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an internal heat exchanger (IHE) needed to be included in the system. They found that unlike pure fluids, isentropic zeotropic mixtures showed the lowest Rankine cycle efficiency. Their investigation also showed that an increase in thermal efficiency could be achieved by combining superheating with an IHE. Mago et al. (2008) compared the performance of a regenerative ORC and a simple ORC system using four different dry organic fluids. They found that for each working fluid, the regenerative ORC showed a better thermal efficiency than the simple ORC. Their first and second law analysis also showed that the regenerative ORC reduces the system irreversibility and increased the second law efficiency. It also reduced the quantity of heat required to produce the same power. Their findings also confirmed the fact that dry fluids do not need to be superheated, since superheating reduces thermal efficiency and increases system irreversibility. They also found that the higher the boiling temperature of the dry organic fluid, the higher the thermal efficiency of the ORC. Kaikko et al. (2009) compared the performance of an Air Bottoming Cycle (ABC) with that of an ORC (using toluene as the working fluid) when both are used as bottoming cycles for a small-scale (7.8 MW) gas turbine with an exhaust temperature of 534oC and a large-scale (16.8 MW) diesel engine with an exhaust temperature of 400oC. They found that under power generation mode, the ORC system always demonstrated a better performance than the ABC at exhaust temperature levels up to 680oC, whilst the ABC dominated at higher temperatures. However, for the cogeneration of 38

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