Dehydrogenation process
First Claim
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1. A dehydrogenation process comprising:
- contacting a composition comprising at least 50 wt % of benzene and at least 0.1 wt % of cyclohexane, the wt % s based upon total weight of the composition, with a dehydrogenation catalyst having oxygen chemisorption value of greater than 30%, said dehydrogenation catalyst comprising;
(i) 0.05 to 0.5 wt % of tin;
(ii) 0.1 to 2 wt % of a metal selected from Groups 6 to 10 of the Periodic Table of the Elements, and (iii) a support, the wt % s based upon total weight of the dehydrogenation catalyst, wherein the dehydrogenation catalyst is prepared by sequential impregnation with the tin being applied to the support before the metal selected from Groups 6 to 10 of the Periodic Table of the Elements, and further wherein the dehydrogenation catalyst contains no cobalt.
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Abstract
Disclosed herein is a process for dehydrogenating a saturated cyclic hydrocarbon and/or 5-membered ring compound with a dehydrogenation catalyst. The dehydrogenation catalyst comprises: (i) 0.05 wt % to 5 wt % of a metal selected from Group 14 of the Periodic Table of Elements; and (ii) 0.1 wt % to 10 wt % of a metal selected from Groups 6 to 10 of the Periodic Table of Elements. The process is conducted under dehydrogenation conditions effective to dehydrogenate at least a portion saturated cyclic hydrocarbon and/or 5-membered ring compound.
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Citations
17 Claims
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1. A dehydrogenation process comprising:
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contacting a composition comprising at least 50 wt % of benzene and at least 0.1 wt % of cyclohexane, the wt % s based upon total weight of the composition, with a dehydrogenation catalyst having oxygen chemisorption value of greater than 30%, said dehydrogenation catalyst comprising; (i) 0.05 to 0.5 wt % of tin;
(ii) 0.1 to 2 wt % of a metal selected from Groups 6 to 10 of the Periodic Table of the Elements, and (iii) a support, the wt % s based upon total weight of the dehydrogenation catalyst, wherein the dehydrogenation catalyst is prepared by sequential impregnation with the tin being applied to the support before the metal selected from Groups 6 to 10 of the Periodic Table of the Elements, and further wherein the dehydrogenation catalyst contains no cobalt. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9)
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10. A dehydrogenation process comprising:
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(a) providing a composition comprising at least 0.1 wt % of cyclohexane and at least 0.05 wt % of methylcyclopentane; and (b) producing a dehydrogenation reaction product by contacting at least a portion of the composition with a dehydrogenation catalyst under conditions effective to convert;
(i) at least a portion of the cyclohexane to benzene; and
(ii) at least a portion of the methylcyclopentane to at least one paraffin,wherein the dehydrogenation catalyst has oxygen chemisorption value of greater than 30%, and comprises;
(i) 0.05 wt % to 0.5 wt % of tin;
(ii) 0.1 wt % to 2 wt % of a metal selected from Groups 6 to 10 of the Periodic Table of the Elements, and (iii) a support, the wt % s based upon total weight of the dehydrogenation catalyst, further wherein the dehydrogenation catalyst contains no cobalt, and further wherein the dehydrogenation catalyst is produced by a method comprising(i) treating the support with the Group 14 metal to form a treated support; (ii) calcining the treated support at a temperature of 100°
C. to 700°
C.;(iii) impregnating the support with the Group 6 to 10 metal to form an impregnated support; and (iv) calcining the impregnated support at a temperature of 100°
C. to 700°
C.,wherein the impregnating step (iii) is effected after the treating step (i). - View Dependent Claims (11, 12, 13, 14, 15, 17)
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16. A process for producing cyclohexylbenzene, the process comprising:
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(a) contacting benzene and hydrogen in the presence of a hydroalkylation catalyst under hydroalkylation conditions effective to form a hydroalkylation reaction product comprising cyclohexylbenzene, cyclohexane, methylcyclopentane, and benzene; (b) separating at least a portion of the hydroalkylation reaction product into (i) a first composition that is rich in at least one of benzene, cyclohexane, and methylcyclopentane; and
(ii) a second composition that is rich in cyclohexylbenzene;(c) contacting at least a portion of the first composition with a dehydrogenation catalyst under conditions effective to convert at least a portion of the cyclohexane to benzene, wherein the dehydrogenation catalyst has oxygen chemisorption value of greater than 30% , and comprises;
(i) 0.05 to 0.5 wt % of tin;
(ii) 0.1 to 2 wt % of a metal selected from Groups 6 to 10 of the Periodic Table of the Elements;
(iii) a support; and
(iv) no cobalt, the wt % s based upon total weight of the dehydrogenation catalyst, further wherein the dehydrogenation catalyst is prepared by sequential impregnation with the tin being applied to the support before the metal selected from Groups 6 to 10 of the Periodic Table of the Elements; and(d) recycling at least a portion of the benzene formed in step (c) to the contacting step (a).
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Specification