Flow boiling heat transfer in a helically coiled steam generator for nuclear power applications. (January 2016)

• Record Type: Journal Article
• Authors: Santini, Lorenzo; Cioncolini, Andrea; Butel, Matthew T.; Ricotti, Marco E.
• Is Part Of: International journal of heat and mass transfer. Volume 92(2016:Jan.)
• Page Start: 91
• Page End: 99
• Publication Date: 2016-01
• Subjects: Helical coil -- Convective flow boiling -- Steam generator -- Curvature effect -- Small modular nuclear reactor; Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Electronic journals; 621.4022
• DOI: 10.1016/j.ijheatmasstransfer.2015.08.012
• Languages: English
• ISSNs: 0017-9310

Abstract

Highlights: New data (1575 points) for convective flow boiling in helically coiled tubes. Data generated with prototypical test facility. Both nucleate boiling and convection contribute to the heat transfer. Curvature effects on flow boiling heat transfer negligible. Seven widely quoted straight tube correlations fit the helical coil data within ±15–20%. Abstract: Forced convection boiling of water was experimentally investigated in a 24 m long full-scale helically coiled steam generator tube, prototypical of the steam generators with in-tube boiling used in small modular nuclear reactor systems. Overall, 1575 axially local and peripherally averaged heat transfer coefficient measurements were taken, covering operating pressures in the range of 2–6 MPa, mass fluxes from 200 to 800 kg m −2 s −1 and heat fluxes from 40 to 230 kW m −2 . The heat transfer coefficient was found to depend on the mass flux and on the heat flux, indicating that both nucleate boiling and convection are contributing to the heat transfer process. Seven widely quoted flow boiling correlations for straight tubes fitted the present helical coil databank with a mean absolute percentage error within 15–20%, which was comparable with the experimental uncertainty of the measured heat transfer coefficient values, thus indicating that curvature effects on flow boiling are small and negligible in practical applications.