Purpose -The purpose of this paper is to develop a numerical model to simulate the flow field as well as the conjugate heat transfer during unsteady cooling of a flat plate with a single submerged water jet. At wall temperatures above the liquid boiling point, the vapor formation process and the interaction of the vapor phase with the developing jet-flow field are included. Design/methodology/approach -The time-dependent flow and temperature distribution during all occurring boiling phases as well as the local and temporal distribution of the heat transfer coefficient on a flat plate can be simulated. Findings -The influence of the liquid jet flow rate (10,800 ¼ Re_d ¼ 32,400) and the nozzle distance to the plate (4 ¼ H/d ¼ 20) on the transient cooling process are analyzed. This includes the time-dependant positions of the transition regions between the boiling phases on the plate as well as the temperatures at these transition regions. Additionally, the local heat transfer rates are a direct result of the unsteady cooling simulation. Originality/value -A single model approach is developed and utilized to simulate the unsteady cooling process of a flat plate with an impinging water jet including all occurring boiling phases.bubble d diameter e energy liq liquid m mass p, q phase indicator ref reference sat saturation sub subcooling sup wall superheat vap vapor 153 Liquid jet cooling process of a flat plate Introduction
Boiling phases and boiling heat transferThe heat transfer from a heated specimen to a liquid at wall temperatures above the boiling temperature of the liquid (T wall 4T sat ) is significantly influenced by boiling phenomena and vapor formation processes. At high surface temperatures a vapor film may be formed, separating the hot solid body from the surrounding liquid. During this film boiling phase, the low conductivity of the vapor phase causes low heat transfer rates. When the wall temperature decreases below the "Leidenfrost-point" the vapor film collapses and the surface partially rewets. This transition point is in coincidence with a local minimum in the heat flux distribution from the surface. Here, the partial contact between the hot wall and the cooling liquid as well as the considerable amount of generated vapor intensifies the heat transfer rates in this nucleate or transition boiling regimes. The convective heat transfer is intensified through the increased movement through bubble formation and detaching processes and an additional amount of energy proportional to the evaporation rate is removed through the latent heat (Kandlikar, 1999;Auracher and Marquardt, 2004;Liščić, 2009). The maximum heat transfer rate is achieved at the critical heat flux (CHF) or departure from nucleation boiling point. For wall temperatures below the saturation temperature of the liquid, evaporation stops and heat transfer can be described based on the mechanisms for convective single-phase flows. The heat transfer rate vs surface temperature in this transient cooling process is described by the Nukiyama-curve ...