Comparison of values of wall temperature gradient θ’ (0)with previous studies for the case of regular fluid Nb = Nt = 10–5when λ = 0.

Comparisons of heat transfer coefficient at different inlet temperature with fluid temperature.

Mei Yang (51996)

July 2016

Comparisons of heat transfer coefficient at different inlet temperature with fluid temperature.</...

Temperature comparison between simulated and measured data.

Zejun Chen (773988)
Huiquan Han (773989)
Wei Ren (267391)
Guangjie Huang (773990)

July 2015

(A) Without considering the velocity of the steel pipe. (B) Considering the effect of the velocit...

Comparisons of heat transfer coefficient with wall and without wall at 33kW/m2 and 120kW/m2 along the tube.

Mei Yang (51996)

July 2016

Comparisons of heat transfer coefficient with wall and without wall at 33kW/m2 and 120...

Numerical values of wall temperature gradient θ’ (0)in the case of regular fluid (Nb = Nt = 10-5). Paranthesis show the corresponding results of Liu et al. [23].

Junaid Ahmad Khan (626920)
M. Mustafa (705036)
T. Hayat (517125)
M. Sheikholeslami (705037)
A. Alsaedi (517127)

March 2015

Numerical values of wall temperature gradient θ’ (0)in the case of regular fluid (Nb</i...

Computational results of wall temperature gradient θ’(0) for different values of parameters.

Junaid Ahmad Khan (626920)
M. Mustafa (705036)
T. Hayat (517125)
A. Alsaedi (517127)

September 2015

Computational results of wall temperature gradient θ’(0) for different values of parameter...

Temperature effect on non-Darcian flow in low-permeability porous media

Yuntian Teng

May 2022

This dataset includes the measured threshold gradients and permeabilities of low permeability porous...

A comparison between isotherms (a), (c) and streamlines (b), (d) of the nanofluid and base fluid in a glass balls porous medium for two inclination angles of α = - 60° and α = + 60° when Ra = 1000, A = 1, φ = 0.05 and ε = 0.5; the dashed red lines are base fluid and the solid green lines are the nanofluid.

Mohammad Ghalambaz (741163)
Mikhail A. Sheremet (741164)
Ioan Pop (399874)

May 2015

A comparison between isotherms (a), (c) and streamlines (b), (d) of the nanofluid and base fluid ...

Differences between measured pipe wall surface temperatures and internal fluid temperatures

Gorman, J.M.
Sparrow, E.M.
Abraham, J.P.

October 2013

AbstractThis report sets forth a case study to clarify the accuracy of a measurement technique commo...

Exact solutions of laminar-boundary-layer equations with constant property values for porous wall with variable temperature /

Donoughe, Patrick L.
Livingood, John N. B.
United States. National Advisory Committee for Aeronautics.

Exact solutions of the laminar-boundary-layer equations for wedge-type flow with constant property v...

Development of wall temperature (Tw) and flow temperature (Tf) at 33kW/m2

Mei Yang (51996)

July 2016

Development of wall temperature (Tw) and flow temperature (Tf) at 33kW/m2</p

Temperature jump as a function of wall temperature gradient at a silica-SAM-water interface.

Jian-Jun Shu (1592365)
Ji Bin Melvin Teo (3233811)
Weng Kong Chan (3233814)

October 2016

Symbols: MD simulation results [<a href="http://www.plosone.org/article/info:doi/10.1371/journal....

Experimental and simulated results of voltage-temperature gradient (a) and current-temperature gradient (b) behavior of the cells.

Muhammad Tariq Saeed Chani (584615)
Kh. S. Karimov (584616)
Abdullah M. Asiri (187546)
Nisar Ahmed (584617)
Muhammad Mehran Bashir (584618)
Sher Bahadar Khan (508662)
Malik Abdul Rub (511347)
Naved Azum (584619)

April 2014

Experimental and simulated results of voltage-temperature gradient (a) and current-temperature gr...

Numerical values of heat flux at the wall when N2 = 1.0, N3 = 0.1, λ = 0.1, M = 0.1, Kr = 0.1, Pr = 1.

Sohail Nadeem (450902)
Sadaf Masood (750313)
Rashid Mehmood (336455)
Muhammad Adil Sadiq (750314)

June 2015

Numerical values of heat flux at the wall when N2 = 1.0, N3 = 0.1, λ = 0.1,...

Effect of nonuniform temperature gradientson thermogravitational convectionin aporouslayer using a thermal nonequilibrium model

Lee, J.
Shivakumara, I.S.
Mamatha, A.L.

January 2011

The effect of various forms of nonuniform basic temperature gradients on the onset of convection in ...

SUMMARY

C. R. Illingworth

January 1952

The paper treats problems of laminar boundary layers with non-uniform density, due either to large t...

Comparisons of heat transfer coefficient at different inlet temperature with fluid temperature.

Mei Yang (51996)

July 2016

Comparisons of heat transfer coefficient at different inlet temperature with fluid temperature.</...

Temperature comparison between simulated and measured data.

Zejun Chen (773988)
Huiquan Han (773989)
Wei Ren (267391)
Guangjie Huang (773990)

July 2015

(A) Without considering the velocity of the steel pipe. (B) Considering the effect of the velocit...

Comparisons of heat transfer coefficient with wall and without wall at 33kW/m2 and 120kW/m2 along the tube.

Mei Yang (51996)

July 2016

Comparisons of heat transfer coefficient with wall and without wall at 33kW/m2 and 120...

Numerical values of wall temperature gradient θ’ (0)in the case of regular fluid (Nb = Nt = 10-5). Paranthesis show the corresponding results of Liu et al. [23].

Junaid Ahmad Khan (626920)
M. Mustafa (705036)
T. Hayat (517125)
M. Sheikholeslami (705037)
A. Alsaedi (517127)

March 2015

Numerical values of wall temperature gradient θ’ (0)in the case of regular fluid (Nb</i...

Computational results of wall temperature gradient θ’(0) for different values of parameters.

Junaid Ahmad Khan (626920)
M. Mustafa (705036)
T. Hayat (517125)
A. Alsaedi (517127)

September 2015

Computational results of wall temperature gradient θ’(0) for different values of parameter...

Temperature effect on non-Darcian flow in low-permeability porous media

Yuntian Teng

May 2022

This dataset includes the measured threshold gradients and permeabilities of low permeability porous...

A comparison between isotherms (a), (c) and streamlines (b), (d) of the nanofluid and base fluid in a glass balls porous medium for two inclination angles of α = - 60° and α = + 60° when Ra = 1000, A = 1, φ = 0.05 and ε = 0.5; the dashed red lines are base fluid and the solid green lines are the nanofluid.

Mohammad Ghalambaz (741163)
Mikhail A. Sheremet (741164)
Ioan Pop (399874)

May 2015

A comparison between isotherms (a), (c) and streamlines (b), (d) of the nanofluid and base fluid ...

Differences between measured pipe wall surface temperatures and internal fluid temperatures

Gorman, J.M.
Sparrow, E.M.
Abraham, J.P.

October 2013

AbstractThis report sets forth a case study to clarify the accuracy of a measurement technique commo...

Exact solutions of laminar-boundary-layer equations with constant property values for porous wall with variable temperature /

Donoughe, Patrick L.
Livingood, John N. B.
United States. National Advisory Committee for Aeronautics.

Exact solutions of the laminar-boundary-layer equations for wedge-type flow with constant property v...

Development of wall temperature (Tw) and flow temperature (Tf) at 33kW/m2

Mei Yang (51996)

July 2016

Development of wall temperature (Tw) and flow temperature (Tf) at 33kW/m2</p

Temperature jump as a function of wall temperature gradient at a silica-SAM-water interface.

Jian-Jun Shu (1592365)
Ji Bin Melvin Teo (3233811)
Weng Kong Chan (3233814)

October 2016

Symbols: MD simulation results [<a href="http://www.plosone.org/article/info:doi/10.1371/journal....

Experimental and simulated results of voltage-temperature gradient (a) and current-temperature gradient (b) behavior of the cells.

Muhammad Tariq Saeed Chani (584615)
Kh. S. Karimov (584616)
Abdullah M. Asiri (187546)
Nisar Ahmed (584617)
Muhammad Mehran Bashir (584618)
Sher Bahadar Khan (508662)
Malik Abdul Rub (511347)
Naved Azum (584619)

April 2014

Experimental and simulated results of voltage-temperature gradient (a) and current-temperature gr...

Numerical values of heat flux at the wall when N2 = 1.0, N3 = 0.1, λ = 0.1, M = 0.1, Kr = 0.1, Pr = 1.

Sohail Nadeem (450902)
Sadaf Masood (750313)
Rashid Mehmood (336455)
Muhammad Adil Sadiq (750314)

June 2015

Numerical values of heat flux at the wall when N2 = 1.0, N3 = 0.1, λ = 0.1,...

Effect of nonuniform temperature gradientson thermogravitational convectionin aporouslayer using a thermal nonequilibrium model

Lee, J.
Shivakumara, I.S.
Mamatha, A.L.

January 2011

The effect of various forms of nonuniform basic temperature gradients on the onset of convection in ...

SUMMARY

C. R. Illingworth

January 1952

The paper treats problems of laminar boundary layers with non-uniform density, due either to large t...

Comparisons of heat transfer coefficient at different inlet temperature with fluid temperature.

Mei Yang (51996)

July 2016

Comparisons of heat transfer coefficient at different inlet temperature with fluid temperature.</...

Temperature comparison between simulated and measured data.

Zejun Chen (773988)
Huiquan Han (773989)
Wei Ren (267391)
Guangjie Huang (773990)

July 2015

(A) Without considering the velocity of the steel pipe. (B) Considering the effect of the velocit...

Comparisons of heat transfer coefficient with wall and without wall at 33kW/m2 and 120kW/m2 along the tube.

Mei Yang (51996)

July 2016

Comparisons of heat transfer coefficient with wall and without wall at 33kW/m2 and 120...

Comparison of values of wall temperature gradient <b><i>θ’</i></b> (0)with previous studies for the case of regular fluid <i>Nb = Nt = 10</i><sup><i>–5</i></sup>when <i>λ</i> = 0.

Abstract

Extracted data

Comparison of values of wall temperature gradient <b><i>θ’</i></b> (0)with previous studies for the case of regular fluid <i>Nb = Nt = 10</i><sup><i>–5</i></sup>when <i>λ</i> = 0.

Abstract

Extracted data

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