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Gnesinka [82]
2 years ago
13

A mass hanging from a spring is set in motion and its ensuing velocity is given by v (t )equals 2 pi cosine pi t for tgreater th

an or equals 0. Assume that the positive direction is upward and ​s(0)equals 0.

Physics
1 answer:
lianna [129]2 years ago
7 0

Answer:

2(maximum), -2(minimum), -2(maximum).

Explanation:

V(t)= 2πcos πt--------------------------------------------------------------------------------(1).

Therefore, there is a need to integrate v(t) to get S(t).

S(t)= 2×sinπt + C ------------------------------------------------------------------------------(2).

Applying the condition given, we have s(0)= 0.

S(0)= 2sin ×π(0) + C.

Which means that; 0+C= 0. That is; C=0.

S(t)= 2 sin πt.

The mass moves to its highest positions at time,t=half(1/2=.5) and time,t=2.5.

Take note that;  sin(π/2) = sin(5π/2) = 1 .

Also, the mass moves to its lowest position at time,t=(3/2); also, sin(3π/2) = -1.

Therefore, we have that 2 maximum; -2 minimum and -2 maximum.

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Here is the full question.

Saturated ethylene glycol at 1 atm is heated by a chromium-plated surface which is circular in shape and has a diameter of 200-mm and is maintained at 480 K.  

At 470 K the properties of the saturated liquid are mu = 0.38 * 10-3 N. s/m^2, Cp = 3280 J/kg. K and Pr = 8.7. The saturated vapour density is p= 1.66 kg/m^3. Take the liquid to surface constants to be Cnb = 0.010 and m=4.1.  

Estimate the heating power requirement and the rate of evaporation  

What fraction is the power requirement of the maximum power associated with the critical heat flux

Answer:

The heating power requirement = 559.2 W

The rate of evaporation = 6.89*10^{-4}kg/s

The fraction of the power requirement  of operating heat flux to the maximum power associated with the critical heat flux is = 0.026

Explanation:

From the thermodynamics tables; we deduced the value for enthalpy at the pressure 1 atm and T_{sat} = 470 K   for the saturated ethylene glycol.

Value for enthalpy of formation h_{fg} = 812 kJ/kg

Density of saturated ethylene glycol \rho___l = 1111 kg/m³

Surface tension \sigma = 32.7*10^{-3}N/m

The heat flux can be calculated by using the formula:

q"s = \mu___l}}}h_{fg}{[\frac{g(\rho{__l}- \rho{__v} }{\sigma} ]^{1/2}  [\frac{C_p*\delta T_c}{C_{sf}*h_{fg}P_r} ]^3

= [0.38*10^{-3}\frac{NS}{m^2} *812*10^3\frac{J}{kg} (\frac{9.81m/s^2*(1111-1.66)kg/m^3}{32.7*10^{-3}N/m} )^{1/2}*(\frac{3280J/kg.K(480-470)K}{0.01*812*10^3\frac{J}{kg}*(8.7)^1 } )]

= 308.56 × 576.6 × 0.1

= 1.78 × 10⁴ W/m²

Now; to find the heating power requirement; we have:

q_{boil} = q__s }*A S

= 1.78*10^4 \frac{W}{m^2}*(\frac{\pi}{4}*(0.2m))^2

Thus, the heating power requirement = 559.2 W

The rate of evaporation is given as:

m= \frac{q_{boil}}{h_[fg}}

= \frac{559.2}{812*10^3}

= 6.89*10^{-4}kg/s

Thus, the rate of evaporation = 6.89*10^{-4}kg/s

To determine to what fraction in the power requirement of the maximum power is associated with the critical total flux ; we needed to first calculate the critical heat flux.

So, the  calculation for the critical heat is given as:q"max = 0.149*h_{fg}}* \rho{___l}}}}[ \frac{\sigma_g (\rho_l - \rho_v}{\rho_v^2} ]^{1/4}

= q"max = 0.149*812810^3* 1.66[ \frac{32.7*10^{-3}*9.8 (1111- 1.66}{1.66^2} ]^{1/4}

= 200840.08 × 3.37

= 6.77 × 10⁵ W/m²

Finally, the fraction of the power requirement  of operating heat flux to the maximum power associated with the critical heat flux is as follows:

= \frac{q''s}{q''max}

= \frac{1.78*10^4}{6.77*10^5}

= 0.026

Thus, the fraction of the power requirement  of operating heat flux to the maximum power associated with the critical heat flux is = 0.026

7 0
3 years ago
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