10 فروردین 1403
آزاده ميروكيلي

آزاده میروکیلی

مرتبه علمی: استادیار
نشانی: دانشکده مهندسی نفت، گاز و پتروشیمی - گروه مهندسی شیمی
تحصیلات: دکترای تخصصی / مهندسی شیمی
تلفن: 21222026
دانشکده: دانشکده مهندسی نفت، گاز و پتروشیمی

مشخصات پژوهش

عنوان Computational Fluid Dynamic Analysis to Investigate Methanol Synthesis on the Commercial Catalysts
نوع پژوهش مقالات در نشریات
کلیدواژه‌ها
Tubular reactors · Plate reactors · Methanol production · CFD · Heat transfer
مجله TOPICS IN CATALYSIS
شناسه DOI 10.1007/s11244-021-01519-9
پژوهشگران مژگان بازآی (نفر اول) ، حسن بازآی (نفر دوم) ، آزاده میروکیلی (نفر سوم) ، محمدرضا رحیمپور (نفر چهارم)

چکیده

In this study, a novel plate methanol reactor (shell and plate) with a higher heat transfer rate compared to the conventional counterparts (shell and tube) was investigated. In fact, in the new configuration, all of the tubes were replaced with plates, and thereby the heat transfer area increased. To compare the two configurations (the conventional reactor (CR) and the plate reactor (PLR)), a two-dimensional computational fluid dynamics (CFD) model was developed. To draw a more meaningful comparison, an equal amount of catalyst was considered for both configurations. The modeling results were also compared with available industrial data, illustrating a good agreement. Results also showed that the main superiority of the obtained temperature of reactant gas and coolant gas in PLR, respectively, was 13 °C more and 9 °C less than CR. This result implies that the increase in the surface area in PLR can increase the heat transfer rate, and thereby increasing the methanol production.