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Rashid [163]
3 years ago
7

A rigid copper tank, initially containing 1 m3 of air at 295 K, 5 bar, is connected by avalve to a large supply line carrying ai

r at 295 K, 15 bar. The valve is opened only as long as required tofill the tank with air to a pressure of 15 ,bar at which point the air in the tank is at 310 .K The copper tank,which has a mass of 20 ,kg is at the same temperature as the air in the tank, both initially and finally. Thespecific heat of the copper is c=0.385 kJ/kg K. Assuming ideal gas behavior for the air, determine:
(a) the initial and final mass of the air within the tank, each in kg, and
(b) the heat transfer to the surroundings from the tank and its contents, in kJ, ignoring kinetic and potential energy effects.
Engineering
1 answer:
asambeis [7]3 years ago
6 0

Answer:

Initial mass = 5.91 kg

Final mass = 16.8 kg

Heat transfer Q = - 625.9 KJ

Explanation:

Given data

Tank volume V = 1 m^{3}

Entering outside air temperature T_{i} = 295 K

Entering outside air pressure P_{i} = 15 bar

Initial tank pressure P_{1} = 5 bar

Initial tank temperature T_{1} = 295 K

Final pressure P_{2} = 15 bar

Final temperature T_{2} = 310 K

We know that

P V = m R T

(a). Initial mass is given by

m_{1} = \frac{P_{1} V_{1} }{R T_{1} }

Put all the values in given equation

m_{1} = \frac{(500000)(1)}{(287)(295)}  = 5.91 \ kg

(b). Final mass is given by

m_{2} = \frac{(1500000)(1)}{(287)(310)}

m_{2} = 16.8 \ kg

This is the final volume of the tank.

Δ U = Δ q + h_{i} Δ m_{cv}

m_{2} u_{2} - m_{1} u_{1} = Q + h_{i} (m_{2} - m_{1} )

Specific internal energy at initial temperature & pressure u_{1} = 210.5 \frac{KJ}{Kg}

Specific internal energy at final temperature & pressure u_{2} = 221.25 \frac{KJ}{Kg}

Specific enthalpy is h_{i} = 295.17  \frac{KJ}{Kg}

Q = ( 16.8 × 210.48 - 5.91 × 210.49 )- 295.17 ( 16.8 - 5.91 )

Q = 2292.23 - 3214.4

Q_{a} = - 741.4 KJ

The heat transfer for the tank is given by

Q_{t} = m C (T_{2} - T_{1})

Q_{t} = 20 × 0.385 × ( 310-295 )

Q_{t} = + 115.5 KJ

Total heat transfer Q = Q_{a} + Q_{t}

Q = - 741.4 + 115.5

Q = - 625.9 KJ

This is the heat transfer to the surrounding from the tank.

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