Chacracteristics of In–Line Tube Bundle Heat Transfer to Vertical Foam Flow


Jonas Gylys1,a, Stasys Sinkunas2,c, Tadas Zdankus1,b and Martynas Babilas2,d

1Energy Technology Institute, Kaunas University of Technology, Kaunas, LT-44239 Lithuania.

ajonas.gylys@ktu.lt
btadas.zdankus@ktu.lt

2Department of Thermal and Nuclear Energy, Kaunas University of Technology, Kaunas, LT-44239 Lithuania.

cstasys.sinkunas@ktu.lt
dmartynas.babilas@stud.ktu.lt

ABSTRACT

An experimental investigation of heat transfer from the in-line tube bundle to the two-phase gas-liquid foam flow was performed. Statically stable foam flow was used as a coolant. The experimental setup consisted of the foam generator, experimental channel, in-line tube bundle, measurement instrumentation and auxiliary equipment. During the experiments the dependence of heat transfer intensity on flow parameters, viz., flow velocity, direction of flow and volumetric void fraction of foam was determined. Further, the influence of tube position of the bundle on heat transfer intensity was also investigated. The results of the investigation showed, that characteristics of in-line tube bundle heat transfer to vertical foam flow is different in comparison with one-phase fluid flow. Heat transfer intensity of the in-line tube bundle to the foam flow is much higher (from 25 to 100 times) than that to the one-phase airflow under the same flow velocity.

Keywords: Heat transfer, Foam flow, In–line tube bundle, Upward and Downward flow.



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