The purpose of this research work is to increase the heat transfer coefficient by operating the heat exchangers at smaller revolution per minute. This signifies an achievement of reduction of pressure drop corresponding to less operating cost. This study has used two types of SPT tape insert to observe the various heat transfer coefficient, heat transfer rate and heat transfer augmentation efficiency. One tape was fully twisted and another tape was partially twisted. The shape of the SPT tape creates turbulence effect. The turbulence flow (swirl flow) generated by SPT tape promotes greater mixing and high heat transfer coefficients. An arrangement scheme has been developed for the experimental investigation. For remarking the rate of change of heat transfer, temperature has been measured numerically through the temperature sensors with various flow rates and RPM. The volume flow rate was varied from 10.3448276 LPM to 21.045574 LPM and the rotation of the perforated twisted tape was varied from 50 RPM to 400 RPM. Finally the research study demonstrates the effectiveness of the results of the proposed approaches. It is observed that the suggested method of heat transfer augmentations is much more effective than existing methods, since it results in an increase in heat transfer area and also an increase in the heat transfer coefficient and reduction of cost in the industrial sectors.

1.
A.E.
Bergles
,
Techniques to augment heat transfer
, in:
W.M.
Rohsenow
,
J.P.
Hartnett
,
E.
Ganie
(Eds.),
Handbook of Heat Transfer Application
,
McGraw-Hill, New York
,
1985
.
2.
A.E.
Bergles
,
Some perspectives on enhanced heat transfer, second-generation heat transfer technology
,
ASME J. Heat Transfer
110
(November) (
1988
)
1082
1096
.
3.
E.
Smithberg
,
F.
Landis
,
Friction and forced convection heat transfer characteristics in tubes fitted with twisted tape swirl generators
,
ASME J. Heat Transfer
2
(
1964
)
39
49
.
4.
A.W.
Date
,
J.R.
Singham
, Numerical prediction of friction factor and heat transfer characteristics of fully developed laminar flow in tubes containing twisted tapes,
ASME Paper No. 72-HT-17
,
1972
.
5.
A.W.
Date
,
Prediction of fully developed flow in a tube containing a twisted tape
,
Int. J. Heat Mass Transfer
17
(
1974
)
845
859
.
6.
S.W.
Hong
,
A.E.
Bergles
,
Augmentation of laminar flow heat transfer in tubes by means of twisted-tape inserts
,
ASME J. Heat Transfer
98
(
1976
)
251
256
.
7.
J.P.
Duplessis
,
D.G.
Kroeger
,
Numerical prediction of laminar flow with heat transfer in tube with a twisted tape insert
, in:
Proceedings of the International Conference on Numerical Methods in Laminar and Turbulent Flow
,
1983
, pp.
775
785
.
8.
R.M.
Manglik
,
A.E.
Bergles
, in: A correlation for laminar flow enhanced heat transfer in uniform wall temperature circular tubes with twisted-tape inserts,
Advances in Heat Transfer-1987
, HTD, vol.
1987
,
ASME
,
New York
,
1987
, pp.
19
25
.
9.
C.
Shivkumar
,
M. Raja
Rao
,
Studies on compound augmentation of laminar flow heat transfer to generalized power law fluids in spirally corrugated tubes by means of twisted tape inserts
,
ASME, HTD
96
(
1988
)
685
692
.
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