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A first part of the analysis focuses on the influence of working conditions on both fluids (mass flows, inlet temperatures) and the impact of the selected coolant fluid.
The extensive pressure drop database comprises both diabatic and adiabatic results covering eight fluids, mass velocities from 23 to 6000 kg/m2 s and vapor qualities up to 1.
Knowing the influence of fluid flow perturbations on the dynamic behavior of fluid-conveying pipes is of relevance, e.g., when exploiting flow-induced oscillations of pipes to determine the fluids mass flow or density, as done with Coriolis flow meters (CFM).
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Cases for two fluid mass flow rate variation combinations, hot fluid inlet temperature and hot and cold fluid mass flow rate variation combinations are modeled and analyzed.
In the same way, assuming a situation where the internal fluid mass changes in several levels, the sloshing modeling design variables for each internal fluid mass are calculated.
In this study, the sloshing phenomenon is analyzed for the internal fluid mass change.
Simultaneously, the thermal resistance also increases significantly with the rise of working fluid mass.
The pressurizer model is developed based upon the conservation of fluid mass, volume, and energy.
Techniques for reducing error of the total fluid mass were also newly added to the OPT.
As working fluid mass flow rate rises, outlet temperature declines and thermal power increases.
Distribution of working fluid mass will significantly impact off-design performance of the Organic Rankine Cycle.
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