Thermo-hydraulic analysis of direct steam generation in a 500 m long row of parabolic trough solar collector using Eulerian two-fluid modeling approach

• Published in: Applied thermal engineering 2024-04, Vol.242, p.122496, Article 122496
• Main Authors: Pal, Ram Kumar, Ravi Kumar, K.
• Format: Article
• Language: English
• Subjects: Concentrating solar power; Direct steam generation; Flow boiling; Parabolic trough solar collector; Thermal-hydraulic modeling
• ISSN: 1359-4311
• DOI: 10.1016/j.applthermaleng.2024.122496

•3-D two-fluid modeling of DSG in PTSC has been presented.•Thermal behavior of the absorber tube is described at various operating conditions.•Steel absorber tubes may be subjected to a circumferential temperature gradient of up to 34 K.•Absorber temperature may reach up to 922 K in the superheating section.•Circumferential temperature difference slowly decreases from preheating to the evaporation section. Direct steam generation (DSG) in the parabolic trough solar collectors is a potential alternative for economic and performance improvement of the solar thermal system. This process comprises the preheating, evaporation, and superheating of water/steam in the solar collectors. The modeling and simulation of the evaporation section are challenging because of the complex physics associated with the boiling phase change process. This work describes the Eulerian two-fluid modeling of the once-through mode of the DSG process in solar collectors. The interfacial interactions between phases have been modeled using the appropriate empirical correlations. The experimental data from the Spanish DISS test facility is used to validate the numerical model. Further, the 3-D thermal–hydraulic investigation of DSG in a 500 m long solar collectors' row has been performed for operating pressures of 60 bar and 100 bar; inlet mass flow rates of 0.4 kg/s and 0.6 kg/s; DNI of 750 W/m2 for the solar time at 12:00 h and 13:00 h. It has been observed that the maximum absorber temperature is reduced by 27 % at 60 bar and 20 % at 100 bar operating pressure when the inlet mass flow rate increases from 0.4 kg/s to 0.6 kg/s. Similarly, the maximum circumferential temperature difference reduces by 12 % and 14 %, respectively. Moreover, the fluid temperature, steam quality, absorber temperature distributions, fluid velocity, and pressure loss under the subjected boundary conditions have been summarized.