首页> 外国专利> Normal;heading 1;heading 2;heading 3;CYCLOHEXANONE PRODUCTION PROCESS WITH MULTIPLE POST-DISTILLATION

Normal;heading 1;heading 2;heading 3;CYCLOHEXANONE PRODUCTION PROCESS WITH MULTIPLE POST-DISTILLATION

机译:常规;品目1;品目2;品目3;多蒸馏后环己酮的生产过程

摘要

The present invention relates to a method for continuously preparing cyclohexanone from phenol making use of a catalyst comprising at least one catalytically active metal selected from platinum and palladium comprising hydrogenating phenol to form a product stream comprising cyclohexanone and unreacted phenol; separating at least part of the product stream, or at least part of the product stream from which one or more components having a lower boiling point than cyclohexanone have been removed, into a first fraction comprising cyclohexanone and a second fraction comprising phenol and cyclohexanol, using distillation; separating the second fraction into a third fraction, rich in cyclohexanol, and a fourth fraction, rich in phenol, using distillation; - subjecting at least part of the fourth fraction to a further distillation step, thereby forming a fifth fraction and a sixth fraction, wherein the fifth fraction is enriched in phenol compared to the sixth fraction, and wherein the sixth fraction comprises side-products having a higher boiling point than phenol, and phenol; and which method is characterized in the additional step of continuously or intermittently separating at least part of the sixth fraction to yet a further distillation step, thereby forming a seventh fraction and an eight fraction, wherein the seventh fraction is enriched in phenol compared to the eight fraction, and wherein the eight fraction comprises side-products having a higher boiling point than phenol.
机译:本发明涉及一种由苯酚连续制备环己酮的方法,该催化剂使用包含至少一种选自铂和钯的催化活性金属的催化剂,该催化剂包括将苯酚加氢以形成包含环己酮和未反应的苯酚的产物流。使用以下方法将至少一部分产物流或至少一部分产物流已被除去的产物流的至少一部分分离为包含环己酮的第一级分和包含苯酚和环己醇的第二级分蒸馏使用蒸馏将第二部分分离为富含环己醇的第三部分和富含苯酚的第四部分; -使至少一部分第四馏分经受进一步的蒸馏步骤,从而形成第五馏分和第六馏分,其中与第六馏分相比,第五馏分富含苯酚,并且其中第六馏分包含具有沸点高于苯酚和苯酚;并且该方法的特征在于将至少一部分第六馏分连续或间歇地分离至又一蒸馏步骤的附加步骤,从而形成第七馏分和第八馏分,其中与第八馏分相比,第七馏分富含苯酚馏分,其中第八馏分包含沸点比苯酚高的副产物。

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