发明名称 Process
摘要 <p>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&lt;5&gt; Pa), while the second distillation zone is preferably operated at a pressure of from about 9 bar (9 x 10&lt;5&gt; bar) absolute to about 15 bar (1.5 x 10&lt;6&gt; Pa) absolute. &lt;IMAGE&gt;</p>
申请公布号 EP0992482(A1) 申请公布日期 2000.04.12
申请号 EP19980308010 申请日期 1998.10.01
申请人 KVAERNER PROCESS TECHNOLOGY LIMITED 发明人 COLLEY, STEPHEN WILLIAM;FAWCETT, CHRISTOPHER RICHARD;SHARIF, MOHAMMAD;TUCK, MICHAEL WILLIAM MARSHALL;WATSON, DAVID JOHN;WOOD, MICHAEL ANTHONY
分类号 C07C67/54;C07C69/14;(IPC1-7):C07C67/54 主分类号 C07C67/54
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