Effect of Tank Diameter on Solid Suspension in Industrial Reactor Vessels

IF 17.7 1区 化学 Q1 CHEMISTRY, MULTIDISCIPLINARY Accounts of Chemical Research Pub Date : 2024-06-01 DOI:10.47176/jafm.17.6.2273
D. K. Iyer, †. A.K.Patel
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Abstract

Present research study analyses the suitability of baffled reactor vessels with large diameter agitated using the Rushton Turbine (RT) impeller maintained at standard clearance condition for the solid-liquid suspension process. The mean and turbulent flow fields associated with reactor vessels of various diameter were simulated using Computational Fluid Dynamics (CFD) approach. The impeller rotation was modelled using Multiple Reference Frame (MRF) technique and entrainment of air was simulated using Volume of Fluid (VOF) method respectively. The increase in the diameter of reactor vessel keeping impeller at standard clearance condition lead to the transition from double to single loop pattern with considerable decrease in the power number. In large reactor vessels, a low pressure zone is developed below the impeller which deflects the discharge streams and trailing vortices towards bottom surface of the reactor vessel causing the formation of single loop down-pumping pattern. The downward propagation of trailing vortices weaken the flow separation region behind the impeller blades which in turn decreases the form drag and power number of the impeller. The development of single loop down-pumping pattern, high magnitudes of axial velocity, vortex and turbulence fields near vessel bottom and inferior entrainment of air makes the large reactor vessels suitable for the solid-liquid suspension process. The high magnitudes of axial velocity developed below the impeller of large reactor vessel with same power consumption as compared to low clearance vessel makes the former vessel configuration more suitable for the solid-liquid suspension process.
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罐体直径对工业反应釜中固体悬浮物的影响
本研究分析了使用保持在标准间隙条件下的拉什顿涡轮(RT)叶轮搅拌的大直径障板反应器在固液悬浮过程中的适用性。采用计算流体动力学(CFD)方法模拟了与不同直径反应器相关的平均流场和湍流场。叶轮旋转采用多参考框架(MRF)技术建模,空气夹带则分别采用流体体积(VOF)方法模拟。在叶轮保持标准间隙的条件下,反应容器直径的增加导致从双回路模式过渡到单回路模式,功率数大幅下降。在大型反应器容器中,叶轮下方会形成一个低压区,使排出的气流和尾流漩涡向反应器容器底面偏转,从而形成单回路下泵模式。尾流涡旋的向下传播削弱了叶轮叶片后的流动分离区,进而降低了叶轮的形式阻力和功率数。单回路向下泵送模式的发展、容器底部附近的高轴向速度、涡旋和湍流场以及较低的空气夹带使得大型反应器容器适合固液悬浮工艺。与低间隙容器相比,大型反应器叶轮下方产生的轴向流速较高,但功耗相同,因此前者更适合固液悬浮工艺。
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来源期刊
Accounts of Chemical Research
Accounts of Chemical Research 化学-化学综合
CiteScore
31.40
自引率
1.10%
发文量
312
审稿时长
2 months
期刊介绍: Accounts of Chemical Research presents short, concise and critical articles offering easy-to-read overviews of basic research and applications in all areas of chemistry and biochemistry. These short reviews focus on research from the author’s own laboratory and are designed to teach the reader about a research project. In addition, Accounts of Chemical Research publishes commentaries that give an informed opinion on a current research problem. Special Issues online are devoted to a single topic of unusual activity and significance. Accounts of Chemical Research replaces the traditional article abstract with an article "Conspectus." These entries synopsize the research affording the reader a closer look at the content and significance of an article. Through this provision of a more detailed description of the article contents, the Conspectus enhances the article's discoverability by search engines and the exposure for the research.
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