کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
67339 48478 2008 9 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Methyl oleate isomerization and hydrogenation over Ni/α-Al2O3: A kinetic study recognizing differences in the molecular size of hydrogen and organic species
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی کاتالیزور
پیش نمایش صفحه اول مقاله
Methyl oleate isomerization and hydrogenation over Ni/α-Al2O3: A kinetic study recognizing differences in the molecular size of hydrogen and organic species
چکیده انگلیسی

The kinetics of the hydrogenation and cis/trans isomerization of methyl oleate on a Ni/α-Al2O3 catalyst was studied in the absence of mass-transport limitation, at 398 K ≤ T ≤ 443 K and 370 kPa≤PH2≤650 kPa370 kPa≤PH2≤650 kPa. On the basis of the Horiuti–Polanyi mechanism, involving a σ half-hydrogenated surface intermediate, a kinetic model was derived in the framework provided by the Langmuir–Hinshelwood–Hougen–Watson formalism, using the advanced concept of semi-competitive adsorption. The classical LHHW rate equations for competitive and non-competitive adsorption between the hydrogen and large organic species were matched as asymptotic cases. Statistical results clearly demonstrated the inadequacy of the model approaching non-competitive adsorption to describe the experimental data, but the residual sum of squares between experimental data and model predictions was insufficient to discriminate between the kinetic models based on competitive and semi-competitive adsorption. However, the model considering semi-competitive adsorption gave additional indication that the adsorbed molecules of cis- and trans-methyl oleate could cover up to eleven surface sites, which is in excellent agreement with a rough estimate from primary molecular modeling. This feature seems to be the most fascinating result, since it is factual and unattainable from the classical LHHW approaches. Results and distinctive features characterizing this advanced approach are highlighted. Some insights to improve parameter estimation and adsorption model discrimination are also pointed out.

The kinetics of the cis–trans isomerization and hydrogenation of methyl oleate on a Ni/α-Al2O3 catalyst was studied in the absence of mass-transport limitation, at 398 K ≤ T ≤ 443 K and 370 kPa≤PH2≤650 kPa370 kPa≤PH2≤650 kPa. Results and distinctive features characterizing the kinetic modeling based on the advanced concept of semi-competitive adsorption model are highlighted. Adsorbed molecule of methyl oleate could cover up to seven surface sites.Figure optionsDownload as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Journal of Molecular Catalysis A: Chemical - Volume 287, Issues 1–2, 15 May 2008, Pages 24–32
نویسندگان
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