首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >PRESSURE DROP OF NEWTONIAN AND NON-NEWTONIAN FLUIDS ACROSS A SULZER SMX STATIC MIXER
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PRESSURE DROP OF NEWTONIAN AND NON-NEWTONIAN FLUIDS ACROSS A SULZER SMX STATIC MIXER

机译:舒尔兹SMX静态混合器上牛顿和非牛顿流体的压降

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This paper presents an experimental study of the pressure drop across a Sulzer SMX static mixer with both Newtonian and non-Newtonian fluids. The extensive experiments were performed under varying operating conditions: the fluid flowrate (2.78 x 10(-6) to 1.11 x 10(-4) m(3)s(-1)), the number of mixing elements aligned in series (6 to 18) and the wall temperature of the static mixer (293 to 363 K). It was found that adequate design correlations gathering perfectly all 397 experimental data points can be proposed over a wide range of a generalized Reynolds number: 0.08 less than or equal to Re-g less than or equal to 10000. These correlations compare favourably with previous work and extend significantly the investigated range of flow regimes. Finally, it was shown that the enhancement of fluid mixing is achieved by a pressure drop penalty up to 23 with respect to an empty tube. [References: 14]
机译:本文介绍了在具有牛顿流体和非牛顿流体的Sulzer SMX静态混合器上压降的实验研究。在不同的操作条件下进行了广泛的实验:流体流量(2.78 x 10(-6)至1.11 x 10(-4)m(3)s(-1)),混合元件的数量串联排列(6至18)和静态混合器的壁温(293至363 K)。已经发现,可以在广泛的广义雷诺数范围内提出适当地收集所有397个实验数据点的适当设计相关性:0.08小于或等于Re-g小于或等于10000。这些相关性与以前的工作相比具有优势。并大大扩展了流态研究范围。最后,显示出通过相对于空管高达23的压降损失来实现流体混合的增强。 [参考:14]

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