Answer:
Vgr = 0.122 = 12.2 vol %
Explanation:
Density of ferrite = 7.9 g/cm^3
Density of graphite = 2.3 g/cm^3
<u>compute the volume percent of graphite </u>
for a 3.9 wt% cast Iron
W∝ = (100 - 3.9) / ( 100 -0 ) = 0.961
Wgr = ( 3.9 - 0 ) / ( 100 - 0 ) = 0.039
Next convert the weight fraction to volume fraction using the equation attached below
Vgr = 0.122 = 12.2 vol %
Answer:
B a lever because it can move up and down
Explanation:
Answer:
The effective stress is 225.6 kN/m²
The total vertical stress is 338.4 kN/m²
Explanation:
Given;
depth of soil surface = 6m
weight unit of the soil samples = 18.8 kN/m³
Stress = force/area
Stress = unit weight x depth
Effective stress at a depth of 12 m below the soil surface:
= (18.8 kN/m³) x (12 m)
= 225.6 kN/m²
Effective stress = 225.6 kN/m²
Total vertical stress at a depth of 12 m below the soil surface:
= (18.8 kN/m³) x (6 m) + (18.8 kN/m³) x (12 m)
= 112.8 kN/m² + 225.6 kN/m²
= 338.4 kN/m²
Total vertical stress = 338.4 kN/m²
Answer:
The fluid property responsible for the development of velocity boundary layer is majorly the fluid's viscosity.
For non-viscous fluids (in theory, because no fluid is entirely non-viscous), there will be no velocity boundary layer.
Explanation:
The velocity boundary layer is the thin layer of viscous fluid that is in direct contact with the pipe surface. The velocity of fluid in this layer is 0 as fluid doesn't move in this layer.
This phenomenon is due to the viscosity of the fluid. Viscosity of the fluid refers to the internal friction that exists between fluid layers, so, the layer of fluid in contact with non-moving, static surface of the pipe experiences friction that causes this layer to not move, causing the fluid velocity to vary from 0 at this surface to the maximum value at the centre of the pipe, before the velocity begins to drop again until it reaches 0 at the other end of the circular pipe.
Since viscosity is the primary cause of this, non-viscous or inviscid fluids are saved from this phenomenon as their flows do not have the velocity boundary layer.
Although, a completely non-viscous or inciscid fluid is an idealized concept because all fluids will experience some sort of viscosity (no matter how small) between their fluid layers. Hence, a velocity boundary layer, no matter how thin (or of minute thickness), will exist in the flow of real fluids.
But, an idealized non-viscous or inviscid fluid will not have a velocity boundary layer.
Hope this Helps!!!