Entropy generation of pseudo-plastic non-Newtonian nanofluids in circular duct under constant wall temperature
Abstract
In this paper the second law analysis of thermodynamic irreversibilities in pseudo-plastic non-Newtonian nanofluids through a circular duct under uniform wall temperature thermal boundary have been carried out for laminar flow condition. This nanofluid consists of sodium carboxymethyl cellulose (CMC)–water and two different types of nanoparticles; namely, CuO and Al2O3. Entropy generation is obtained for various Power law number, various volume concentration of nanoparticles, various dimensionless temperature and various Reynolds number. It is found that with the decreasing Power law number and duct length values, total entropy generation at fixed Reynolds number decreases and with increasing wall temperature values, total entropy generation increases, also entropy generation decreases with increasing volume concentration of nanoparticles.
Full Text:
PDFReferences
B.C. Pak, I.Y. Cho. (1998) Hydrodynamic and heat transfer study of dispersed fluids withSub-micron metallic oxide particles. Experimental Heat Transfer, 151-170. [1]
H. Masuda, A. Ebata, K. Teramae, N. Hishiunma. (1993) Alteration of thermal conductivity and viscosity of liquid by dispersed ultra-fine particles (dispersion of Al2O3, SiO2, and TiO2 ultra-fine particles). Netsu Bussei, 227–233. [2]
SK. Da, N. Putra, P. Thiesen, W. Roetzel. (2003) Temperature dependence of thermal conductivity enhancement for nanofluids. Journal of Heat Transfer, 567–574. [3]
A. Bejan. (1979)A study of entropy generation in fundamental convective heat transfer. Journal of Heat Transfer, 101(4), 718-725. [4]
A. Bejan. (1982) Entropy generation through heat and fluid flow. New York, Wiley. [5]
A. Bejan. (1996) Entropy generation minimization. Boca Raton, FL, CRC Press. [6]
A. Bejan. (1996) Entropy generation minimization: the new thermodynamics of finite size devices and finite-time processes. Journal of Applied Physics, 1191-1218. [7]
I. Dagtekin, H.F. Ozotop,A.Z. Sahin. (2005) An analysis of entropy generation through a circular duct with different shaped longitudinal fins for laminar flow. International Communications in Heat and Mass Transfer, 171–181. [8]
H.F. Ozotop, I. Dagtekin, A.Z. Sahin. (2009) Second law analysis of fully developed laminar flow for rectangular ducts with semicircular ends. International Communications in Heat and Mass Transfer, 725–730. [9]
A.Z. Sahin. (1996) Thermodynamics of laminar viscous flow through a duct subjected to constant heat flux. Energy, 1179–1187. [10]
A.Z. Sahin. (1998) Irreversibilities in various duct geometries with constant wall heat flux and laminar flow. Energy, 465–473. [11]
A.R. Falahat, A. Vosough. (2012) Effect of nanofluid on entropy generation and pumpingpower in coiled tube. J Thermophys. Heat Transfer, 26 (1), 141–146. [12]
A.R. Falahat. (2011) Entropy generation analysis of fully developed laminar forced convection in a confocal elliptical duct with uniform wall heat flux. Indian Journal of Science and Technology, 1649-1653. [13]
M. Moghaddami, A. Mohammadzade, S.A.V. Esfehani. (2011)Second law analysis of nanofluid flow. Energy Conversion and Management, 1397–1405. [14]
Jin DX, Wu YH, Zou JT. Studies on heat transfer to pseudo plastic fluid in an agitated tank with helical ribbon impeller. Petro-Chemical Equipment. 2000;29 (2): 7–9. [15]
K. Khanafer, K. Vafai, M. Lightstone. (2003) Buoyancy-Driven Heat Transfer Enhancement in a Two-Dimensional Enclosure Utilizing Nanofluids. International journal of Heat and Mass Transfer, 3639-3653. [16]
A.K. Santra, S. Sen, N. Chakraborty. (2008)Study of heat transfer augmentation in adifferentially heated square cavity using copper-water nanofluid. International Journal Thermal Science, 1113–1122. [17]
A. Raptis, C. Perdikis, H.S. Takhar. (2004) Effect of thermal radiation on MHD flow. ApplicationMathematical Computation, 645–649. [18]
A.Z. Sahin. (1998) A second law comparison for optimum shape of duct subjected to constant wall temperature and laminar flow. Journal Heat and Mass Transfer, 425–430. [19]
J.M. Coulson, J.F. Richardson. (1999) Chemical Engineering (6th edition)., Oxford: Butterworth–Heinemann. [20]
R.P. Chhabra, J.F. Richardson. (2008) Non-Newtonian Flow in the Process Industries Fundamentals and Engineering Applications. Chemical Engineering (2nd edition). [21]
DOI: http://dx.doi.org/10.2022/jmet.v10i1.866
PRINT ISSN No.: 2180-1053
E ISSN No.: 2289-8123