1968
DOI: 10.1016/s0360-0564(08)60428-9
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Stereochemistry and Mechanism of Hydrogenation of Naphthalenes on Transition Metal Catalysts and Conformational Analysis of the Products

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Cited by 99 publications
(46 citation statements)
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“…Thus, in the case of decalin, the conversion in the cis -isomer dehydrogenation in the temperature range 300–340 °C approaches the maximum values, while the highest conversion of trans -decalin in this range barely reaches 70%. At the same time, the calculation of the equilibrium constants of all elementary acts occurring during the dehydrogenation of decalin and perhydroterphenyl indicates that the cis -isomer has a tendency to transition to a more stable trans -isomer over the entire temperature range under study [ 18 , 19 ]. Taking into account the cis-trans transition during dehydrogenation of decalin, this leads to a decrease in the overall reaction rate and affects the completeness of hydrogen release.…”
Section: Resultsmentioning
confidence: 99%
“…Thus, in the case of decalin, the conversion in the cis -isomer dehydrogenation in the temperature range 300–340 °C approaches the maximum values, while the highest conversion of trans -decalin in this range barely reaches 70%. At the same time, the calculation of the equilibrium constants of all elementary acts occurring during the dehydrogenation of decalin and perhydroterphenyl indicates that the cis -isomer has a tendency to transition to a more stable trans -isomer over the entire temperature range under study [ 18 , 19 ]. Taking into account the cis-trans transition during dehydrogenation of decalin, this leads to a decrease in the overall reaction rate and affects the completeness of hydrogen release.…”
Section: Resultsmentioning
confidence: 99%
“…In considering various methods for the calculation of the relative distribution of isomers, perhaps the simplest approach is the semiempirical method developed by Weitkamp (1968) for the dimethylcyclohexanes, methyldecalins, and dimethyldecalins. The advantages of this procedure are that few thermodynamic data are needed and the results are easily extended to the methyl and polymethyl derivatives of other systems, e.g., anthracene, phenanthrene, diphenyl, etc.…”
Section: Resultsmentioning
confidence: 99%
“…The symmetry number can be incorporated into the calculation of isomer distribution as follows: 10.0 7.5 9.4 2.9 0.0 0.0 0.0 "Results obtained by calculation using CHEMIX; see text, (this work). bResulta obtained by calculation using the method described by Weitkamp (1968) with k = 1.5; see text (this work). 'Product from catalytic cracker unit, Bass Strait crude oil (this work).…”
Section: Resultsmentioning
confidence: 99%
“…Hydrogenation of NL is well studied in gas-phase and liquid-phase processes [5,6,9,[12][13][14].A few studies have reported data on the hydrogenation of aromatics in SC CO2 [15,16]but, to date, there are no reports on TL catalytic synthesis in SC solvent (i.e., hexane) conditions. The best catalytic systems of NL hydrogenation are based on nanoparticles (NPs) of platinum, palladium, nickel and their combinations with other metals supported on coal, alumina, zinc oxide, and zeolites [6,[9][10][11]14,[16][17][18][19][20][21] allowing integral selectivity with respect to TL in the range of 94-99% at high NL conversions, or transforming TL to DLs under more stringent conditions. Typically, the activity of platinum-containing catalysts to produce TL is in the temperature range of 200-300 °C and pressures of 4-6 MPa.…”
Section: Introductionmentioning
confidence: 99%