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Featured researches published by P.K. Sarma.


International Journal of Thermal Sciences | 2003

Laminar convective heat transfer with twisted tape inserts in a tube

P.K. Sarma; T. Subramanyam; P.S. Kishore; V.Dharma Rao; S. Kakaç

Abstract A new method is postulated to predict heat transfer coefficients with twisted tape inserts in a tube, in which the wall shear and the temperature gradients are properly modified through friction coefficient correlation leading to heat transfer augmentation from the tube wall. The eddy diffusivity expression of van Driest is modified to respond to the case of the internal flows in a tube with twisted tapes for ranges of Reynolds number corresponding to the laminar flow in tubes. The predictions from the present theory are compared with some correlations available in literature for twisted tape inserts. The present theoretical results are rendered in the form of a correlation equation.


International Journal of Thermal Sciences | 2000

The effects of thermal non-equilibrium and inlet temperature on two-phase flow pressure drop type instabilities in an upflow boiling system

L. Cao; S. Kakaç; Hongtan Liu; P.K. Sarma

Abstract In this paper a theoretical model for the two-phase flow pressure drop type instabilities in an upflow boiling system is presented. The thermal non-equilibrium effect between the two phases is included assuming the enthalpy profile in the subcooled boiling region. The system of differential equations describing the single-phase and boiling regions of the system (drift-flux model) is solved using finite difference method for the steady state characteristics of the system over a wide range of operating conditions. Upon obtaining the steady state characteristics, the dynamic formulation of the pressure drop type oscillation is solved numerically. The modeling results are verified by the experimental findings. The effect of the thermal non-equilibrium on the steady state characteristics, stability boundaries and oscillation periods at different heat inputs and inlet temperatures are presented as being compared with the experimental measurements as well as the results obtained from the thermal equilibrium model.


International Journal of Thermal Sciences | 2002

Convective condensation heat transfer in a horizontal condenser tube

P.K. Sarma; C.V.N Sastry; V.D. Rao; S. Kakaç; Hongton Liu

The purpose of this article is to solve analytically the problem of convective condensation of vapors inside a horizontal condenser tube. Homogeneous model approach is employed in the estimation of shear velocity, which is subsequently, made use of in predicting local convective condensation heat transfer coefficients. The resulting analysis of the present study is compared with some of the available equations in the literature. It is observed that the agreement is reasonably satisfactory validating the assumptions and the theory presented.


International Journal of Heat and Mass Transfer | 2001

Condensation of vapours on a fin in the presence of non-condensable gas

P.K. Sarma; M. Anjaneya Reddy; Arthur E. Bergles; S. Kakaç

Abstract Condensation of vapours on a vertical fin in the presence of non-condensable gas is formulated and solved for a wide range of system parameters, making use of the analogy between heat and mass transfer. The formulation enables the derivation of special cases such as condensation of vapours on a vertical isothermal surface with and without non-condensable gas in the vapour. Besides, the analysis of condensation of vapour on a fin has revealed non-isothermal conditions of the thin fin with the temperature of the liquid–vapour interface also changing along the length of the fin. The numerical results from the analysis are rendered into dimensionless equations that can be used to predict the mean condensation heat transfer coefficients.


International Journal of Thermal Sciences | 2000

A method to predict two-phase pressure drop using condensation heat transfer data

P.K. Sarma; V.D. Rao; T. Subrahmanyam; S. Kakaç; Hongtan Liu

Abstract The data of Kutateladze related to mean condensation heat transfer coefficients of pure vapors of steam flowing in a horizontal tube are correlated considering the phenomenon as a homogenous flow. Colburns analogy assuming to hold good the mean friction coefficients for a homogenous flow conditions are evaluated making use of heat transfer data. By extending the model further the two-phase frictional pressure drop multipliers are established. Predictions from these correlations have reasonably agreed with the magnitudes obtained from Lockhart and Martinelli correlations which are conventionally used in the design.


International Communications in Heat and Mass Transfer | 2009

Estimation of heat transfer coefficient and friction factor in the transition flow with low volume concentration of Al2O3 nanofluid flowing in a circular tube and with twisted tape insert

K.V. Sharma; L. Syam Sundar; P.K. Sarma


International Journal of Thermal Sciences | 2014

Comparison of Convective Heat Transfer Coefficient and Friction Factor of TiO2 Nanofluid flow in a tube with Twisted Tape Inserts

W.H. Azmi; K.V. Sharma; P.K. Sarma; Rizalman Mamat; Shahrani Anuar


International Communications in Heat and Mass Transfer | 2014

Heat Transfer and Friction Factor of Water Based TiO2 and SiO2 Nanofluids under Turbulent Flow in a Tube

W.H. Azmi; K.V. Sharma; P.K. Sarma; Rizalman Mamat; G. Najafi


International Communications in Heat and Mass Transfer | 2004

Performance of a Circular Fin in a Cylindrical Porous Enclosure

S.V. Naidu; V. Dharma Rao; P.K. Sarma; T. Subrahmanyam


Heat and Mass Transfer | 2001

Theoretical analysis of pressure-drop type instabilities in an upflow boiling system with an exit restriction

L. Cao; S. Kakaç; Hongtan Liu; P.K. Sarma

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W.H. Azmi

Universiti Malaysia Pahang

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Rizalman Mamat

Universiti Malaysia Pahang

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P.S. Kishore

Gandhi Institute of Technology and Management

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L. Cao

University of Miami

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K.V. Sharma

Jawaharlal Nehru Technological University

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