Gas hold-up and mass transfer in bubble columns with pseudoplastic liquids
✍ Scribed by G.Y. Vatai; M.N. Tekić
- Publisher
- Elsevier Science
- Year
- 1989
- Tongue
- English
- Weight
- 466 KB
- Volume
- 44
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
partial pressure of 0, in the plasma membrane Gupta, B. B. and Seshadri, V., 1977, Flow of red blood cell interface, mm Hg suspensions through narrow tubes. Biorheology 14, 133-143. average 0, partial pressure: mm Hg total flow rate, cm"/s flow rate in the core, cm'/s flow rate in the plasma layer, cm'/s initial saturation of O,, % saturation of 0, at the wall, % thickness of the membrane, cm Jayaraman. G., Lautier. A.. Bui-Mong Hung. J. G. and Laurent, D., 1981, A numerical scheme for modelling oxygen transfer in membrane oxygenators.
📜 SIMILAR VOLUMES
Experimental measurements of the gas hold-up and volumetric mass transfer coefficient have been made for bubble columns (BCs) treating various foaming liquids under mechanical and chemical foam control. The gas hold-up and the volumetric mass transfer coefficient in a mechanical foam-control system
Gas holdups and volumetric mass transfer coefficients (kLa) for oxygen were measured in suspensions of kieselguhr (7 pm), aluminium oxide (8 pm) and activated carbon (5 pm) in water or 0.8 molar sodium sulfate solution. By comparison to previously reported specific interfacial areas (a) determined b