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section of all three tubes at the same time, when reaching the first round of heat exchanger tubes. After passing the first round of tubes, the working fluid will flow further and pass the continued section of the three tubes in the same way. Consequently, the working fluid flow will pass all the sections of the three tubes until it passes the last round of heat exchanger tubes. For the outside heat transfer calculation, the module can be simplified by spreading the conically shaped heat exchanger plate into a trapezoid shape as shown in Figure 9‐6. The airflow is indicated in the figure as an example of heat exchanger outside fluid flow and different colors symbolize different heat exchanger tubes. As shown in the figure, the incoming air will pass the first section of the three tubes at the same time, when it flows over the first round of heat exchanger tubes. After that, the air flow will then pass the second section of three tubes in the same way, when it crosses the second round of heat exchanger tubes. The air will keep flowing and cross the different loops of heat exchanger tubes continually, until it reaches the last section of tubes. For every loop, the CO2 in each section of heat exchanger tubes is assumed to have the same conditions (i.e. the same temperature, the same heat transfer characteristics and pressure drop, etc.). Figure 9‐6 Heat exchanger calculation module, schematic 1 103PDF Image | Thermodynamic Cycles using Carbon Dioxide
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