International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 03 Issue: 09 | Sep -2016 www.irjet.net p-ISSN: 2395-0072
© 2016, IRJET | Impact Factor value: 4.45 | ISO 9001:2008 Certified Journal | Page 805
EFFECT OF HEAT FLUX AND PRESSURE ON HEAT TRANSFER
COEFFCIENT DURING THE BOILING OF DISTILLED WATER AND
BENZENE
Tarun Kumar
1
, Dr. C. H. Tyagi
2
, Varun Tyagi
3
1
Assistant Professor, Department of Mechanical Engineering, IIMT Engineering College, Meerut, UP, INDIA
2
Professor & Head, Department of Mechanical Engineering, Subharti University, Meerut, UP, INDIA
3
Assistant Professor, Department of Mechanical Engineering, Subharti University, Meerut, UP, INDIA
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ABSTRACT: This investigation presents experimental
work on the studies of nucleate pool boiling of distilled
water and benzene at atmospheric and sub atmospheric
pressure. The experimental investigation is carried out on
heat transfer studies from a submerged horizontal
stainless steel cylinder under the condition of constant
heat flux to the pool of distilled water and benzene. The
heating surface consisted of a horizontal SS cylinder of 70
mm diameter, 4 mm thickness and the length of 244 mm
was taken. The surface temperature of the cylinder was
measured at three different positions by means of copper
constantan thermocouple. They were placed in three axial
holes in the thickness of the heating cylinder. These were
at its top-, side- and bottom- positions. The liquid
temperatures were also measured at the corresponding
positions in the bulk of the liquid. The experimental data
were conducted to account for the effect of heat flux and
pressure on heat transfer coefficient. The pressure was
varied from 35.36 to 100.07 kN/m
2
and the heat flux was
varied from 13027.99 to 33740.46 watt/m
2
. The heating
surface exhibited distinct thermal response to the changes
in heat flux.
For all the data conducted with distilled water and
benzene, the heating surface showed a distribution of
boiling heat transfer coefficient around its circumference.
The coefficient decreases from top- to side- to bottom-
positions distinctly. The average value of heat transfer
coefficient for the boiling of benzene has functional
relationship with heat flux. The data analysis shows that
the seven-tenth power law relating heat transfer
coefficient is valid for the boiling of distilled water and
benzene at atmospheric and sub atmospheric pressures.
The effect of pressure for the sub atmospheric pressure
range, it is found that the heat transfer coefficient
increases with pressure raised to the power 0.32. Actually,
the heating surface characteristics and the physico-
thermal properties of boiling fluids have marked influence
on heat transfer coefficient for sub atmospheric as well as
for the data at atmospheric pressure also.
1. INTRODUCTION
Free convection and nucleate pool boiling from
horizontal surface are of wide occurrence in process
industries, refrigeration industries and in many other
industries. Because of their industrial applications, a
considerable research has been done by the scientists to
investigate the various aspects which may give an insight
into the fundamental principles involved. All such
studies have been carried out extensively both
theoretically as well as experimentally by employing
heating surfaces of different materials, shapes and sizes.
There are so many parameters which affects the heat
transfer coefficient during the pool boiling of liquids. In
the present investigation we have conducted the
experiments on the boiling of distilled water and the
benzene. The effect of the various parameters like heat
flux, pressure, surface characteristics etc. has also been
studied. The present investigations have been carried
out with the following objectives.
I. To obtain the experimental data representing
the circumferential temperature distribution of
a horizontal cylindrical surface and of the liquid
surround it.
II. To conduct the experiments on the boiling fluids
like distilled water and benzene at their
saturation temperature over a range of low heat
flux and atmospheric and sub atmospheric
pressures.
III. To account for the parametric effects of
operating variable like heat flux, system
pressure and heating surface characteristics on
boiling heat transfer coefficient and to
recommend a generalised correlation.