Naslov
Modelling of Condensation in Vertical Tubes for Passive Safety Systems

Autori
Papini, Davide ; Ricotti, Marco ; Santini, Lorenzo ; Grgić, Davor

Vrsta, podvrsta i kategorija rada
Radovi u zbornicima skupova, cjeloviti rad (in extenso), znanstveni

Izvornik
Proceedings of the 7th International Conference on Nuclear Option in Countries with Small and Medium Electricity Grids / Čavlina, Nikola ; Pevec, Dubravko ; Bajs, Tomislav - Zagreb : Hrvatsko nuklearno društvo, 2008, S-05.87.1

ISBN
978-953-55224-0-9

Skup
7th International Conference on Nuclear Option in Countries with Small and Medium Electricity Grids

Mjesto i datum
Dubrovnik, Hrvatska, 25.05.2008. - 29.05.2008

Vrsta sudjelovanja
Poster

Vrsta recenzije
Međunarodna recenzija

Ključne riječi
vertical tube condenser; passive safety system; HTC correlation

Sažetak
The transient and safety analysis is usually carried out by means of best-estimate, thermalhydraulic codes, as RELAP. Suitable heat transfer correlations are required to duly model the two-phase processes. As far as the condensation process is concerned, RELAP5/MOD3.3 adopts the Nusselt correlation to calculate the heat transfer coefficient in laminar conditions and the Shah correlation for turbulent conditions ; the maximum of the predictions from laminar and turbulent regimes is used to calculate the condensation heat transfer coefficient. Shah correlation is generally considered as the best empirical correlation for turbulent annular film condensation, but suitable in proper ranges of the various parameters. Nevertheless, recent investigations have pointed out that its validity is highly questionable for high pressure and large diameter tube applications with water, as should be for the utilization for vertical tube condensers in passive safety systems. Thus, a best-estimate model, based on the theory of film condensation on a plain wall, is proposed. Condensate velocity, expressed in terms of Reynolds number, governs the development of three different regime zones: laminar, laminar wavy and turbulent. The best correlation for each regime (Nusselt’ s for laminar, Kutateladze’ s for laminar wavy and Chen’ s for turbulent) is considered and then implemented in RELAP code. Comparison between the Nusselt-Shah and the proposed model shows substantial differences in heat transfer coefficient prediction. Especially, a trend of increasing value of the heat transfer coefficient with tube abscissa (and quality decreasing) is predicted, when turbulence establishes and overcomes the increased thermal resistance due to the film thickness growth. This trend and the order of magnitude of calculated heat transfer coefficients have been preliminarily validated with experimental data, coming from the PERSEO facility (SIET labs, Piacenza), showing a good prediction by the new model implemented in RELAP.

Izvorni jezik
Engleski

Znanstvena područja
Elektrotehnika

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