Mass transfer of RAFM steel in Li by simple immersion, impeller induced flow and thermal convection

2011 ◽  
Vol 417 (1-3) ◽  
pp. 1200-1204 ◽  
Author(s):  
Masatoshi Kondo ◽  
Takeo Muroga ◽  
Takuya Nagasaka ◽  
Qi Xu ◽  
Valentyn Tsisar ◽  
...  
Author(s):  
V.V. Shekhovtsov ◽  
◽  
YU.A. Abzaev ◽  
O.G. Volokitin ◽  
A.A. Klopotov ◽  
...  

The paper presents the results of numerical modeling of development melting zone hollow spherical microparticle α-Al2O3. The object of the study was part circular sector, which represents the shell of hollow particle, which is formed under action plasma flow. Numerically describe the unsteady convective heat and mass transfer in shell hollow particle, we used the system Navier-Stokes equations in Boussinesq approximation, which describes the weak convection medium. Due to the high coefficient of porosity (P = 0.56) initial agglomerated particle with the α-Al2O3 structure, the inner region at the stage of heating Tp ≥ Tmelt is in the conditions heat exchange with the incoming heat flux, as result of which the temperature center coincided with the temperature particle surface. Result of overheating of the condensed phase, liquid layer of fused grains is formed in the inner and outer regions microparticle. In this case, the melting front is directed towards center shell. Result of numerical modeling, it has been established that convective heat and mass transfer is observed in melting zones (liquid phase), vector field of which covers almost the entire region of the liquid phase. It was found that thermal convection in the external liquid phase is characterized by velocities that are more than 2 times higher than the displacement velocity in the inner region of the particle. It is shown that there is no displacement of the material inside the convection region, thereby inhomogeneous heating occurs in the molten layer of the particle, which significantly affects the speed of movement of the melting front.


2017 ◽  
Vol 72 (2) ◽  
pp. 107-125 ◽  
Author(s):  
F. Moukalled ◽  
J. Kasamani ◽  
M. Darwish ◽  
A. Hammoud ◽  
M. Khamis Mansour

CORROSION ◽  
1965 ◽  
Vol 21 (2) ◽  
pp. 57-61 ◽  
Author(s):  
JAMES Y. N. WANG

Abstract Mass transfer of nickel to the hot leg (454 C, 850 F) of a mercury thermal convection loop in which titanium samples were exposed has been observed. This involved dissolution of nickel in mercury at 320 C (608 F), its transfer to the surface of the sample in the hot leg, and subsequent interdiffusion of nickel and titanium. Microprobe study of surface layers on the titanium sample indicated stratification of nickel. Outer layer contained two materials with compositions closely approximating those of TiNi and TiNi3, and an inner layer a material with nickel content close to the reported solubility limit for nickel in β-Ti, even though the reaction was conducted below α-β transformation temperature. Effects of other metallic additives are also discussed.


2021 ◽  
Vol 127 (24) ◽  
Author(s):  
Yun-Bing Hu ◽  
Shi-Di Huang ◽  
Yi-Chao Xie ◽  
Ke-Qing Xia

2017 ◽  
Vol 27 (6) ◽  
pp. 1282-1303 ◽  
Author(s):  
M.M. Rahman ◽  
Sourav Saha ◽  
Satyajit Mojumder ◽  
Khan Md. Rabbi ◽  
Hasnah Hasan ◽  
...  

Purpose The purpose of this investigation is to determine the nature of the flow field, temperature distribution and heat and mass transfer in a triangular solar collector enclosure with a corrugated bottom wall in the unsteady condition numerically. Design/methodology/approach Non-linear governing partial differential equations (i.e. mass, momentum, energy and concentration equations) are transformed into a system of integral equations by applying the Galerkin weighted residual method. The integration involved in each of these terms is performed using Gauss’ quadrature method. The resulting non-linear algebraic equations are modified by the imposition of boundary conditions. Finally, Newton’s method is used to modify non-linear equations into the linear algebraic equations. Findings Both the buoyancy ratio and thermal Rayleigh number play an important role in controlling the mode of heat transfer and mass transfer. Originality/value Calculations are performed for various thermal Rayleigh numbers, buoyancy ratios and time periods. For each specific condition, streamline contours, isotherm contours and iso-concentration contours are obtained, and the variation in the overall Nusselt and Sherwood numbers is identified for different parameter combinations.


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