2006
DOI: 10.1007/s00231-006-0123-9
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Convective heat transfer in the thermal entrance region of finned double-pipe

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Cited by 32 publications
(15 citation statements)
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“…The average Nusselt numbers Nu h and Nu e and the two average products of the Fanning friction factor and the Reynolds number fRe h and fRe e may be expressed in their dimensionless form as [3][4][5][6][7][8][9][20][21][22][23][24][25]]…”
Section: Optimization Problem and Its Solutionmentioning
confidence: 99%
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“…The average Nusselt numbers Nu h and Nu e and the two average products of the Fanning friction factor and the Reynolds number fRe h and fRe e may be expressed in their dimensionless form as [3][4][5][6][7][8][9][20][21][22][23][24][25]]…”
Section: Optimization Problem and Its Solutionmentioning
confidence: 99%
“…He employed the finite difference method for finding the numerical solution of the governing system of equations. Then for the same geometry, the performance of FDP in the entrance region of the developing flow was evaluated for various configurations of the finned annulus [21][22][23][24]. Syed et al [25] studied the flow and heat transfer characteristics, taking into account the heat transfer coefficient and the pressure loss as the measuring parameters, by using the finite element method for the solution of the governing momentum and energy equations.…”
mentioning
confidence: 99%
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“…In [11], the actual pipes are deployed in a helical coil pattern. Other enhanced double-pipe heat exchangers involved features such as [12,13] (fins), [14] (louvered strips), [15] (ring protuberances), [16] (twisted inner square tube in an outer circular tube), [17] (bulbous protrusions in the inner tube wall), and [18,19] (two helically-wrapped circular tubes). The literature involving corrugated double pipe heat exchangers is virtually exclusively concerned with experimentation.…”
Section: Introductionmentioning
confidence: 99%
“…Syed et al [19] made numerical simulation of finned double-pipe heat exchanger, where fins are distributed around the outer wall of the inner pipe. By using H1 (constant heat flux) and T1 (constant wall temperature) boundary conditions and one-dimensional fin equation, he concluded that the fin heat loss increases if we increase the conductivity of fin.…”
Section: Introductionmentioning
confidence: 99%