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Journal articles on the topic 'Gnielinski'

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1

Erens, P. J., and A. A. Dreyer. "Heat Transfer from Immersed Slender Bodies." International Journal of Mechanical Engineering Education 23, no. 3 (1995): 203–11. http://dx.doi.org/10.1177/030641909502300304.

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This article describes a simple, low-cost experiment which could be used as a good educational example for students, combining the effects of radiation, natural convection, forced convection and condensation into one experiment. Many correlations are available for the calculation of the heat transfer from single, slender bodies (or tubes) immersed in a moving fluid. Even for a simple cylindrical tube the predicted heat transfer coefficients differ significantly from correlation to correlation. For more complex tube geometries fewer correlations could be found in the literature. The correlation
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2

Zulfattah, Z. M., S. A. Rafeq, Z. M. Shukri, et al. "Gnielinski Method in Calculating the Heat Transfer Coefficient for Metallic Solar Tower Absorber." Procedia Engineering 68 (2013): 293–98. http://dx.doi.org/10.1016/j.proeng.2013.12.182.

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3

Abedini, E., A. Behzadmehr, H. Rajabnia, SMH Sarvari, and SH Mansouri. "Experimental investigation and comparison of subcooled flow boiling of TiO2 nanofluid in a vertical and horizontal tube." Proceedings of the Institution of Mechanical Engineers, Part C: Journal of Mechanical Engineering Science 227, no. 8 (2012): 1742–53. http://dx.doi.org/10.1177/0954406212466765.

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In this study, variations of local heat transfer coefficient are obtained in subcooled flow boiling conditions for water/TiO2 nanofluid in a vertical and horizontal tube. The results for the base fluid are compared with the predictions of the well known Shah correlation and Gnielinski formula for laminar and turbulent flows for single-phase forced convection and also with Chen correlation for subcooled flow boiling. A good agreement between the results is realized. At the subcooled regime, heat transfer coefficient of nanofluid is less than that of the base fluid and it decreases by increasing
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4

Harmen, Willy Adriansyah, Abdurrachim, and Ari Darmawan Pasek. "METODOLOGI PERHITUNGAN KOEFISIEN PERPINDAHAN PANAS KONVEKSI PAKSA FLUIDA ORGANIK PROPANA PADA KONDISI SUPERKRITIK." Jurnal Teknologi 9, no. 2 (2017): 89. http://dx.doi.org/10.24853/jurtek.9.2.89-96.

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Penelitian tentang siklus Rankine organik superkritis mulai giat dilakukan sebagai salah satu usaha untuk meningkatkan efisiensi termal dari siklus Rankine organik. Pada kondisi superkritik, sifat-sifat termodinamika dan fisika dari fluida organik berubah dengan sangat drastis disekitar titik kritisnya. Sehingga perhitungan koefisien perpindahan panas konveksi paksa tidak dapat lagi dilakukan dengan asumsi sifat-sifat fluida konstan. Dalam penelitian ini diusulkan sebuah metodologi untuk menghitung nilai koefisien perpindahan panas pada kondisi superkritis. Propana digunakan sebagai fluida org
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5

Ji, Wen-Tao, Ding-Cai Zhang, Ya-Ling He, and Wen-Quan Tao. "Prediction of fully developed turbulent heat transfer of internal helically ribbed tubes ? An extension of Gnielinski equation." International Journal of Heat and Mass Transfer 55, no. 4 (2012): 1375–84. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2011.08.028.

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6

Wang, Ning, Yu Pan, Heng Bao, and Jin Zhou. "Numerical Investigation on Supercritical Heat Transfer of RP3 Kerosene Flowing inside a Cooling Channel of Scramjet." Advances in Mechanical Engineering 6 (January 1, 2014): 213438. http://dx.doi.org/10.1155/2014/213438.

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Supercritical convective heat transfer characteristics of hydrocarbon fuel play a fundamental role in the active cooling technology of scramjet. In this paper, a 2D-axisymmetric numerical study of supercritical heat transfer of RP3 flowing inside the cooling channels of scramjet has been conducted. The main thermophysical properties of RP3, including density, specific heat, and thermal conductivity, are obtained from experimental data, while viscosity is evaluated from a commercial code with a ten-species surrogate. Effects of heat flux, mass flow rate, and inlet temperature on supercritical h
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7

Sarafraz, M. M., S. M. Peyghambarzadeh, and N. Vaeli. "Subcooled flow boiling heat transfer of ethanol aqueous solutions in vertical annulus space." Chemical Industry and Chemical Engineering Quarterly 18, no. 2 (2012): 315–27. http://dx.doi.org/10.2298/ciceq111020008s.

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The subcooled flow boiling heat-transfer characteristics of water and ethanol solutions in a vertical annulus have been investigated up to heat flux 132kW/m2. The variations in the effects of heat flux and fluid velocity, and concentration of ethanol on the observed heat-transfer coefficients over a range of ethanol concentrations implied an enhanced contribution of nucleate boiling heat transfer in flow boiling, where both forced convection and nucleate boiling heat transfer occurred. Increasing the ethanol concentration led to a significant deterioration in the observed heat-transfer coeffic
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8

Ammar, Syed Muhammad, and Chan Woo Park. "Validation of the Gnielinski correlation for evaluation of heat transfer coefficient of enhanced tubes by non-linear regression model: An experimental study of absorption refrigeration system." International Communications in Heat and Mass Transfer 118 (November 2020): 104819. http://dx.doi.org/10.1016/j.icheatmasstransfer.2020.104819.

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9

Steiner, R. "Verdampfung, Kristallisation, Trocknung. VonV. Gnielinski,A. Mersmann undF. Thurner. Friedrich Vieweg & Sohn Verlagsgesellschaft mbH, Braunschweig 1993. 259 S., mit zahlr. Abb. und Tab., DM 54,-." Chemie Ingenieur Technik 66, no. 6 (1994): 874. http://dx.doi.org/10.1002/cite.330660625.

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10

Gawande, K. R., and A. V. Deshmukh. "Experimental Investigation of Heat Transfer Rate Using Twisted Tape with Elliptical Holes." IRA-International Journal of Technology & Engineering (ISSN 2455-4480) 7, no. 2 (S) (2017): 105. http://dx.doi.org/10.21013/jte.icsesd201711.

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An experimental investigation was carried for measuring tube-side heat transfer coefficient, friction factor, heat transfer enhancement efficiency of water for turbulent flow in a circular tube fitted with rectangular-cut twisted tape insert. A copper tube of 26.6 mm internal diameter and 30 mm outer diameter and 900 mm test length was used. A stainless steel rectangular-cut twisted tape insert of 5.25 twist ratio was inserted into the smooth tube. The rectangular cut had 8 mm depth and 14 mm width. A uniform heat flux condition was created by wrapping nichrome wire around the test section and
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11

Martins, Jonathan Ribeiro, Daniel da Cunha Ribeiro, Fabio de Assis Ressel Pereira, Marcos Pellegrini Ribeiro, and Oldrich Joel Romero. "Heat dissipation of the Electrical Submersible Pump (ESP) installed in a subsea skid." Oil & Gas Science and Technology – Revue d’IFP Energies nouvelles 75 (2020): 13. http://dx.doi.org/10.2516/ogst/2020009.

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The recent development of Electrical Submersible Pump (ESP) in the skid, installed in the seabed downstream of the wellhead in an offshore oil production system, is an alternative to the conventional system with the set installed at the bottom of the producing well, facilitating interventions in case of failure. The pump is driven by an electric motor whose cooling must be efficient to ensure the continuity of its operation. The heat withdrawal is performed by the fluid produced. The purpose of this article is to understand the process of electric motor cooling to the single-phase and turbulen
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12

Slaney, A. J., and R. Bhamidimarri. "Adsorption of pentachlorophenol (PCP) by activated carbon in fixed beds: application of homogeneous surface diffusion model." Water Science and Technology 38, no. 7 (1998): 227–35. http://dx.doi.org/10.2166/wst.1998.0296.

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The adsorption of pentachlorophenol (PCP) from aqueous solutions was investigated using fixed beds of activated carbon. The equilibrium behaviour was shown to fit a Freundlich isotherm with the values of parameters K and l/n of 95 and 0.180 respectively, which are comparable to those of other substituted phenolics. The surface diffusion coefficient was evaluated from batch kinetic adsorption experiments and was found to be 2.26 × 10−9 cm2s−1. The film transfer coefficient in the fixed beds was estimated using Gnielinski’s correlation. A Homogeneous Surface Diffusion Model (HSDM) was proposed t
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13

Abdelkader, M., H. Ameur, and Y. Menni. "Investigation of the convective heat transfer and friction factor of magnetic Ni nanofluids within cylindrical pipes." International Journal of Thermofluid Science and Technology 8, no. 1 (2021). http://dx.doi.org/10.36963/ijtst.2021080101.

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The current paper reports the results of numerical research on the magnetic Ni nanofluid flowing in a tube, developing turbulent flows under constant heat flux conditions. The numerical investigations are conducted for a Reynolds number range from 3,000 to 22,000, and a particle concentration range of 0% to 0.6%. The effects of the Reynolds number on the friction factor and Nusselt number are computed and compared satisfactorily with the experimental results of the literature. The classical correlations of Gnielinski, Notter – Rouse, and Pak and Cho are verified by predicting the Nusselt numbe
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14

Godson, Lazarus, B. Raja, D. Mohan Lal, and S. Wongwises. "Convective Heat Transfer Characteristics of Silver-Water Nanofluid Under Laminar and Turbulent Flow Conditions." Journal of Thermal Science and Engineering Applications 4, no. 3 (2012). http://dx.doi.org/10.1115/1.4006027.

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The convective heat transfer coefficient and pressure drop of silver-water nanofluids is measured in a counter flow heat exchanger from laminar to turbulent flow regime. The experimental results show that the convective heat transfer coefficient of the nanofluids increases by up to 69% at a concentration of 0.9 vol. % compared with that of pure water. Furthermore, the experimental results show that the convective heat transfer coefficient enhancement exceeds the thermal conductivity enhancement. It is observed that the measured heat transfer coefficient is higher than that of the predicted one
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15

Aly, Wael I. A. "Computational Fluid Dynamics and Optimization of Flow and Heat Transfer in Coiled Tube-in-Tube Heat Exchangers Under Turbulent Flow Conditions." Journal of Thermal Science and Engineering Applications 6, no. 3 (2014). http://dx.doi.org/10.1115/1.4026120.

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The present computational fluid dynamics (CFD) study was performed to investigate the 3D turbulent flow and heat transfer of coiled tube-in-tube heat exchangers (CTITHEs). The realizable k-ε model with enhanced wall treatment was used to simulate the turbulent flow and heat transfer in the heat exchangers. Temperature dependent thermophysical properties of water were used and heat exchangers are analyzed considering conjugate heat transfer from hot fluid in the inner-coiled tube to cold fluid in the annulus region. After simulations, Taguchi method was used for finding the optimum condition fo
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16

Vojacek, Ales, Vaclav Dostal, Friedrich Goettelt, Martin Rohde, and Tomas Melichar. "Performance Test of the Air-Cooled Finned-Tube Supercritical CO2 Sink Heat Exchanger." Journal of Thermal Science and Engineering Applications 11, no. 3 (2019). http://dx.doi.org/10.1115/1.4041686.

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This technical paper presents results of an air-cooled supercritical CO2 (sCO2) finned-tube sink heat exchanger (HX) performance test comprising wide range of variable parameters (26–166 °C, 7–10 MPa, 0.1–0.32 kg/s). The measurement covered both supercritical and subcritical pressures including transition of pseudocritical region in the last stages of the sink HX. The test was performed in a newly built sCO2 experimental loop which was constructed within Sustainable Energy (SUSEN) project at Research Centre Rez (CVR). The experimental setup along with the boundary conditions are described in d
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17

Valentín, Francisco I., Narbeh Artoun, Masahiro Kawaji, and Donald M. McEligot. "Forced and Mixed Convection Heat Transfer at High Pressure and High Temperature in a Graphite Flow Channel." Journal of Heat Transfer 140, no. 12 (2018). http://dx.doi.org/10.1115/1.4039585.

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High pressure/high temperature forced and mixed convection experiments have been performed with helium and nitrogen at temperatures and pressures up to 893 K and 64 bar, respectively. The test section had a 16.8 mm ID flow channel in a 108 mm OD graphite column. Flow regimes included turbulent, transitional, and laminar flows with the inlet Reynolds numbers ranging from 1500 to 15,000. Due to strong heating, the local Reynolds number decreased by up to 50% over the 2.7 m test section. In addition, heat transfer degradation and flow laminarization caused by intense heating led to Nusselt number
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18

Lupiano Contreras, J., A. S. Doval, and P. A. Alberto. "Thermal–Hydraulic Design in the Transition Laminar–to–Turbulent Flow Regime." Journal of Nuclear Engineering and Radiation Science 5, no. 2 (2019). http://dx.doi.org/10.1115/1.4042363.

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Difficulties are experienced during the thermal–hydraulic design of a nuclear reactor operating in the transition flow regime and are the result of the inability to accurately predict the heat transfer coefficient (HTC). Experimental values for the HTC in rectangular channels are compared with the calculated by correlations usually used for the design of material testing reactors (MTR). The values predicted by Gnielinski and Kreith correlations at Reynolds numbers below 5000 are not necessarily conservative. The Al-Arabi-Churchill correlation with the correction proposed by Jones has proved to
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19

Forrest, Eric C., Lin-Wen Hu, Jacopo Buongiorno, and Thomas J. McKrell. "Convective Heat Transfer in a High Aspect Ratio Minichannel Heated on One Side." Journal of Heat Transfer 138, no. 2 (2015). http://dx.doi.org/10.1115/1.4031646.

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Experimental results are presented for single-phase heat transfer in a narrow rectangular minichannel heated on one side. The aspect ratio and gap thickness of the test channel were 29:1 and 1.96 mm, respectively. Friction pressure drop and Nusselt numbers are reported for the transition and fully turbulent flow regimes, with Prandtl numbers ranging from 2.2 to 5.4. Turbulent friction pressure drop for the high aspect ratio channel is well-correlated by the Blasius solution when a modified Reynolds number, based upon a laminar equivalent diameter, is utilized. The critical Reynolds number for
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