𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Two-phase flow — III. Interfacial area in cocurrent gas—liquid flow

✍ Scribed by G. Kasturi; J.B. Stepanek

Publisher
Elsevier Science
Year
1974
Tongue
English
Weight
570 KB
Volume
29
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.

✦ Synopsis

Specific interfacial areas for cocurrent gas-liquid flow through a vertical tube 6 mm i.d. and 1524 mm long have been obtained by absorbing carbon dioxide from air into aqueous sodium hydroxide. The interfacial area was found to increase with the liquid flow rate but a maximum was observed on the interfacial area vs gas flow rate curves. The position of the maximum is virtually independent of the liquid flow rate. A correlation is presented in terms of the rate of creation of the interfacial area V,,a& against the pressure drop.

📜 SIMILAR VOLUMES

Interfacial area in cocurrent gas—liquid
Interfacial area in cocurrent gas—liquid upward flow in tubes of various size
✍ R.V. Shilimkan; J.B. Stepanek 📂 Article 📅 1977 🏛 Elsevier Science 🌐 English ⚖ 541 KB

Abstra&-Interfacxal area was measured for the case of cocurrent gas-hqmd upward flow u1 tubes 10,lS and 20 mm I d using the tecbruque of absorption w~tb fast chermcal reaction of carbon dloxlde into 1 N aqueous solution of sodmm hydromde Measured data on pressure drop and void fration are also repor

Two-phase gas-liquid flow
Two-phase gas-liquid flow
✍ J.J.J. Chen 📂 Article 📅 1985 🏛 Elsevier Science 🌐 English ⚖ 130 KB

Heat Mass Transfer 10 1767-l 778. Hewitt G. F. and Roberts D. N., 1969, Studies of two phase flow patterns by simultaneous X-ray and flash photograph. AERE Report M2 159. Taitel Y., Barnea D. and Dukler A. E., 1980, Modelling flow pattern transition for steady upward gas-liquid flow in vertical tube

Cocurrent gas—liquid flow in packed colu
Cocurrent gas—liquid flow in packed columns
✍ B.E.T. Hutton; L.S. Leung 📂 Article 📅 1974 🏛 Elsevier Science 🌐 English ⚖ 396 KB

A model is proposed for cocurrent gas liquid flow through a packed bed. For a given packing, gas and liquid flow rates, we proposed that (i) liquid holdup is a function only of pressure gradient and liquid flow rate and (ii) pressure gradient is only a function of liquid holdup and gas flow rate. Eq