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Solid-liquid mass transfer in falling liquid films on single spheres

TLDR
In this article, mass transfer equations were derived and compared with dissolution experiments of C6H5COOH-H2O and Cu-H 2SO4-K2Cr2O7 systems on single spheres (6 different sizes from 3/4" to 3").
Abstract
Mass transfer equations are derived and compared with dissolution experiments of C6H5COOH-H2O and Cu-H2SO4-K2Cr2O7 systems on single spheres (6 different sizes from 3/4" to 3"). In region I (long contact time with smooth laminar film), Sh converges Sh=1.608 (GaSc/Pe*)1/3 or k=2.01 D√δ(δ: mean film thickness) and increases with decreasing volumetric flow rate Q. In region II (short contact time with smooth laminar film), Sh converges Sh=0.716 Pe*1/9(GaSc)2/9The transition from region I to II occurs around Pe*/(GaSc)1/4≤10. In region III (short contact time with wavy film surface), Sh increases with Pe* to the 1/3 - 1/2 power and is substantially higher than that in region II. A generalized short contact time equation using the measured local film thickness δ Sh=0.501 Pe*1/3{∫π0(d/δ)sinθdθ}2/3is valid in this region. Thus, main cause for enhancement in Sh is the reduction in film thickness relevant to the wave formation. The II-III transition is somewhere between wave inception and wave coverage flow rates. In the above, Sh=kd/D, Pe*=Q/dD and Ga=gd3/v2, in which k is based on a log-mean driving force.

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Journal ArticleDOI

Radial mass-transfer enhancement in bubble-train flow ☆

TL;DR: In this paper, the effect of two-phase bubble-train flow on mass transfer between liquid and wall has been studied and a mathematical correlation for the Sherwood-number of the system is presented and the mechanism of transport enhancement is elucidated.
Journal ArticleDOI

Mixed convection in the copper dissolution technique of studying mass transfer.

TL;DR: In this article, the authors investigated the rate of mass transfer between the wall of a tube and a liquid flowing laminarly through the tube using the copper dissolution technique and revealed a significantly higher rate than predicted by the theoretical solution of the Graetz-Nusselt problem.
Journal ArticleDOI

Liquid-solid mass transfer in a rotating trickle-bed reactor: Mathematical modeling and experimental verification

TL;DR: In this paper, a mathematical model considering the wetting efficiency was first established to describe the liquid-solid mass transfer process in a rotating trickle-bed reactor (RTBR), which has great potential for process intensification of heterogeneous catalytic reactions.
Journal ArticleDOI

Hydrodynamics and mass transfer characteristics of co-current downflow packed tube columns

TL;DR: In this paper, the authors measured absorption and desorption of oxygen in different packed tube columns containing Pall rings (standard and low height to dia. ratio), multifilament wire gauge packings (MFWGP) and DPP.
Journal ArticleDOI

Diffusion controlled dissolution of metal powder in acidic solutions in stirred vessels

TL;DR: The rate of diffusion controlled dissolution of copper powder in acidified chromate solution under forced convection conditions was studied in this article, where rotational speed, initial concentration and physical properties of the acidic solution were investigated.
References
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Journal ArticleDOI

Mass Transfer into Liquid Film Flowing over Spheres

H. Hikita, +1 more
- 01 Jan 1959 - 
TL;DR: In this paper, experiments were performed on the absorption of pure carbon dioxide by water with and without a wetting agent, in columns containing 1, 3 and 5 spheres, respectively.
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