کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
155030 456880 2014 11 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Coarse-graining of diffusion–reaction models with catalyst archipelagos
ترجمه فارسی عنوان
مدل های واکنش پراکندگی واکنش با ذرات خرد شده با اسکاتلند کاتالیزور
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


• Reduced order model is developed for diffusion and reaction in supported catalysts.
• The mesoscale kinetic constants in a single-mode model are diffusion disguised.
• The two-mode model retains the true kinetics and up-scales the microscale effects.
• Mass-transfer coefficient in two-mode model depends on crystallite distribution.

We consider the problem of diffusion and reaction in a supported catalyst in which the active sites are located on the crystallites that are distributed in the form of islands (archipelagos) on the pore walls. We determine the coarse-grained mesoscale kinetic constants in terms of the true crystallite scale constants, catalyst activity distribution, pore size and species molecular diffusivities. We analyze the effect of different catalyst archipelagos on the mesoscale rate constants. We also develop a two-mode coarse grained model to describe diffusion and reaction accurately in such systems and develop criteria under which the pore and crystallite scale gradients can be neglected. A significant result is that for moderately fast reactions, the kinetics is disguised in the coarse-grained model if a single pore space averaged concentration mode is used. However, the true kinetics may be represented accurately with the use of two concentration modes, the second mode being the activity weighted concentration.

Activity (crystallite) distribution (left) and the corresponding concentration at the wall in the axial and azimuthal directions (right) for diffusion and reaction in a cylindrical pore.Figure optionsDownload high-quality image (128 K)Download as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Science - Volume 110, 3 May 2014, Pages 44–54
نویسندگان
, ,