کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
10263667 | 457135 | 2005 | 12 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
On the Langmuir-Hinshelwood formulation for zeolite catalysed reactions
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کلمات کلیدی
Entropy effectsMFI zeolite - MFI زئولیتIsomerization - ایزومریزاسیونSimulated moving bed reactor - رآکتور بستر متحرک متحرکPacked bed reactor - راکتور بسته بندی شدهLangmuir–Hinshelwood kinetics - سینتیک Langmuir-HinshelwoodMolecular simulations - شبیه سازی های مولکولیIdeal Adsorbed Solution Theory - نظریه راه حل جذب ایده آلZeolite catalysis - کاتالیز زئولیت
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
![عکس صفحه اول مقاله: On the Langmuir-Hinshelwood formulation for zeolite catalysed reactions On the Langmuir-Hinshelwood formulation for zeolite catalysed reactions](/preview/png/10263667.png)
چکیده انگلیسی
The Langmuir-Hinshelwood (LH) rate expression is often used to describe the kinetics of heterogeneously catalysed reactions using zeolites. A factor θVnâ¡(1-âiθi)n in the LH expression allows for the reduction of the reaction rate with increased fractional occupancies θi of the individual species involved in an n-molecular reaction on the catalyst surface. Most commonly in practice the multicomponent Langmuir (MCL) approach is used for calculation of the fractional occupancies giving θVâ¡1/(1+âibipi) where the bi are the Langmuir adsorption constants and pi are the partial pressures in the gas phase. The LH-MCL approach is, however, thermodynamically consistent only when the saturation capacities of all the individual species in the mixture are identical to one another, or when the component loadings are small. For mixtures containing molecules with different saturation capacities, the sorption loadings are significantly affected by entropy effects, especially for high loadings within the zeolite catalyst. In the general case we need to determine the sorption loadings, and occupancies, using the Ideal Adsorbed Solution Theory. Using the gas phase isomerization of n-hexane with MFI zeolite catalyst as an illustration we demonstrate the limitations of the LH-MCL kinetics for calculation of reactor conversions. More significantly, we demonstrate how entropy effects can be exploited in simulated moving bed reactor configuration to obtain supra-equilibrium conversions and improved reaction selectivities.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Science - Volume 60, Issue 4, February 2005, Pages 1155-1166
Journal: Chemical Engineering Science - Volume 60, Issue 4, February 2005, Pages 1155-1166
نویسندگان
R. Krishna, R. Baur,