Design and characterization of a Low‐pressure‐drop static mixer

迷惑 雷诺数 混合(物理) 机械 静态混合器 压力降 转速 材料科学 牛顿流体 数学 化学 热力学 分析化学(期刊) 机械工程 物理 工程类 色谱法 湍流 量子力学
作者
S. M. Hosseini,Kiyanoosh Razzaghi,Farhad Shahraki
出处
期刊:Aiche Journal [Wiley]
卷期号:65 (3): 1126-1133 被引量:24
标识
DOI:10.1002/aic.16505
摘要

Four‐blade static mixer was designed for inline mixing of Newtonian fluids at Reynolds numbers from 700 to 6800. The mixer consists of four equally spaced blades mounted on cylindrical housing with 45° rotation relative to the circumference. It was tested in three different compartments of 6, 8, and 10 mixing elements; each element rotated 45° relative to the adjacent one. Multipoint sampling was used to measure concentration downstream the mixer. The mixing quality was measured by the coefficient of variance (CoV). The CoV decreases as the energy input per unit mass increases. This effect is more pronounced when the number of mixing elements increases. For the case of 10 mixing elements, a good mixing performance (typically more than 95% mixedness or CoV < 0.05) achieved, although a marginally good mixing performance could also be achieved by eight mixing elements. The friction factors were correlated as f = C 1 /Re + C 2 /Re n with an average deviation of ±10% from experimental data. Furthermore, experimental friction factors were compared with existing models. For a wide range of Reynolds numbers, the friction factors are apparently smaller than those from SMV, KMX, and baffle‐type static mixers. © 2018 American Institute of Chemical Engineers AIChE J , 65: 1126–1133, 2019
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