A high-performance heat exchanger should be used in the evaporator and condenser of Ocean Thermal Energy Conversion (OTEC) since the utilizable temperature difference is small (about 20°C). It is generally said that the plate-type and the double-fluted tube-type heat exchangers are suitable for an OTEC power plant. In this paper, optimization carried out using a double-fluted tubetype heat exchanger, considering turbine configuration. Ammonia is used as the working fluid. The performance of an OTEC plant with a plate-type exchanger is compared with the performance of a plant with a double-fluted tube-type exchanger.
The objective function g is defined Уby the following equation:
У= Total heat exchanger area/Net power = AT / PN (M2/kw) (1)
The net power is obtained by subtracting the power of the warm seawater pump, the cold seawater pump and the working fluid pump from the gross power. The total heat transfer area is obtained by using heat transfer coefficients of the seawater and the working fluid side.
The overall heat transfer area of the evaporator AE, and the overall heat transfer area of the condenser AC are given as follows:
AE= QE/{UE(ΔTm)E} (2)
AC= QC/{UC(ΔTm)C} (3)