Non iterative model for steam condensation in presence of non-condensable gases inside passive containment cooling vertical tubes

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dc.contributor.author De la Rosa, J.C.
dc.contributor.author Munoz-Cobo, J.L.
dc.contributor.author Escrivá, A.
dc.date.accessioned 2014-12-03T08:42:00Z
dc.date.available 2014-12-03T08:42:00Z
dc.date.issued 2007
dc.description.abstract Paper presented at the 5th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, South Africa, 1-4 July, 2007. en_US
dc.description.abstract The modelling of condensation in presence of non-condensable gases is of relevance for the design of passive containment cooling condenser of the third generation of Passive Nuclear Power Plants. Fast and accurate methods of predictions for condensation in presence of non-condensable gases are necessary in order to be implemented in the thermal-hydraulic codes without slowing down the computational speed of these codes. In this paper we present a mechanistic model for condensation in presence of non-condensable gases inside vertical tubes. In this model we take into account the influence of the non-condensable gases over the liquid side heat transfer without any iteration to calculate the liquid-steam interfacial temperature. The trick is to perform a set of Taylor expansions for the main physical magnitudes as viscosity, steam mass fraction and so on. We also consider the interfacial shear stress exerted by the steam-non-condensable mixture flow over the condensate layer thickness. The calculation of the condensate layer thickness can be performed with the help of the mass, energy and momentum conservation equations and can be achieved without any iteration following the method of Munoz-Cobo et al [1,2]. The new proposed mechanistic model solves explicitly the real interfacial temperature by means of a cubic or a quartic equation depending on the degree of approximation that has been chosen. Moreover, as the main non-condensable effects can be accounted for in the heat and mass transfer processes, the new model will be more realistic. The model has been validated with the Vierow experimental data, obtaining a total average relative error, for the fourth order equation method model, of 21% with 268 experimental points at different conditions en_US
dc.description.librarian cs2014 en_US
dc.format.extent 9 pages en_US
dc.format.medium PDF en_US
dc.identifier.citation De la Rosa, JC, Munoz-Cobo, JL & Escrivá, A 2007, Non iterative model for steam condensation in presence of non-condensable gases inside passive containment cooling vertical tubes, Paper presented to the 5th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, South Africa, 1-4 July 2007. en_US
dc.identifier.isbn 9781868546435
dc.identifier.uri http://hdl.handle.net/2263/42775
dc.language.iso en en_US
dc.publisher International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics en_US
dc.relation.ispartof HEFAT 2007
dc.rights University of Pretoria en_US
dc.rights.uri University of Pretoria en_US
dc.subject Non-condensable gases en_US
dc.subject Passive containment cooling condenser en_US
dc.subject Passive nuclear power plants en_US
dc.subject Steam-non-condensable mixture flow en_US
dc.subject Vierow experimental data en_US
dc.title Non iterative model for steam condensation in presence of non-condensable gases inside passive containment cooling vertical tubes en_US
dc.type Presentation en_US


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