Droplet size scaling in a turbulent pipeline flow

被引：1

作者：

Eskin, Dmitry ^{[1
]}

机构：

[1] Schlumberger DBR Technol Ctr, Edmonton, AB T6N 1M9, Canada

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 2015年 / 93卷 / 11期

关键词：

breakup regime; droplet size; modelling; pipeline; scaling; turbulence;

D O I：

10.1002/cjce.22286

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The changes of a droplet breakup regime at transition from an inertial to a viscous turbulence subrange are analyzed for pipe flow. Equations for evaluation of the maximum droplet size in both breakup regimes, as well as conditions for the breakup regime transition, are formulated as functions of the Reynolds and Weber numbers for a pipeline flow. Numerical values for the coefficients of the equations derived are estimated.

引用

页码：2051 / 2054

页数：4

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