振荡振幅对中尺度振荡折流板反应器停留时间分布的影响

H. W. Yussof, S. Bahri, A. Phan, Ap Harvey
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引用次数: 2

摘要

振荡折流板反应器技术的一项最新进展是缩小反应器的规模,使其能够用于诸如小规模连续生产生物乙醇等应用。研制了一种中尺度振荡折流板反应器(MOBR),该反应器具有中央折流板系统。本文的目的是通过评估停留时间分布(RTD)来分析MOBR内部的混合条件,净流雷诺数(Re n)分别为4.2、8.4和12.6,对应的流速分别为1.0、2.0和3.0 ml/min,振荡雷诺数(Re o)在62至622之间,Strouhal数(Str)在0.1至1.59之间。在频率、幅值和速度比分别为4 ~ 8hz、1 ~ 4mm和1 ~ 118时,研究了振荡频率和幅值对RTD性能的影响。振荡频率的影响导致RTD的方差随着振荡频率从5 Hz增加到8 Hz而增加,在6 Hz处达到峰值0.264。5赫兹以上的频率进一步增加导致RTD略微变宽并正偏斜。在5 Hz频率下,在1 ~ 4 mm范围内的所有测试振幅值的RTD剖面都接近高斯形式。在低振幅下,即xo =1 mm,方差在Re =156时在0.842左右达到最小值。当雷诺数增加到300以上时,方差迅速增加到1.28,随后消除了塞流行为,反应器的行为类似于单个连续搅拌槽反应器。化工研究通报19(2017)111-117
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Effect of Oscillation Amplitude on the Residence Time Distribution for the Mesoscale Oscillatory Baffled Reactor
A recent development in oscillatory baffled reactor technology is down-scaling the reactor, so that it can be used for the applications such as small-scale continuous production of bioethanol. A mesoscale oscillatory baffled reactor (MOBR) with central baffle system was developed and fabricated at mesoscales (typically 5 mm diameter). This present work aims to analyse the mixing conditions inside the MOBR by evaluating the residence time distribution (RTD) against the dynamic parameters of net flow Reynolds number ( Re n ) at 4.2, 8.4 and 12.6 corresponding to flow rates of 1.0, 2.0 and 3.0 ml/min respectively, oscillatory Reynolds number ( Re o ) between 62 to 622, and Strouhal number ( Str ) between 0.1 to 1.59. The effect of oscillation frequency and amplitude on RTD performance were studied at frequency, amplitude, and velocity ratio ranging from 4 to 8 Hz, 1 to 4 mm and 1 to 118, respectively. Effect of oscillation frequency has resulted in the variance of the RTD increased as the oscillation frequency increased from 5 Hz to 8 Hz and peak at 6 Hz of 0.264. A further increase in the frequency above 5 Hz caused the RTD to slightly broaden and positively skewed. At frequency of 5 Hz, the RTD profiles were close to Gaussian form for all tested amplitude values from 1 mm to 4 mm. At low amplitudes, i.e. xo = 1 mm, the variance exhibited its minimum around 0.842 at Re o =156. An increase in Re o above 300 resulted in increased in the variance rapidly to 1.28, and later eliminated the plug flow behaviour and the reactor behaved similar to a single continuous stirred tank reactor. Chemical Engineering Research Bulletin 19(2017) 111-117
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