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Modeling of a Low Temperature Rankine Cycle for Small Scale Cogen

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Modeling of a Low Temperature Rankine Cycle for Small Scale Cogen ( modeling-low-temperature-rankine-cycle-small-scale-cogen )

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Sylvain Quoilin Chapter 4 : Description of the experiments by the uncertainties on the measurements at the nozzle. The (pessimistic) uncertainties taken into account are : – 0.3 K on the nozzle air supply temperature (non calibratedthermocouple) – A hypothetical 1% error on the pressure transducers. In order to determine which method is the best to measure the air flow rate, the heat fluxes over the evaporator are calculated and compared with each method : Three different heat transfers are compared : ● Over the first exchanger (hx1). In this case, only the 13 first tests are taken into account, the fluid being in two­phase state at the exhaust of hx1 in the other tests. (cfr figure 26) ● Over the two first exchangers (hx12). In this case, on the other hand, only the 13 last points are taken into account, in order to be sure that the fluid is in superheated vapor state at the exhaust of the second exchanger. ● Over the whole evaporator (hx123) They are calculated as follows : 48

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