首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Surface aerators - Power number, mass transfer coefficient, gas hold up profiles and flow patterns
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Surface aerators - Power number, mass transfer coefficient, gas hold up profiles and flow patterns

机译:表面曝气机-功率数,传质系数,气体滞留曲线和流型

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Mass transfer coefficient (k(L)a) and Power Number (N-p) have been measured in three flat-bottomed cylindrical acrylic tanks of 0.5, 1.0 and 1.5 m diameter. Three different impeller designs were employed [viz. pitched blade upflow turbine (PBTU), pitched blade downflow turbine (PBTD) and disc turbine (DT)]. Measurements have been made at two submergence levels of 0.23D and 0.3D. The power consumption per unit volume (P/V) was varied in the range of 10-250 W m(-3) which is normally employed in surface aeration applications. It is observed that at given submergence the power number is independent of the off bottom clearance and the power number changes with submergence. In case of PBTD and DT the dependence is higher as compared to PBTU. It has also been observed that the gas hold-up distribution significantly changes with the impeller design, submergence and the rotation speed. Gamma ray attenuation technique has been employed for the measurement of gas hold-up distribution for all the three impellers and its influence on the power number behaviour has also been discussed. In addition, the axial velocity measurements have been carried out for all the three types of impellers under surface aeration conditions for 0.5 m diameter tank with Ultrasound Doppler velocimeter. The validation of the measurement technique has also been done with the help of Laser Doppler Anemometer (LDA) measurements as well as with the CFD code. The velocity profile depends on the inherent gas hold-up in the impeller region, which in turn is governed by the impeller design, submergence and rotational speed. An attempt has also been made to shed some light on the interdependence of mass transfer coefficient, power number, gas hold-up and flow pattern. Finally the correlations have been proposed for the estimation of power number and mass transfer coefficient independently for each type of impeller, which are expected to be useful to practicing engineers.
机译:在三个直径为0.5、1.0和1.5 m的平底圆柱形丙烯酸储罐中测量了传质系数(k(L)a)和功率数(N-p)。采用了三种不同的叶轮设计[即。变桨叶向上流动涡轮(PBTU),变桨叶向下流动涡轮(PBTD)和盘式涡轮(DT)]。在0.23D和0.3D的两个浸没水平下进行了测量。每单位体积的功耗(P / V)在10-250 W m(-3)的范围内变化,通常在表面曝气应用中使用。可以看出,在给定的浸入状态下,功率数与离底间隙无关,并且功率数随浸入而变化。对于PBTD和DT,与PBTU相比,依赖性更高。还已经观察到,气体滞留量的分布会随着叶轮的设计,浸入和转速的变化而显着变化。伽马射线衰减技术已用于测量所有三个叶轮的气体滞留量分布,并且还讨论了其对功率数行为的影响。此外,还使用超声多普勒测速仪对直径为0.5 m的储罐在表面曝气条件下对所有三种叶轮进行了轴向速度测量。借助激光多普勒风速计(LDA)测量以及CFD代码也可以完成对测量技术的验证。速度曲线取决于叶轮区域内的固有气体滞留量,而气体滞留量又取决于叶轮的设计,浸入量和转速。还试图阐明传质系数,功率数,气体滞留率和流动模式之间的相互关系。最后,提出了相关性,以分别估算每种叶轮的功率数和传质系数,这对实践工程师很有用。

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