Nonequilibrium Stage Modeling of Carbon Dioxide Absorption by Partially Carbonated Ammonia Solution
عنوان مقاله: Nonequilibrium Stage Modeling of Carbon Dioxide Absorption by Partially Carbonated Ammonia Solution
شناسه ملی مقاله: NICEC12_325
منتشر شده در دوازدهمین کنگره ملی مهندسی شیمی ایران در سال 1387
شناسه ملی مقاله: NICEC12_325
منتشر شده در دوازدهمین کنگره ملی مهندسی شیمی ایران در سال 1387
مشخصات نویسندگان مقاله:
A Ghaemi - ۱Process Simulation and Control Research Laboratory, Department of Chemical Engineering, Iran University of Science and Technology-Nuclear Science Research School, Nuclear Science and Technology Research Institute
M Ghannadi Maragheh - Nuclear Science Research School, Nuclear Science and Technology Research Institute
H Ghanadzadeh
خلاصه مقاله:
A Ghaemi - ۱Process Simulation and Control Research Laboratory, Department of Chemical Engineering, Iran University of Science and Technology-Nuclear Science Research School, Nuclear Science and Technology Research Institute
M Ghannadi Maragheh - Nuclear Science Research School, Nuclear Science and Technology Research Institute
H Ghanadzadeh
A nonequilibrium dynamic stage model has been presented for reactive absorption of carbon dioxide by amines solutions. The model has been developed based on unsteady film modeling that considers mass transfer between gas and liquid phases in both directions. The model has been validated against experimental data of carbon dioxide reactive absorption in partially carbonated ammonia solution. The
experimental data has been obtained from a pilot plant absorption column. The model equations were discritized in column height direction using method of lines. A comparison of the experimental and simulation results demonstrated their good agreement.
کلمات کلیدی: Carbon dioxide (CO2); dynamic simulation; nonequilibrium stage model;reactive absorption
صفحه اختصاصی مقاله و دریافت فایل کامل: https://civilica.com/doc/58019/