✦ LIBER ✦

Pressure drop and film height measurements for annular gas-liquid flow

✍ Scribed by J.E. Laurinat; T.J. Hanratty; J.C. Dallman

Publisher: Elsevier Science
Year: 1984
Tongue: English
Weight: 816 KB
Volume: 10
Category: Article
ISSN: 0301-9322
DOI: 10.1016/0301-9322(84)90025-9

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Interfacial drag and film height for ver

Interfacial drag and film height for vertical annular flow

✍ J. C. Asali; T. J. Hanratty; Paolo Andreussi 📂 Article 📅 1985 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 733 KB

Film thichness, entrainment, and pressur

Film thichness, entrainment, and pressure drop in upward annular and dispersed flow

✍ G. A. Hughmark 📂 Article 📅 1973 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 387 KB 👁 2 views

Pressure drop and holdup in stratified g

Pressure drop and holdup in stratified gas-liquid flow

✍ T. W. F. Russell; A. W. Etchells; R. H. Jensen; P. J. Arruda 📂 Article 📅 1974 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 576 KB

Counter current gas-liquid vertical flow

Counter current gas-liquid vertical flow, model for flow pattern and pressure drop

✍ Yehuda Taitel; Dvora Barnea 📂 Article 📅 1983 🏛 Elsevier Science 🌐 English ⚖ 614 KB

The distribution of drop size and veloci

The distribution of drop size and velocity in gas-liquid annular flow

✍ Larry B. Fore; Abraham E. Dukler 📂 Article 📅 1995 🏛 Elsevier Science 🌐 English ⚖ 661 KB

A phenomenological model for pressure dr

A phenomenological model for pressure drop, liquid holdup, and flow regime transition in gas-liquid trickle flow

✍ R.A. Holub; M.P. Duduković; P.A. Ramachandran 📂 Article 📅 1992 🏛 Elsevier Science 🌐 English ⚖ 467 KB

## A phenomenological, pore-scale, hydrodynamic model is developed for representation of the uniform, two-phase, gas-liquid cocurrent flow in the low interaction regime in trickle bed reactors. The model provides improved predictions for both the pressure drop and liquid holdup using the parameters