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Sav [38]
4 years ago
9

A rotating cup viscometer has an inner cylinder diameter of 2.00 in., and the gap between cups is 0.2 in. The inner cylinder len

gth is 2.50 in. The viscometer is used to obtain viscosity data on a Newtonian liquid. When the inner cylinder rotates at 10 rev/min, the torque on the inner cylinder is measured to be 0.00011 in-lbf. Calculate the viscosity of the fluid. If the fluid density is 850 kg/m^3, calculate the kinematic viscosity
Engineering
1 answer:
Lesechka [4]4 years ago
4 0

Answer:

The dynamic viscosity and kinematic viscosity are 1.3374\times 10^{-6} lb-s/in2 and 1.4012\times 10^{-3} in2/s.

Explanation:

Step1

Given:

Inner diameter is 2.00 in.

Gap between cups is 0.2 in.

Length of the cylinder is 2.5 in.

Rotation of cylinder is 10 rev/min.

Torque is 0.00011 in-lbf.

Density of the fluid is 850 kg/m3 or 0.00095444 slog/in³.

Step2

Calculation:

Tangential force is calculated as follows:

T= Fr

0.00011 = F\times(\frac{2}{2})

F = 0.00011 lb.

Step3

Tangential velocity is calculated as follows:

V=\omega r

V=(\frac{2\pi N}{60})r

V=(\frac{2\pi \times10}{60})\times1

V=1.0472 in/s.

Step4

Apply Newton’s law of viscosity for dynamic viscosity as follows:

F=\mu A\frac{V}{y}

F=\mu (\pi dl)\frac{V}{y}

0.00011=\mu (\pi\times2\times2.5)\frac{1.0472}{0.2}

\mu =1.3374\times 10^{-6}lb-s/in².

Step5  

Kinematic viscosity is calculated as follows:

\upsilon=\frac{\mu}{\rho}

\upsilon=\frac{1.3374\times 10^{-6}}{0.00095444}

\upsilon=1.4012\times 10^{-3} in2/s.

Thus, the dynamic viscosity and kinematic viscosity are 1.3374\times 10^{-6} lb-s/in2 and 1.4012\times 10^{-3} in2/s.

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A rectangular beam having b=300 mm and d=575 mm, spans 5.5 m face to face of simple supports. It is reinforced for flexure with
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Answer:

provide 180 mm spacing

Explanation:

GIVEN DATA

rectangular beam: (b) = 300 mm, (d) = 575 mm

reinforced for flexure = 4Ф32 bars

WD = 30 kN /m,  WL = 45 kN/m

Wu = 1.4 * 30 + 1.6 * 45 = 114 kN/m

i) concrete shear stress ( vc)

100 Ac / bd = (100 * u * \frac{\pi }{4} *  32^2) / 300 * 575 = 1.865

from table 3.8

when:  100 Ac / bd = 1.865  then Vc = 0.778 N/mm^2

Ultimate shear force = (114 *5.5) / 2 = 313.5 kN

design shear stress =  V / bd = (313.5 * 10^3) / (300 * 575) = 1.82 N/mm^2

v < 0.8\sqrt{22}   =      1.82 < 3.75

design link provided  according to

Asv / sv =  b(v-vc) / 0.87 fy  = 300(1.82 - 0.778) / 0.87 (420)

ASv / Sv = 0.855

From table 3.13 :the value of Asv / sv can be calculated as

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The velocity distribution for laminar flow between parallel plates is given by u umax = 1 − ( 2y h ) 2 Where h is the distance s
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4 years ago
Sea water with a density of 1025 kg/m3 flows steadily through a pump at 0.21 m3 /s. The pump inlet is 0.25 m in diameter. At the
myrzilka [38]

Answer:

\dot W_{pump} = 16264.922\,W\,(16.265\,kW)

Explanation:

The pump is modelled after applying Principle of Energy Conservation, whose form is:

\frac{P_{1}}{\rho\cdot g}+ \frac{v_{1}^{2}}{2\cdot g} +z_{1} + h_{pump}=\frac{P_{2}}{\rho\cdot g}+ \frac{v_{2}^{2}}{2\cdot g} +z_{2}

The head associated with the pump is cleared:

h_{pump} = \frac{P_{2}-P_{1}}{\rho\cdot g}+\frac{v_{2}^{2}-v_{1}^{2}}{2\cdot g}+(z_{2}-z_{1})

Inlet and outlet velocities are found:

v_{1} = \frac{0.21\,\frac{m^{3}}{s} }{\frac{\pi}{4}\cdot (0.25\,m)^{2} }

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