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Chapter 7 observed so far. Compared to the amount of theoretical and numerical studies on non-classical gas dynamics, a comparatively limited amount of effort has been devoted to experimental assess- ments, mainly due to the technical difficulties related to the observation of these fleeting waves, as discussed in Refs. [24, 25]. A first attempt has been carried out in the former USSR by Borisov and colleagues in 1983 [26, 27] who claimed to have measured a RSW in Freon-13 (trifluorochloromethane, CCl3F). Fer- gason et al. [24, 28] and others [22, 29] refute that this could have been a RSW in the single phase region and provide alternative interpretations of that experiment by pointing towards critical point phenomena and two-phase effects. Recent studies show that the fundamental derivative of gas dy- namics indeed is negative in the two-phase critical point region [30] and that rarefaction shockwaves are possible in close-to-critical conditions [31]. In the early 2000’s, a shock-tube experiment has been pursued at the University of Colorado at Boulder, with the aim of producing a RSW in perfluorocarbon fluid PP10 (Perfluorofluorene, C13F22), see Ref. [24]. The experiment eventually failed because the working fluid underwent thermal decomposition due to the extremely high operating temperature. This put into evidence one of the major obstacles, namely that the BZT thermodynamic region is very close to the thermal decomposition temperature of suitable organic fluids, which is in the range 350–400 oC. In addition, the repeatable rupture of the shock-tube diaphragm proved unattainable due to the relatively small pressure difference and the large acoustic impedance of the fluid [32, 33]. 7.3 The FAST Set-Up Building on the experience acquired during the Boulder experiment, the novel FAST set-up for the generation of RSWs has been conceived, designed and constructed at the Delft University of Technology, The Netherlands, with the participation of an international consortium of academic and industrial partners, as documented in Ref. [25]. Siloxanes have been selected as the working fluid class for the available knowledge regarding their thermal stability [34, 35], thermodynamic properties [19, 36–38], and their use as working fluids in thermal energy conversion systems [39–41]. Moreover, the products of thermal decom- position of siloxanes are non-toxic polymers, whereas thermal decomposition of perfluorocarbons may result in highly corrosive hydrofluoric acid (HF) and possibly other very toxic compounds. Furthermore, the flammability of siloxanes is far lower than that of hydrocarbons. Few of the compounds of the siloxane family are candidate BZT fluids [18]. Initially, D6 is chosen as working fluid as the result of a trade-off between the size of the predicted BZT region and the thermal stability of the fluid. The design of the RSW experiment drove studies aimed at better identifying the thermody- namic region within which non-classical phenomena are admissible, see, e.g., Ref [42]. Given that the experimental conditions are difficult to realize and that the rarefaction shock wave is expected to be weak, therefore more challenging to measure, several authors proposed methods aimed at relaxing the experimental constraints by producing comparatively stronger phenomena [28]. In particular, Guardone et al. [43] presented an analytical procedure to identify the thermo- dynamic states resulting in the RSW exhibiting the maximum pressure difference, the RSW with maximum Mach number, and the RSW with the largest strength, over the entire dense-vapour ther- modynamic region of a given BZT fluid. Uncertainty quantification applied to flow simulations has been preliminarily used, as an aid in determining the optimal experimental conditions [44]. 180PDF Image | New Concepts FOR Organic Rankine Cycle Power Systems
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