction solvent and separating the extract into an oily phase and an aqueous phase, a distillation process of distilling the oily phase to obtain a distillate containing allyl acetate as a main component, and a hydrogenation process of subjecting the distillate to a hydrogenation reaction.
申请公布号 US9040743(B2) 申请公布日期 2015.05.26
申请号 US201113637834 申请日期 2011.03.14
申请人 SHOWA DENKO K.K. 发明人 Oguchi Wataru;Maruta Hiroshi
分类号 C07C67/58;C07C67/54;C07C67/283;C07C67/055 主分类号 C07C67/58
代理机构 Sughrue Mion, PLLC 代理人 Sughrue Mion, PLLC
主权项 1. A method for producing n-propyl acetate, comprising: a first oil-water separation process of separating a raw material liquid containing allyl acetate, water and acetic acid into an oily phase (A) and an aqueous phase (A); an extraction-separation process of subjecting the oily phase (A) to an extraction operation using water as an extraction solvent and separating the extract into an oily phase (B) containing allyl acetate as a main component and an aqueous phase (B) containing water as a main component; a first distillation process of distilling the oily phase (B) to obtain a distillate (X) containing allyl acetate as a main component; a second oil-water separation process of separating the distillate (X) into an oily phase (C) and an aqueous phase (C); a second distillation process of distilling the oily phase (C) to obtain a distillate (Y) containing allyl acetate as a main component; and a hydrogenation process of subjecting the distillate(Y) to a hydrogenation reaction, wherein the concentration of water (by mass) in distillate (Y) for use in the hydrogenation reaction is 100 ppm or less.
地址 Tokyo JP