System and Process for Making Phenol and/or Cyclohexanone
US-2015375135-A1 · Dec 31, 2015 · US
US9469589B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9469589-B2 |
| Application number | US-201414891177-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 4, 2014 |
| Priority date | Jun 30, 2011 |
| Publication date | Oct 18, 2016 |
| Grant date | Oct 18, 2016 |
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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.
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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.
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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