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(a) 0 1.05 4 5 6 3.5 3.55 3.6 3.65 3.7 t [s] t [s] (b) 300 250 200 150 100 50 change in superheating set-point Valve opening (CT charging) FOV opening change in Tsat set-point TE1.0 TE2.0 T sat 0 0 5 10 15 20 25 t [hours] Figure 7.12: Temperature measurements acquired during a test campaign in D6 siloxane at 1.27 bar and 298 ◦C. Tsat is the saturation temperature calculated starting from the measured pressure. TE1.0 is the temperature measured by the PT-100 in the vapour generator. TE2.0 is the temperature measured by the PT-100 in the reference tube. 1.4 1.2 1 0.8 PIT1, PIT2 PIT3, PIT4 1.25 1.2 PIT3 PIT4 0.6 1.15 0.4 0.2 Figure 7.13: Original signals from an expansion in D6 siloxane at 1.27 bar and 298 ◦C. 7.13a: complete expansion, the two couples of signals, corresponding to the two measurement stations are visible. 7.13b: detail of the first expansion, it is possible to distinguish the four signals. sured quantities has not taken into account). As detailed in Ref. [19], an expanded uncertainty of the order of 6% can be associated to the specific heat capacity of the fluid. Being the epistemic un- certainty associated to the cited thermodynamic model unknown, a first and conservative approach 1.1 Commissioning of the FAST setup PIT1 PIT2 P [bar] P [bar] o T [ C] 195PDF Image | New Concepts FOR Organic Rankine Cycle Power Systems
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