1970
DOI: 10.1016/0009-2509(70)85001-1
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Kinetics of consecutive heterogeneous catalytic reaction: Gas-phase hydrogenation of phenol on a platinum catalyst

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Cited by 9 publications
(4 citation statements)
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“…[24][25][26][27] However, cyclohexanone is readily further hydrogenated to cyclohexanol under the investigated conditions. 18,22,[28][29][30][31][32][33][34][35] Another proposed reaction pathway involves cyclohexanol formation not only via cyclohexanone but also from 1-hydroxycyclohexene or directly from phenol. [36][37][38][39][40][41][42][43][44][45] In addition, some research groups have revealed that cyclohexanone and cyclohexanol are formed independently rather than at the expense of each other (Fig.…”
Section: Reaction Pathwaysmentioning
confidence: 99%
“…[24][25][26][27] However, cyclohexanone is readily further hydrogenated to cyclohexanol under the investigated conditions. 18,22,[28][29][30][31][32][33][34][35] Another proposed reaction pathway involves cyclohexanol formation not only via cyclohexanone but also from 1-hydroxycyclohexene or directly from phenol. [36][37][38][39][40][41][42][43][44][45] In addition, some research groups have revealed that cyclohexanone and cyclohexanol are formed independently rather than at the expense of each other (Fig.…”
Section: Reaction Pathwaysmentioning
confidence: 99%
“…In 1970s, gas‐phase hydrogenation of phenol was carried out over Pt‐based catalysts which exhibited high catalytic activity . However, cyclohexanol instead of cyclohexanone was formed predominantly .…”
Section: Gas‐phase Hydrogenation Of Phenolmentioning
confidence: 99%
“…Considering the fact that the reaction routes and prerequisites for catalysts were different under different reaction conditions, the catalysts used in gas-phase and liquidphase hydrogenation of phenol were summarized and classified, respectively. 1%Pt/silica gel [15] 150 19 (initial) W/F 0.48 kg h mol À1 Fixed bed reactor 66.0 51.0 1%Pt/silica gel [15] 150 19 (initial) W/F 0.85 kg h mol À1 Fixed bed reactor 96.0 78.0 5%Pt/C [7a] 200 4.7 H 2 uptake 81.7 umol g À1 cat Fixed bed reactor 64.5 83.9 5%Pt-0.5%Cr/C [7a] 200 4.7 H 2 uptake 26.7 umol g À1 cat Fixed bed reactor 55.0 100 5%Pt-0.5%Zr/C [28] 200 4.7 H 2 uptake 20. [22] 150 -W/F phenol 385 g mol À1 h Fixed bed reactor 55.0 90.0 Pd/Ta 2 O 5 [22] 150 -W/F phenol 128 g mol À1 h Fixed bed reactor 54.0 87.0 Pd/graphite [22] 150 .…”
Section: Reaction Mechanismmentioning
confidence: 99%
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