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Analysis of possibilities for 1MW electricity generation from waste heat in the port of Rotterdam Page 47 We can see that this cycle is more complex because it contains more elements: • Apparatus 1 is the heat exchanger • Apparatus 2 is a node, the separator • Apparatus 3 is the high-temperature regenerator • Apparatus 4 is a node, the mixer • Apparatus 5 is the turbine • Apparatus 6 is the pump • Apparatus 7 is the low-temperature regenerator • Apparatus 8 is the condenser • Apparatus G is the generator There are also 3 circuits (as in the ORC) although the WF circuit is more complicated due to the existence of the separator (apparatus 2): 4.3 • • • The circuit in red is for the HS: source 21 is the HS outlet and sink 22 is the inlet The blue circuit is for the CS: source 11 is the CS outlet and sink 12 is the inlet. The circuit in black represents an ammonia/water mixture with an 80% concentration. In the separator, the flow is divided into two streams: the stream in green represents the poor mixture (around 50% ammonia) while the circuit in purple represents the rich mixture (around 98% ammonia) that will action the turbine. After the turbine, the two streams are mixed again into an 80% concentration mixture. Results of simulation The Cycle-Tempo diagram with the full set of results can be found in Annex F.3 and F.4, while the summary of the results is shown in Table 4.2 below: HS flow CS flow WF flow Thermal Exergetic [kg/s] [kg/s] [kg/s] efficiency efficiency Carnot ratio Ammonia/ water summer winter 5,6 356 256 16,1 7,69% 36,09% 28,88 % 35,88 % 29,93 % Table 4.2 – Summary of results for Kalina simulation Finally, we obtained a range of prices for ammonia, which is the expensive component of the water/ammonia mixture. The indicative prices of ICIS.com [Ref. 60] show a range of 380–780 $/ton, which equals to 28-60 c€/kg.PDF Image | 1MW electricity generation from waste heat port of Rotterdam
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