FLOW OF SUSPENSIONS IN PIPELINES .2. 2 MECHANISMS OF PARTICLE SUSPENSION

被引:43
作者
SHOOK, CA
DANIEL, SM
SCOTT, JA
HOLGATE, JP
机构
[1] Department of Chemistry and Chemical Engineering, University of, Saskatoon, Saskatchewan
[2] Cambrian Engineering Limited, Saskatoon, Saskatchewan
[3] Shell of Canada Limited, Montreal, Quebec
关键词
D O I
10.1002/cjce.5450460405
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The distribution of sand and nickel particles with height in a horizontal channel of rectangular cross section has been measured and eddy diffusivities have been computed from these measurements. Turbulent suspension of particles appeared to occur where the concentration of solid particles was low, the particle diameter was small (< 0.2 mm.) and the ratio of the settling velocity of the particles to the friction velocity of the flow was less than 0.2. Where these criteria were not satisfied, concentration profiles were observed to deviate significantly from the shape associated with turbulent suspension. These deviations are attributed to the effect of particle interactions investigated by Bagnold. Copyright © 1968 Canadian Society for Chemical Engineering
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页码:238 / &
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