SCHOOL of ENGINEERING               UNIVERSITY of PLYMOUTH                                   

 

BENG1   INTRODUCTION to THERMO-FLUIDS (THER 103)

 

TUTORIAL EXAMPLES in FIRST LAW CLOSED SYSTEMS (2)

 

(SSL conditions are 101.325 kPa, and 15°C)

 

1.              0.05 kg of CO2, molar mass 44 kg/kmol, occupying a volume of 0.03 m3 at 102.5 kPa is compressed reversibly until the pressure is 615 kPa.  Calculate the initial temperature, and the final temperature and work transfer:

(a) when the process is according to the law pV1.31 = constant;

(b) when the process is isothermal.

Assume CO2 to be a perfect gas. The Universal Gas Constant is 8.3143 kJ/kmol K.

[325.46 K; (a) 224.33 K; 5.24 kJ; (b) 325.46 K; 5.51 kJ]

 

2.              A quantity of gas occupying 0.14 m3 at a pressure of 1.4 MPa and temperature of 300°C is expanded adiabatically to 280 kPa.  If, for this gas, CV = 0.74 kJ/kgK and CP = 1.04 kJ/kgK, determine:

(a) the mass of the gas;

(b) the temperature of the gas after expansion;

(c) the work done during the expansion.          [1.14 kg;  360.2 K;  -179.56 kJ]

 

3.              A quantity of CO2, initially occupying 0.10 m3 at pressure 101.3 kPa and temperature 27°C is compressed according to the law pVn =  constant, until it occupies 0.02 m3 at a pressure of 620kPa.  Determine:

(a) the value of ‘n’;

(b) the change of internal energy of the system;

(c) the heat transfer to/from the system;

For CO2: CV = 0.737 kJ/kgK.  R = 0.189 kJ/kgK.        [n = 1.1256; 8.852 kJ; -9.22 kJ]

 

4.              A certain gas occupies 4 m3 at 110 kPa and 20°C.  It is compressed adiabatically in a closed system to a pressure of 690 kPa.  Determine:

(a) the final temperature

(b) the final volume

(c) the change in internal energy of the gas.

 

The density of the gas is 1.39 kg/m3 at 101.3 kPa and 0°C, and the specific heat capacity at constant volume is 0.732 kJ/kgK.              [478.6K, 1.042 m3, 764.3 kJ]

 

5.              Air at SSL conditions is compressed to a pressure of 900 kPa before it is delivered to a reservoir. If the compression process follows a law pV1.27 = constant determine:

(a) the specific work transferred to the air during the compression process;

(b) the temperature of the delivered air;

(c) the heat transfer/kg of air delivered.       [180.91 kJ/kg; 458.2 K; -58.37 kJ/kg]