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It is also found that the boundary layer thickness for second solution is higher than first solution for the three types of nanofluids for shrinking sheet.
β denotes the ratio of the square of two lengths, the classical boundary layer thickness for a high Reynolds number flow D/ 2Re1/2D) and the fiber-interaction layer thickness K1/2.
Thus, the velocity boundary layer thickness for the Casson fluid is larger than the Newtonian fluid.
The boundary layer thickness for the first solution is always thinner than that for the second solution.
It is to be noted that momentum boundary layer thickness for the second solution is thicker than for the first solution.
Again, Figure 11(a) and (b) shows that as the Soret number increases, the boundary layer thickness for the solute concentration reduces.
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The effects of gap to diameter ratio, Reynolds number and flat seabed roughness for a given boundary layer thickness of the inlet flow upstream of the cylinder have been investigated.
The diffusive boundary layer thickness of ∼0.2 mm in stirred solution was considered for accurate quantification of concentration.
Scaling rules are presented for the thermal and concentration boundary layer thickness, and for the concentration and uniformity of reactant, intermediates and byproducts.
The momentum boundary layer thickness increased for the case of the first solution, while an opposite phenomenon appeared for the second solution and a similar phenomenon was observed for concentration profile.
From the boundary condition, it is clear that the velocity at the surface is equal to λ; and so with increase in λ, the momentum boundary layer thickness increases for the case of the first solution, while an opposite phenomenon appears for the second solution which concurs with the results reported by Bhattacharyya et al. [38].
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