MHD boundary layer flow and heat transfer of a nanofluid past a permeable stretching sheet with velocity, thermal and solutal
slip boundary conditions, Computer and Fluids 75: 1-10.
This is the reason why the viscosity decreases in the medium or the free stream velocity increases, and it results in the thermal and solutal
boundary layer thickness decrease.
Copper casting alloys are commonly divided into three groups based on their freezing range, which governs the degree of solutal
undercooling, associated dendritic growth, and tendency to form microporosity.
Themal and solutal
transport by fluid flowing through a porous matrix is a phenomenon of great interest from both the theory and application point of view.
Promotion of steam condensation heat transfer using solutal
Marangoni condensation Trans.
where Ec is the Eckert number, Pr is the Prandtl number, Sc is the Schmidt number, Sr is the Soret number, Du is the Dufour number, M is the Magnetic field parameter, Gr is the thermal Grashof number, Gc is the Solutal
Grashof number, k is the porous parameter, [b.
The dendritic in the melt zone can be either equiaxed or columnar depending on the solidification parameters, heat transfer, fluid flow, local thermal and solutal
4 where the Le value is big, the solutal
effect drives down the Hopf bifurcation.
Chang, "Hyperbolic Homogenized Models for Thermal and Solutal
Dispersion," SIAM J.
The surface-tension variation on the free liquid surface resulting from the temperature gradient or concentration gradient can induce motion within the fluid called thermocapillary flow or solutal
capillary flow (thermal Marangoni convection or solutal
The nondimensional parameters that govern the flow are the Prandtl number (Pr), which is inversely proportional to the thermal diffusivity of the working fluid, the Frank-Kamenetskii parameter ([lambda]), the Soret number (Sr), the magnetic parameter (M), the thermal Grashof number (Gr), the solutal
Grashof number (Gc), the nondimensional time (t), the Schmidt number (Sc), which is inversely proportional to the mass diffusivity of the working fluid, and suction/injection parameter (y), which were simultaneously applied each to opposite porous plates of the channel at the same rate.
5] investigated theoretically the problem of free convection boundary layer flow of nanofluids over a non-linear stretching sheet, incorporating the effects of buoyancy parameter, the solutal
buoyancy parameter and the power law velocity parameter.