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Hold-up prediction in packed columns for co-current gas—liquid downflow

✍ Scribed by J.P. Reynier; J.C. Charpentier

Publisher
Elsevier Science
Year
1971
Tongue
English
Weight
163 KB
Volume
26
Category
Article
ISSN
0009-2509

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✦ Synopsis

Shorter Communications many authors, and the equation is identical to that derived by Lochiel and Calderbank [5]. For mass transfer to spherical drops or bubbles at high Reynolds number, the analysis of Moore [6] and Cheh and Tobias [7] can be applied to derive 2+3/~a/tLc l'45]t/~/.___/bx.__XlJ2-1,2 ---i l l re '. Sho = 1.13 1 -1 + (Pa/xa~ v2 Rett2J \tzc + txa] (20) \pcIl~c/

📜 SIMILAR VOLUMES

Prediction of two-phase pressure drop an
Prediction of two-phase pressure drop and liquid holdup in co-current gas–liquid downflow of air–Newtonian systems through packed beds
✍ Ponnan Ettiyappan Jagadeesh Babu; Appusamy Arunagiri; Thanapalan Murugesan 📂 Article 📅 2005 🏛 Wiley (John Wiley & Sons) 🌐 English ⚖ 230 KB 👁 1 views

## Abstract The dependency of pressure drop and liquid holdup on phase velocities, geometry of the column and packing materials as well as on the physical properties have been analyzed. Our experimental data (825 data points obtained using four liquid systems and three different particles) along wi