1. “Modeling of a Coal
Fired Natural Circulation Boiler”, ASME Journal of Energy Resources and
Technology, in press.
Abstract-
Modeling of natural circulation boiler for a coal fired thermal power
station is presented here. The boiler system is divided into seven
sub-components and for each section, models based on conservation of mass,
momentum and
energy are formulated. The pressure drop at various sections and the heat
transfer coefficients are computed using empirical correlations. Solutions
are obtained by using SIMULINK. The model is validated by comparing
its steady
state and dynamic responses with the actual plant data. Open loop responses
of the model to the step changes in the operating parameters like pressure,
temperature, steam flow, feed water flow, are also analyzed. The present
model can be used for the development and design of effective boiler control
systems.
2. “CFD Modeling of Two
Phase Bubbly Flow with Heat and Mass Transfer” Joint ISHMT- ASME, Heat
and Mass Transfer Conference, 2006.
Abstract-
Sub-cooled flow boiling is a case of two phase bubbly flow, which is
encountered in various engineering applications such as boilers, reactors,
refrigeration systems, heat exchangers and various power generation systems.
If there is very high heat flux, the film boiling burnout or flow
instability may lead to failure of components. Prediction of void fraction
profile, flow pattern, thermal field and velocity distribution, is essential
for design and safety analysis of such systems.
In this paper, three dimensional two fluid model (continuous liquid phase
and dispersed vapor phase) is solved to estimate void fraction, velocity and
temperature profiles with inclusion of inter phase heat and mass transfer
processes. Commercial CFD software CFX-5.7.1 is used to solve the problem.
The above parameters are evaluated for upward bubbly flow in a vertical pipe
with six heated rods for high pressure. The various drag and non-drag forces
are tested. Model developed by Rensselaer Polytechnic Institute (RPI), is
used to distribute the wall heat flux between vapor generation and heating
sub-cooled liquid. The results of present study are compared with numerical
results of Anglart-Nylund and experimental data of Nylund et.al. The present
study shows a good agreement with experimental data and numerical results in
the literature.
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