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Journal ArticleDOI

Mass Transfer to Single Spheres

Kazuo Sato, +1 more
- 01 Jan 1958 - 
- Vol. 22, Iss: 2, pp 76-81
TLDR
In this article, the rate of mass transfer to single spheres, with the aid of a diffusion-controlled electrode reaction, was studied. But it was found that neither the results thus obtained nor those by previous investigators showed good agreement with the Ranz-Marshall's eq.
Abstract
Studies were made on the rate of mass transfer to single spheres, with the aid of a diffusioncontrolled electrode reaction:Microelectrodes used as anode were platinum spheres having 1.66mm and 2.74mm diameters respectively, each with PVC-coated platinum wire of 0.6mm diameter. The reference electrode used as cathode was a thin platinum plate of 50×120mm. The experimental apparatus employed was as shown in Fig. 1. To obtain uniform distribution of liquid velocity over the entire column cross-section, glass beads of 5mm diameter were packed to a height of 30mm, topped with 10 sheets of Saran screen of about 12 meshes. Below the packing and 8mm above the spherical electrode, a Saran screen of about 150 meshes was placed.From the measurements of limiting current 6), 8) at various liquid flow rates, the mass transfer coefficients, kf, were calculated by the equation:kf=i/nFAc (7)The experimental results are shown in Table 1. It was found that neither the results thus obtained nor those by previous investigators3), 9), 10), 14), 16) showed good agreements with the Ranz-Marshall's eq. (2)14).Thereupon, assuming that the empirical equation might be presented as:Sh-2=kRepScq (8)the authors determined the values of the constants k, p and q (Figs. 3, 4 and 5), obtaining an equation:Sh=2.0+0.52Re0.54Sc0.35 (9)The value of the exponent of the Schmidt group, 0.35, agrees well with 0.348 obtained by Frossling3) from his experimental data.

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Experimental and theoretical studies of the dynamics of startup and product switchover operations of distillation columns

TL;DR: In this paper, the authors have made experimental studies with the help of laboratory-scale distillation columns of the startup and product switchover operations of distillation column and showed that the time needed to reach steady state can be considerably reduced, and consequently the costs.
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CO2 quality control through scrubbing in oxy-fuel combustion: Simulations on the absorption rates of SO2 into droplets to identify operational pH regions

TL;DR: In this article, a theoretical model was developed based on the two-film mass transfer model, and considering both the SO2 and CO2 reactions with sodium solutions, and simulations focused on the impacts of droplet position, gas phase CO2 and droplet size on the absorption rate of SO2.
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Development and Experimental Verification of a Simulation Tool for Column Startup

TL;DR: In this paper, a simulation tool for column startup is developed based upon a mathematical model founded on the conservation laws, the equilibrium relationship as well as pressure, holdup and heat transfer correlations.
Journal ArticleDOI

Region of molecular diffusion controlling for film coefficient of mass transfer between particles and fluid in dilute packed beds

TL;DR: In this article, the authors measured the film coefficients of mass transfer for dilute packed beds of irregular (ef=0.392) or regular (ef =0.313) packing, applying the diffusion current method.
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