## Abstract Experimental data on flow pattern transitions, pressure drop, and flow characteristics for cocurrent gas–liquid flow through packed columns in microgravity is analyzed. The pulse flow regime exists over a wider range of gas and liquid flow rates under microgravity conditions. Furthermor
Liquid holdup in gas—liquid countercurrent flow through a bed of packing
✍ Scribed by Jiri Tichy
- Publisher
- Elsevier Science
- Year
- 1973
- Tongue
- English
- Weight
- 251 KB
- Volume
- 28
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
l/~*)~I~e-BR(l--~')]e~'~.
(I*) Ackmwkdgement-I am sincerely grateful to the referee of this paper for his invaluable comments which led to the improvement of the paper. I am also grateful to Prof. P. H. We observe here from (12) that the velocity still increases Calderbank, Department of Chemical Engineering, Uniwith time at a given point. For large values of /S?(comes-versity of Edinburgh for his interest in my work. uondina to lame values of afR*/v, since K is small) w is zherefoie effeczvely independent of r* except in a region near the wall (where (1r*) is small). Thus for small v/dR*, the flow of elastico-viscous fluids exhibits boundary layer characteristics. Conversely, when v/agR4 is large, the velocity is strongly dependent on position and there is no boundary layer. For K = 0, this problem reduces to that considered v,. by Sanyal(3) Proceeding as in Ref.
[4], we can show that the velocity Department ofMathematics V. M. SOUNDALGEKAR depends upon the distance from the wall and hence there Indian Institute of Technology is no boundary layer character in this case.
📜 SIMILAR VOLUMES
Step-function injection and purging of a dilute salt tracer in water was used to measure axial dispersion for low Reynolds number liquid flow through beds of uniform sized, random packed glass spheres. The resultant data and those of several previous studies are coordinated and interpreted in terms