发明名称 Process.
摘要 A process is described for the recovery of substantially pure ethyl acetate from a feedstock comprising ethyl acetate, ethanol and water. This uses a first distillation zone maintained under first distillation conditions effective for distillation therefrom of a first distillate comprising ethyl acetate, ethanol, and less than about 10 mol % water. The first distillate is recovered from the first distillation zone and is supplied to a second distillation zone maintained under second distillation conditions which include use of a higher pressure than that of the first distillation zone, which are effective for distillation therefrom of a second distillate comprising ethanol, water, and a minor proportion of ethyl acetate and which yield a substantially pure ethyl acetate bottom product, which is recovered. The second distillate is returned to the first distillation zone. A typical feedstock to the process contains less than about 20 mol % water which is supplied to the first distillation zone. Typically the first distillation zone is operated at a pressure of less than about 4 bar (2 x 10<5> Pa), while the second distillation zone is preferably operated at a pressure of from about 9 bar (9 x 10<5> bar) absolute to about 15 bar (1.5 x 10<6> Pa) absolute. <IMAGE>
申请公布号 ZA200102080(B) 申请公布日期 2001.09.13
申请号 ZA20010002080 申请日期 1999.09.29
申请人 KVAERNER PROCESS TECHNOLOGY LIMITED 发明人 STEPHEN WILLIAM COLLEY;CHRISTOPHER RICHARD FAWCETT;MOHAMMAD SHARIF;MICHAEL WILLIAM MARSHALL TUCK;DAVID JOHN WATSON;MICHAEL ANTHONY WOOD
分类号 C07C67/54;C07C69/14 主分类号 C07C67/54
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