i)
ii)
b) i)
A thin-walled concentric tube heat exchanger has a uniform overall heat transfer
coefficient, and operates under the following conditions in Table 1.
ii)
Cold fluid
Hot fluid
Mass flow Specific heat
rate
[kg-s¹]
capacity
[J-kg-¹-K¹]
3850
1900
Inlet
Outlet
temperature temperature
[°C]
[°C]
0.2
0.25
Table 1: Heat exchanger conditions for question 2a.
25
240
110
Calculate the maximum possible heat transfer rate between the fluids,
describing fully the assumptions you must make.
[7 marks]
Calculate the hot outlet temperature, assuming the heat exchanger operates in
the mode that maximises the heat transfer rate.
[5 marks]
Write a chemical equation for the complete combustion of 1 kmol of cetane
(C16H34) in air assuming stoichiometric conditions. Take air to be 79%
nitrogen and 21% oxygen by volume.
Substance
Carbon Dioxide
Water
Oxygen
Pentane
5 kilomoles of pentane (CsH12) are burned completely in pure oxygen under
stoichiometric conditions with temperature and pressure being constantly
maintained at standard conditions of 25°C and 105 Pa respectively. Calculate
how much energy is available for external heating.
Enthalpies of formation are available in Table 2 and you may take the
chemical equation for the combustion of pentane to be
C5H12 +80₂5 CO₂ + 6H₂0
Enthalpy of Formation [kJ.kmol ¹]
-393,522
[5 marks]
-241,827
0
-146,800
Table 2: Enthalpy values for question 2b.
[8 marks]
Fig: 1