Process for producing phenol and/or cyclohexanone

US9469589B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9469589-B2
Application numberUS-201414891177-A
CountryUS
Kind codeB2
Filing dateJun 4, 2014
Priority dateJun 30, 2011
Publication dateOct 18, 2016
Grant dateOct 18, 2016

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

In a process for producing phenol and/or cyclohexanone, cyclohexylbenzene is contacted with an oxygen-containing gas in the presence of an oxidation catalyst under oxidation conditions effective to produce an oxidation effluent comprising cyclohexylbenzene hydroperoxide. At least a portion of the oxidation effluent is then subjected to a concentrating step to produce a cleavage feed having a higher concentration of cyclohexylbenzene hydroperoxide than the oxidation effluent. A cleavage reaction mixture comprising the cleavage feed is then contacted with a solid acid catalyst in a cleavage reaction zone under conditions effective to produce a cleavage product comprising phenol and cyclohexanone.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for producing phenol, the process comprising: (a) contacting cyclohexylbenzene with an oxygen-containing gas in the presence of an oxidation catalyst under oxidation conditions effective to produce an oxidation effluent comprising cyclohexylbenzene hydroperoxide at a first concentration Con1 and residual cyclohexylbenzene; (b) concentrating at least a portion of the oxidation effluent to produce a cleavage feed comprising cyclohexylbenzene hydroperoxide at a second concentration Con2, where Con2>Con1; and (c) contacting a cleavage reaction mixture formed from the cleavage feed with a solid acid catalyst in a cleavage reaction zone under conditions effective to produce a cleavage product comprising phenol and cyclohexanone; (d) dividing the cleavage product into a first fraction and a second fraction, each comprising phenol and cyclohexanone; (e) supplying a polar solvent comprising water to the second fraction to form a combined recycle stream; and (f) providing the combined recycle stream to the cleavage reaction zone. 2. The process of claim 1 , wherein the concentrating step (b) comprises distillation to remove at least a portion of the cyclohexylbenzene in the oxidation effluent. 3. The process of claim 1 , wherein Con2−Con1>10 wt %. 4. The process of claim 1 , wherein Con2−Con1>20 wt %. 5. The process of claim 1 , wherein Con1 is in a range from 10 wt % to 30 wt % and Con2 is in a range from 30 wt % to 80 wt %. 6. The process of claim 1 , wherein Con1 is in a range from 15 wt % to 25 wt % and Con2 is in a range from 40 wt % to 60 wt %. 7. The process of claim 1 , wherein the weight ratio of the first fraction to the second fraction is in a range from 1 to 50. 8. The process of claim 1 , wherein the solid acid catalyst comprises an acidic molecular sieve. 9. The process of claim 8 , wherein the acidic molecular sieve comprises an aluminosilicate zeolite. 10. The process of claim 8 , wherein the acidic molecular sieve comprises at least one of zeolite beta, faujasite, ZSM-12, mordenite and an MCM-22 family molecular sieve. 11. The process of claim 1 , further comprising: (g) regenerating at least a portion of the solid acid catalyst. 12. A process for producing phenol, the process comprising: (a) hydroalkylating benzene with hydrogen in the presence of a hydroalkylation catalyst under conditions effective to produce a hydroalkylation reaction product comprising cyclohexylbenzene; (b) contacting at least a portion of the cyclohexylbenzene from the hydroalkylation reaction product with an oxygen-containing gas in the presence of an oxidation catalyst under oxidation conditions effective to produce an oxidation effluent comprising cyclohexylbenzene hydroperoxide at a first concentration Con1 and residual cyclohexylbenzene; (c) concentrating at least a portion of the oxidation effluent to produce a cleavage feed comprising cyclohexylbenzene hydroperoxide at a second concentration Con2, where Con2>Con1; and (d) contacting a cleavage reaction mixture formed from the cleavage feed with a solid acid catalyst in a cleavage reaction zone under conditions effective to produce a cleavage product comprising phenol and cyclohexanone; (e) dividing the cleavage product into a first fraction and a second fraction, each comprising phenol and cyclohexanone; (f) supplying a polar solvent comprising water to the second fraction to form a combined recycle stream; and (g) providing the combined recycle stream to the cleavage reaction zone. 13. The process of claim 12 , wherein the concentrating step (b) comprises distillation to remove at least a portion of the residual cyclohexylbenzene in the oxidation effluent. 14. The process of claim 12 , wherein Con2−Con1>10 wt %. 15. The process of claim 12 , wherein Con2−Con1>20 wt %. 16. The process of claim 12 , wherein Con1 is in a range from 10 wt % to 30 wt %, and Con2 is in a range from 30 wt % to 80 wt %. 17. The process of claim 12 , wherein Con1 is in a range from 15 wt % to 25 wt %, and Con2 is in a range from 40 wt % to 60 wt %. 18. The process of claim 12 , wherein the weight ratio of the first fraction to the second fraction is from 1 to 50. 19. The process of claim 12 , wherein the solid acid catalyst comprises an acidic molecular sieve. 20. The process of claim 19 , wherein the acidic molecular sieve comprises an aluminosilicate zeolite. 21. The process of claim 19 , wherein the acidic molecular sieve comprises at least one of zeolite beta, faujasite, ZSM-12, mordenite and an MCM-22 family molecular sieve. 22. The process of claim 12 , further comprising: (e) regenerating at least a portion of the solid acid catalyst.

Assignees

Inventors

Classifications

  • the carbon atom belonging to a ring other than a six-membered aromatic ring · CPC title

  • by decomposition of hydroperoxides, e.g. cumene hydroperoxide · CPC title

  • by addition with simultaneous hydrogenation · CPC title

  • Phenol · CPC title

  • Polycyclic hydrocarbons or acyclic hydrocarbon derivatives thereof · CPC title

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What does patent US9469589B2 cover?
In a process for producing phenol and/or cyclohexanone, cyclohexylbenzene is contacted with an oxygen-containing gas in the presence of an oxidation catalyst under oxidation conditions effective to produce an oxidation effluent comprising cyclohexylbenzene hydroperoxide. At least a portion of the oxidation effluent is then subjected to a concentrating step to produce a cleavage feed having a hi…
Who is the assignee on this patent?
Exxonmobile Chemical Patents Inc, Exxonmobil Chemical Patents Inc
What technology area does this patent fall under?
Primary CPC classification C07C45/53. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Oct 18 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).