Slug flow was studied for air velocities less than 8 m/s with polyethylene pellets in a straight pipe 32 mm in diameter and 5.5 m in length, and was classified into 2 regimes: successive slug flow and solitary slug flow. A settled layer of particles did not form in the latter and high air pressure w
β¦ LIBER β¦
Estimating the solid particle velocity in horizontal pneumatic conveying lines
β Scribed by W-C. Yang; D. L. Keairns; D. H. Archer
- Book ID
- 112053392
- Publisher
- John Wiley and Sons
- Year
- 1973
- Tongue
- English
- Weight
- 249 KB
- Volume
- 51
- Category
- Article
- ISSN
- 0008-4034
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
Low-velocity pneumatic conveying of coar
β
Y. Tomita; H. Asou
π
Article
π
2009
π
Elsevier Science
π
English
β 881 KB
Particle velocity and concentration char
β
Hui Li; Yuji Tomita
π
Article
π
2000
π
Elsevier Science
π
English
β 760 KB
Low-velocity pneumatic conveying in hori
β
Yuji Tomita; Vijay Kumar Agarwal; Hiroyuki Asou; Katsuya Funatsu
π
Article
π
2008
π
Elsevier
π
English
β 398 KB
First, the characteristics of low-velocity conveying of particles having different hardness are experimentally investigated in a horizontal pipeline in terms of flow pattern and pressure drop to show that the slug flow can be classified into two types depending on the settling of particles along the
Flow frictional resistance in pneumatic
β
Melda Γ. Carpinlioglu; TΓΌlay A. Γzbelge; Vedat Oruc
π
Article
π
2002
π
Elsevier Science
π
English
β 164 KB
The influence of pipe geometry on the cr
β
K.-E. Wirth; O. Molerus
π
Article
π
1985
π
Elsevier Science
π
English
β 712 KB
97/03551 A model for the drying of wet s
π
Article
π
1997
π
Elsevier Science
β 201 KB