کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
146137 456362 2015 16 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Hydrodynamics and residence time distribution of liquid flow in tubular reactors equipped with screen-type static mixers
ترجمه فارسی عنوان
هیدرودینامیک و زمان ماندگاری مایع جریان مایع در راکتورهای لوله ای مجهز به میکسرهای استاتیک روی صفحه نمایش
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


• Pressure drop and RTD were investigated in reactors equipped with screen mixers.
• Effect of number and geometry of mixers, and operating conditions were studied.
• Less energy is required to drive the flow when compared to other motionless mixers.
• Axial dispersion was always minimized by the presence of screen mixers.
• Choosing the proper characteristic length to calculate Re is very important.

This paper discusses the characteristics of liquid flow through tubular reactors/contactors equipped with woven mesh, screen-type static mixers from hydrodynamic and macromixing perspectives. The effect of changing the screen geometry, number of mixing elements, reactor configuration, and the operating conditions, were investigated by using four different screen types of varying mesh numbers. Pressure drop was measured over a wide range of flow rates (2300 ⩽ Re ⩽ 21,500) and was found to increase with a decreasing mesh opening. Friction factor values are also reported in the work, when compared to other types of motionless mixers, screen-type mixers were found to require much lower energy requirements with very low recorded Z values (1.15 ⩽ Z ⩽ 5) that are two to three orders of magnitude lower than those reported for other motionless mixers.Furthermore, residence time distribution experiments were conducted in the transitional and turbulent regimes (2300 ⩽ Re ⩽ 11,500). Using a deconvolution technique the RTD function was extracted in order to quantify the axial/longitudinal dispersion. The findings highlight that regardless of the number and geometry of the mixer, reactor configuration, and/or operating conditions, axial dispersion coefficients that are lower than those of an empty pipe were always recorded. The wire diameter and mesh opening were found to directly affect the axial dispersion in the reactor, while, the number of elements showed a minor effect. Furthermore, the choice of the characteristic parameter used to calculate the Reynolds number was found to be of paramount importance in analyzing the data.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Journal - Volume 279, 1 November 2015, Pages 948–963
نویسندگان
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