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A Novel Approach to Simplification of NPSH(r) CFD calculation

机译:简化NPSH(r)CFD计算的新方法

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Present work proposes approach that significantly shortens the calculation time for NPSH(r). This time is comparable with time for the head calculations. Most cavitation models take into account phase change, bubble dynamics, turbulent pressure fluctuations, etc. In this case multiphase flow model must be used. This work presents some simplifications, based on the physical nature of cavitation on the pump impeller, which significantly (10 -50 times) reduces the calculation time of NPSH (r). The main idea of proposed procedure is to determine the liquid vapor (cavitation) zone simply from steady state calculation of one phase incompressible flow without taking into account multiphase effects. Based on absolute pressure distribution it is easy to determine areas with absolute pressure lower then saturated liquid vapor pressure for given liquid conditions. Consequently it is possible to consider the steady state location of liquid vapor (cavitation) on the impeller vanes. So this zone may simply be expelled from the flow domain. For many pump related cases, these zones are very close to cavitation areas, and give main impact on the head of the pump. Commercial Fluent 12.1.4 code is used for calculations. Proposed procedure for NPSH(r) calculation is in good agreement with test data for different types of pumps and may be used as a tool to shorten a design process for new pumps.
机译:当前的工作提出了一种方法,可以大大缩短NPSH(r)的计算时间。此时间与水头计算时间相当。大多数空化模型都考虑了相变,气泡动力学,湍流压力波动等。在这种情况下,必须使用多相流模型。这项工作基于泵叶轮上气蚀的物理特性,进行了一些简化,这大大减少了(10 -50倍)NPSH(r)的计算时间。所提出程序的主要思想是简单地从一相不可压缩流的稳态计算中确定液体蒸气(气蚀)区域,而无需考虑多相效应。根据绝对压力分布,很容易确定绝对压力低于给定液体条件下的饱和液体蒸气压的区域。因此,可以考虑叶轮叶片上液体蒸汽(气蚀)的稳态位置。因此,可以将该区域简单地从流域中排除。对于许多与泵相关的情况,这些区域非常靠近气蚀区域,并且对泵的扬程产生主要影响。商业Fluent 12.1.4代码用于计算。提议的NPSH(r)计算程序与不同类型泵的测试数据非常吻合,可以用作缩短新泵设计过程的工具。

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