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ahrayia [7]
3 years ago
14

A closed system undergoes an adiabatic process during which the work transfer into the system is 12 kJ. The system then returns

to its original state via a non-adiabatic process during which the work transfer out of the system is 5 kJ. What is the magnitude and direction of the heat transfer for the second process?
Engineering
1 answer:
Harrizon [31]3 years ago
3 0

Answer:

Q= - 7 KJ

Heat is rejected

Explanation:

In first process:

Process is adiabatic so heat transfer will be zero.

Q= 0 For adiabatic process

Now from first law of thermodynamics

Q = ΔU + W

ΔU is the change in internal energy

Q is the heat transfer

W is the work.

So here Q= 0

And work is transfer to the system .It means that work done on the system so it will be taken as negative.

 W= - 12 KJ

Q = ΔU + W

0 = ΔU -12

ΔU = 12 KJ

It means that in first process internal energy of system  increase.

In second process:

non-adiabatic process and work done by system is 5 KJ.

Q = ΔU + W

U is the point function and it does not depends on the path follows it depends only on final and initial states.

So fro second process

ΔU  = - 12 KJ

Q= -12 + 5

Q= - 7 KJ

In magnitude Q= 7 KJ

It mean that heat is rejected from the system because it give negative sign.

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Calculate the convective heat-transfer coefficient for water flowing in a round pipe with an inner diameter of 3.0 cm. The water
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Answer:

h = 10,349.06 W/m^2 K

Explanation:

Given data:

Inner diameter = 3.0 cm

flow rate  = 2 L/s

water temperature 30 degree celcius

Q = A\times V

2\times 10^{-3} m^3 = \frac{\pi}{4} \times (3\times 10^{-2})^2 \times velocity

V = \frac{20\times 4}{9\times \pi} = 2.83 m/s

Re = \frac{\rho\times V\times D}{\mu}

at 30 degree celcius = \mu = 0.798\times 10^{-3}Pa-s , K  = 0.6154

Re = \frac{10^3\times 2.83\times 3\times 10^{-2}}{0.798\times 10^{-3}}

Re = 106390

So ,this is turbulent flow

Nu = \frac{hL}{k} = 0.0029\times Re^{0.8}\times Pr^{0.3}

Pr= \frac{\mu Cp}{K} = \frac{0.798\times 10^{-3} \times 4180}{0.615} = 5.419

\frac{h\times 0.03}{0.615}  = 0.0029\times (1.061\times 10^5)^{0.8}\times 5.419^{0.3}

SOLVING FOR H

WE GET

h = 10,349.06 W/m^2 K

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