Disadvantages Of Heat Transfer

1038 Words3 Pages

Boiling is the most efficient forms of heat transfer since large values of heat flux can be realized at small value of temperature difference between a heated surface and working fluid. For conventional engineering applications the temperature difference is in the range of 5 ~ 15 K, which can cause heat flux values typically exceeding 10 W/cm2 (and in some reports reaching values as high as 1 kW/cm2). This is 100 ~ 1000 times higher than other forms of heat transfer (such as natural convection). These high values of boiling heat flux are achieved by leveraging the large values of enthalpy change associated with liquid-vapor phase change. These enthalpy differentials are in turn combined with significant mass transport fluxes as well as a combination …show more content…

The boiling phenomena is modulated in these applications by leveraging different operational and systemic parameters. In addition to temperatures of the heater and the working fluid - the transport processes in boiling can be modulated by several parameters such as geometry (shape and size), morphology and orientation of the heater; orientation and magnitude of gravitational acceleration; material properties of the heater surface as well as the fluid; system pressure; exposure to electro-magnetic field; flow velocities and inter-molecular interactions at the solid-liquid interface. When external actuators are not employed to induce the flow of the working fluid during liquid-to-vapor phase change phenomena for heater temperatures exceeding the saturation temperature it is termed as pool boiling. In contrast, when external actuators are employed for inducing bulk fluid motion on a heater exposed to the working fluid it is termed as flow …show more content…

These analytical and numerical approaches were observed to provide satisfactory predictions for wall heat flux on conventional plain heater configurations (flat plate, cylinder, spheres, etc.). However, significant discrepancies were observed between the predictions obtained from these mechanistic models and the experimental observations involving heaters with nanostructured surfaces. Hence, this study is focused on parametric exploration of pool boiling phenomena on a flat plate heater involving both conventional and nano-structured heaters. The scope of this study is focused on monitoring the bubble departure diameter and bubble departure frequency for different segments of the boiling curve (i.e., boiling heat flux expressed as a function of wall superheat and liquid subcooling). A brief description of the boiling curve is provided

Open Document