...
首页> 外文期刊>Chemical Engineering Science >Friction factor-Reynolds number relationship for laminar flow of non-Newtonian fluids in open channels of different cross-sectional shapes
【24h】

Friction factor-Reynolds number relationship for laminar flow of non-Newtonian fluids in open channels of different cross-sectional shapes

机译:非牛顿流体层流在不同横截面形状下的摩擦系数-雷诺数关系

获取原文
获取原文并翻译 | 示例

摘要

The effect of channel shape on the friction factor-Reynolds number relationship for laminar, open channel flow of three non-Newtonian fluids was investigated. For each channel shape, the data can be described by a general relationship, f=K/Re where f is the Fanning friction factor and Re is the appropriate Haldenwang et al. (2002) Reynolds number corresponding to the flow curve model used to describe the non-Newtonian behaviour exhibited by the test fluid. The K values were found to be 14.6 for triangular channels with a vertex angle of 90 degrees, 16.2 for semi-circular channels, 16.4 for rectangular channels and 17.6 for trapezoidal channels with 60 degrees sides, These K values were found to be in line with those reported by Straub et al. (1958) and Chow (1959) for open channel flow of Newtonian fluids as opposed to the assumption made by Haldenwang et al. (2002, 2004) of using a constant value of 16 based on the pipe flow paradigm for all channel shapes. (C) 2010 Elsevier Ltd. All rights reserved.
机译:研究了三种非牛顿流体层流,明渠流动的通道形状对摩擦系数-雷诺数关系的影响。对于每个通道形状,数据可以通过以下一般关系来描述:f = K / Re,其中f是Fanning摩擦因数,Re是合适的Haldenwang等。 (2002)雷诺数对应于用于描述测试流体表现出的非牛顿行为的流动曲线模型。发现顶点角为90度的三角形通道的K值为14.6,半圆形通道的K值为16.2,矩形通道的K值为16.4,侧面为60度的梯形通道的K为17.6,发现这些K值与Straub等人报道的那些。 (1958)和Chow(1959)提出的牛顿流体的明渠流动与Haldenwang等人的假设相反。 (2002年,2004年)基于所有管道形状的管道流范式使用常数16。 (C)2010 Elsevier Ltd.保留所有权利。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号