Cyclohexanone-containing products and processes for making the same
AssigneeExxonMobil Chemical Patents Inc.
InventorsKendele S. Galvan, Christopher L. Becker, Jörg F. W. Weber, Ashley J. Malik
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Abstract
Disclosed are processes for making cyclohexanone from a feed mixture comprising cyclohexylbenzene, cyclohexanone, phenol, 3-cylclohexenone and optionally 2-cyclohexenone, comprising feeding the feed mixture to a first distillation column and hydrogenating a fraction from the first distillation column in a hydrogenation reactor separate from the first distillation in the presence of a hydrogenation catalyst under hydrogenation conditions. A cyclohexanone-rich upper effluent comprising 3-cyclohexenone and 2-cyclohexenone at low concentrations can be obtained from the first distillation column.
Claims20
A process for producing cyclohexanone from a first feed mixture comprising cyclohexylbenzene, cyclohexanone, phenol, and 3-cyclohexenone, the process comprising:
- feeding the first feed mixture into a first distillation column at a first feeding location on the first distillation column;
- obtaining a lower cyclohexylbenzene-rich effluent from the first distillation column;
- obtaining a first upper effluent from a first upper effluent location on the first distillation column above the first feeding location, the first upper effluent comprising cyclohexanone, cyclohexanol, and is substantially free of phenol and 3-cyclohexenone;
- obtaining a middle effluent from a middle effluent location on the first distillation column above the first feeding location and below the first upper effluent location, the middle effluent comprising cyclohexanone, phenol, and 3-cyclohexenone;
- feeding at least a portion of the middle effluent to a hydrogenation reactor, where the middle effluent contacts with hydrogen in the presence of a hydrogenation catalyst under hydrogenation conditions to produce a hydrogenation reactor effluent substantially free of 3-cylcohexenone;
- feeding at least a portion of the hydrogenation reactor effluent to the first distillation column at a recycle location between the middle effluent location and the first upper effluent location, wherein:
- the recycle location is 6 to 30 stages above the middle effluent location;
- and
- the conversion of phenol in the hydrogenation reactor is no higher than 99%.
Dependencies are inferred from the claim text.