Dehydrogenation process

US9469580B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9469580-B2
Application numberUS-201314435670-A
CountryUS
Kind codeB2
Filing dateNov 18, 2013
Priority dateDec 17, 2010
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.

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.

First claim

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.

Assignees

Inventors

Classifications

  • of germanium, tin or lead · CPC title

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

  • C07C5/367Primary

    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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What does patent US9469580B2 cover?
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 deh…
Who is the assignee on this patent?
Exxonmobil Chemical Patents Inc
What technology area does this patent fall under?
Primary CPC classification C07C5/367. 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).