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Experimental Studies on Suspension of Solid Particles in a Low-Shear Stirred Vessel

机译:低剪切搅拌容器中固体颗粒悬浮的实验研究

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摘要

A low-shear stirred vessel was explored. Experimental studies on the suspension of solid particles in solid-liquid and gas-solid-liquid systems were conducted to examine the performance of this new reactor. The method based on the power number curve was modified to determine the critical impeller speeds required for just complete off-bottom suspension of solids under non-gassed (N_(js)) and gassed conditions (N_(jsg)) in this reactor, and a PC-6A fiber-optic probe for the measurement of solid distribution was used to complementarily validate this method. A more homogeneous flow field was gained with a draft tube installed, so that the standard deviations of average shear rate and maximal shear rate are reduced. The modified power consumption method can determine N_(js) and N_(jsg), and the values of N_(js) with a draft tube are much lower than those without it. N_(jsg) increases slightly with increasing gas flow rate, and N_(jsg) with a higher solid weight fraction is larger in this lower-shear reactor.
机译:探索了低剪切搅拌容器。对固体颗粒在固液和气固液体系中的悬浮液进行了实验研究,以检验该新型反应器的性能。修改了基于功率数曲线的方法,以确定在该反应器中,在未充气(N_(js))和充气条件(N_(jsg))下,固体完全从底下完全悬浮所需的临界叶轮速度,以及用于测量固体分布的PC-6A光纤探头用于补充验证该方法。安装引流管后,流场更加均匀,因此平均剪切速率和最大剪切速率的标准偏差减小了。修改后的功耗方法可以确定N_(js)和N_(jsg),带有引流管的N_(js)值比没有引流管的N_(js)低得多。 N_(jsg)随着气体流速的增加而略有增加,而固含量分数较高的N_(jsg)在该较低剪切反应器中较大。

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