System and Process for Making Cyclohexylbenzene
US-2015361009-A1 · Dec 17, 2015 · US
US9469580B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9469580-B2 |
| Application number | US-201314435670-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 18, 2013 |
| Priority date | Dec 17, 2010 |
| Publication date | Oct 18, 2016 |
| Grant date | Oct 18, 2016 |
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Disclosed herein is a process for dehydrogenating a hydrocarbon with a dehydrogenation catalyst comprising a step of activating the catalyst precursor in a H 2 -containing atmosphere. A particularly advantageous activation process includes heating the catalyst precursor to a temperature in a range from 400° C. to 600° C. The process of the present disclosure is particularly advantageous for dehydrogenating cyclohexane to make benzene.
Opening claim text (preview).
The invention claimed is: 1. A dehydrogenation process, the process comprising: (1A) providing a catalyst precursor comprising (i) an inorganic support, and (ii) 0.01 wt % to 10.0 wt % of a first metal selected from the Groups 6 to 10 metals of the Periodic Table of Elements based on the total weight of the catalyst precursor; (1B) obtaining an activated dehydrogenation catalyst by treating the catalyst precursor at a temperature in a range from 450° C. to 600° C. for a period of at least 15 minutes in a H 2 -containing atmosphere; and (1C) contacting a first composition comprising cyclohexane with the activated dehydrogenation catalyst in a dehydrogenation reactor under a dehydrogenation condition to convert at least a portion of the cyclohexane to benzene and obtain a dehydrogenation reaction product. 2. The process of claim 1 , wherein the temperature of step (1B) is in a range from 450° C. to 550° C. 3. The process of claim 1 , wherein the first composition in step (1C) is obtained by: (1Ba) contacting benzene and hydrogen with a hydroalkylation catalyst under a hydroalkylation condition to form a hydroalkylation reaction mixture comprising cyclohexylbenzene, cyclohexane, methylcyclopentane, and benzene; and (1Bb) obtaining from at least a portion of the hydroalkylation reaction mixture (i) a first composition that has a higher concentration of at least one of benzene and cyclohexane than cyclohexylbenzene; and (ii) a second composition that has a higher concentration of cyclohexylbenzene than benzene and cyclohexane. 4. The process of claim 3 , further comprising: (1D) recycling at least a portion of the benzene in the dehydrogenation reaction product to step (1Ba). 5. The process of claim 1 , wherein the first metal comprises Pt and/or Pd. 6. The process of claim 1 , wherein at least a portion of the first metal in the catalyst precursor in step (1A) is in an oxidation state higher than zero. 7. The process of claim 1 , wherein the catalyst precursor further comprises at least one of: (iii) from 0.01 wt % to 5.0 wt % of a second metal selected from Group 14 of the Periodic Table of Elements; and (iv) from 0.01 wt % to 10.0 wt % of a third metal selected from the Groups 1 and 2 metals of the Periodic Table of Elements. 8. The process of claim 7 , wherein the second metal comprises Sn and the third metal comprises K. 9. The process of claim 1 , wherein in step (1B), the H 2 -containing atmosphere comprises at least 90 wt % of hydrogen. 10. The process of claim 1 , wherein step (1B) comprises treating the catalyst precursor in a flowing stream of H 2 -containing atmosphere. 11. The process of claim 1 , wherein the H 2 -containing atmosphere in step (1B) has a benzene concentration of at most 1 wt %, based on the total weight of the H 2 -containing atmosphere. 12. The process of claim 3 , wherein in step (1Bb) the first composition further comprises hydrogen, and in step (1B) the H 2 -containing atmosphere is the first composition. 13. The process of claim 1 , wherein after step (1B) but before step (1C), the activated dehydrogenation catalyst is protected by a protective atmosphere free of O 2 . 14. The process of claim 13 , wherein the protective atmosphere comprises at least one of H 2 and CH 4 . 15. The process of claim 1 , wherein step (1A) comprises: (1A-1) providing the inorganic support; (1A-2) impregnating the inorganic support with a solution of a salt of the first metal to obtain an impregnated support; and (1A-3) calcining the impregnated support at a temperature in a range from 300° C. to 1000° C. 16. The process of claim 1 , wherein steps (1B) and (1C) are both conducted in the dehydrogenation reactor. 17. The process of claim 1 , wherein in step (1Ba) the first composition comprises benzene and hydrogen. 18. The process of claim 1 , wherein in step (1C), the first composition comprises 0.01 wt % to 5.0 wt % methylcyclopentane based on the total weight of the first composition, and at least a portion of the methylcyclopentane is converted into a paraffin. 19. The process of claim 1 , wherein in step (1C), the dehydrogenation condition comprises a temperature in a range from 300° C. to 600° C. 20. A process for making phenol and/or cyclohexanone, the process comprising: (2A) producing cyclohexylbenzene from the second composition obtained in step (1Bb) according to the process of claim 3 ; (2B) oxidizing at least a portion of the cyclohexylbenene to obtain an oxidation reaction product comprising cyclohexylbenzene hydroperoxide; and (2C) cleaving at least a portion of the cyclohexylbenzene hydroperoxide to produce a cleavage reaction product comprising phenol and cyclohexanone.
of germanium, tin or lead · CPC title
by decomposition of hydroperoxides, e.g. cumene hydroperoxide · CPC title
Formation of an aromatic six-membered ring from an existing six-membered ring, e.g. dehydrogenation of ethylcyclohexane to ethylbenzene · CPC title
by oxidation reactions introducing directly hydroxy groups on a =CH-group belonging to a six-membered aromatic ring with the aid of other oxidants than molecular oxygen or their mixtures with molecular oxygen · CPC title
Preparation of peroxy compounds · CPC title
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