Lütfullah Kuddusi
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Lütfullah Kuddusi has a total of 11 co-authors. Here are the top co-authors by number of shared publications:
- Mustafa Yasin Gökaslan
Van Yuzuncu Yil Universitesi
2 shared publications - Ali Koşar
Faculty of Engineering and Natural Sciences, Sabanci University, 34956 Tuzla, Istanbul, Turkey
1 shared publication - Aydın Hacı Dönmez
Mechanical Engineering Department, Halic University, Istanbul, Turkey
1 shared publication - Burak Çoban
Mechanical Engineering Programme, Graduate School, Istanbul Technical University, 34469 Maslak, Istanbul, Turkey
1 shared publication Jesse C. Denton
Energy Associates, P.O. Box 355, Belton, TX 76513-0355, USA
1 shared publication- Kaan Erdem
Mechanical Engineering Program, Graduate School of Science Engineering and Technology, Istanbul Technical University, Maslak, 34496 Istanbul, Turkey
1 shared publication
Latest Publications
- 17 February 2026
- Published by Springer Nature
- p. 279-285
Determination of the Local Nusselt Number in the Thermal Entrance Region of Flow Between Two Parallel Plates
- 17 February 2026
- Published by Springer Nature
- p. 279-285
Determination of the Local Nusselt Number in the Thermal Entrance Region of Flow Between Two Parallel Plates
- 16 January 2025
- Published by Wiley in ZAMM - Journal of Applied Mathematics and Mechanics / Zeitschrift für Angewandte Mathematik und Mechanik
- Vol. 105 (1)
Heat transfer in the entrance region of annular laminar flow with constant and different heat flux on two walls
Heat transfer differs in the regions where the flow is developed and developing thermally. These regions can be differentiated by using the thermal entry length. Many researchers have presented correlations to determine the thermal entry length for natural and forced convection. In this study, heat transfer in the entrance region of a concentric annuli is investigated. It is accepted that beginning from the inlet of annuli the flow is developed hydrodynamically and it is developing thermally. Heat transfer is investigated where the internal or external surfaces of the annuli are at constant but different heat fluxes. The fluid velocity is assumed to be constant or radially variable. Due to thermal boundary conditions, one thermal boundary layer appears on the outer cylinder surface, another on the inner cylinder surface. The edge of two boundary layers will be adiabatic and naturally, the temperature of fluid between the two edges will be equal to free stream temperature. Transformation, Separation of Variables method, eigenvalue problem, Sturm‐Liouville system, Bessel differential equation and properties of orthogonal functions are used in solution of the problem. Exact and analytical solutions of the momentum and energy equations are presented. Velocity and temperature distributions, local Nusselt numbers and convection heat transfer coefficients are calculated for the internal and external surfaces of annuli.
- 16 January 2025
- Published by Wiley in ZAMM - Journal of Applied Mathematics and Mechanics / Zeitschrift für Angewandte Mathematik und Mechanik
- Vol. 105 (1)
Heat transfer in the entrance region of annular laminar flow with constant and different heat flux on two walls
Heat transfer differs in the regions where the flow is developed and developing thermally. These regions can be differentiated by using the thermal entry length. Many researchers have presented correlations to determine the thermal entry length for natural and forced convection. In this study, heat transfer in the entrance region of a concentric annuli is investigated. It is accepted that beginning from the inlet of annuli the flow is developed hydrodynamically and it is developing thermally. Heat transfer is investigated where the internal or external surfaces of the annuli are at constant but different heat fluxes. The fluid velocity is assumed to be constant or radially variable. Due to thermal boundary conditions, one thermal boundary layer appears on the outer cylinder surface, another on the inner cylinder surface. The edge of two boundary layers will be adiabatic and naturally, the temperature of fluid between the two edges will be equal to free stream temperature. Transformation, Separation of Variables method, eigenvalue problem, Sturm‐Liouville system, Bessel differential equation and properties of orthogonal functions are used in solution of the problem. Exact and analytical solutions of the momentum and energy equations are presented. Velocity and temperature distributions, local Nusselt numbers and convection heat transfer coefficients are calculated for the internal and external surfaces of annuli.
- Open Access
- 1 May 2024
- Published by MDPI AG in Micromachines
- Vol. 15 (5) , 618
An Experimental Investigation of R600a Condensation in a Multiport Microchannel
This study aims to provide condensation heat transfer coefficients of R600a (isobutane) refrigerant under mass fluxes between 50 and 98 kg/m2·s at saturation temperatures of 35 °C, 40 °C and 45 °C. Additionally, experiments are conducted with varying inlet vapour quality to understand its effect on the condensation heat transfer measurement. An aluminium multiport microchannel with a hydraulic diameter () of 0.399 mm is used, where a plexiglass cover is mounted on the top of the microchannels to observe the flow conditions. A 1D heat transfer through the aluminium block is assumed, and heat flux through the refrigerant to the coolant is measured to obtain condensation heat transfer coefficients of R600a. The results showed that decreasing saturation temperature and increasing vapour quality increase the condensation heat transfer coefficient. Increasing refrigerant mass flux increases the heat transfer coefficient up to a specific mass flux. It is observed that the effect of inlet vapour quality becomes significant as introduced quality decreases due to increasing fluctuation.- 1 May 2024
- Published by MDPI AG in Micromachines
- Vol. 15 (5) , 618
Open AccessAn Experimental Investigation of R600a Condensation in a Multiport Microchannel
This study aims to provide condensation heat transfer coefficients of R600a (isobutane) refrigerant under mass fluxes between 50 and 98 kg/m2·s at saturation temperatures of 35 °C, 40 °C and 45 °C. Additionally, experiments are conducted with varying inlet vapour quality to understand its effect on the condensation heat transfer measurement. An aluminium multiport microchannel with a hydraulic diameter () of 0.399 mm is used, where a plexiglass cover is mounted on the top of the microchannels to observe the flow conditions. A 1D heat transfer through the aluminium block is assumed, and heat flux through the refrigerant to the coolant is measured to obtain condensation heat transfer coefficients of R600a. The results showed that decreasing saturation temperature and increasing vapour quality increase the condensation heat transfer coefficient. Increasing refrigerant mass flux increases the heat transfer coefficient up to a specific mass flux. It is observed that the effect of inlet vapour quality becomes significant as introduced quality decreases due to increasing fluctuation. - 28 February 2021
- Published by Springer Nature in Heat and Mass Transfer
- Vol. 57 (9) , 1453-1465
Experimental study on laminar air flow through spiral channel packed with steel balls
- 28 February 2021
- Published by Springer Nature in Heat and Mass Transfer
- Vol. 57 (9) , 1453-1465
Experimental study on laminar air flow through spiral channel packed with steel balls
- Open Access
- 14 April 2020
- Published by MDPI AG in Micromachines
- Vol. 11 (4) , 412
Differential Sorting of Microparticles Using Spiral Microchannels with Elliptic Configurations
Label-free, size-dependent cell-sorting applications based on inertial focusing phenomena have attracted much interest during the last decade. The separation capability heavily depends on the precision of microparticle focusing. In this study, five-loop spiral microchannels with a height of 90 µm and a width of 500 µm are introduced. Unlike their original spiral counterparts, these channels have elliptic configurations of varying initial aspect ratios, namely major axis to minor axis ratios of 3:2, 11:9, 9:11, and 2:3. Accordingly, the curvature of these configurations increases in a curvilinear manner through the channel. The effects of the alternating curvature and channel Reynolds number on the focusing of fluorescent microparticles with sizes of 10 and 20 µm in the prepared suspensions were investigated. At volumetric flow rates between 0.5 and 3.5 mL/min (allowing separation), each channel was tested to collect samples at the designated outlets. Then, these samples were analyzed by counting the particles. These curved channels were capable of separating 20 and 10 µm particles with total yields up to approximately 95% and 90%, respectively. The results exhibited that the level of enrichment and the focusing behavior of the proposed configurations are promising compared to the existing microfluidic channel configurations.
- 14 April 2020
- Published by MDPI AG in Micromachines
- Vol. 11 (4) , 412
Open AccessDifferential Sorting of Microparticles Using Spiral Microchannels with Elliptic Configurations
Label-free, size-dependent cell-sorting applications based on inertial focusing phenomena have attracted much interest during the last decade. The separation capability heavily depends on the precision of microparticle focusing. In this study, five-loop spiral microchannels with a height of 90 µm and a width of 500 µm are introduced. Unlike their original spiral counterparts, these channels have elliptic configurations of varying initial aspect ratios, namely major axis to minor axis ratios of 3:2, 11:9, 9:11, and 2:3. Accordingly, the curvature of these configurations increases in a curvilinear manner through the channel. The effects of the alternating curvature and channel Reynolds number on the focusing of fluorescent microparticles with sizes of 10 and 20 µm in the prepared suspensions were investigated. At volumetric flow rates between 0.5 and 3.5 mL/min (allowing separation), each channel was tested to collect samples at the designated outlets. Then, these samples were analyzed by counting the particles. These curved channels were capable of separating 20 and 10 µm particles with total yields up to approximately 95% and 90%, respectively. The results exhibited that the level of enrichment and the focusing behavior of the proposed configurations are promising compared to the existing microfluidic channel configurations.
- 4 December 2018
- Published by International Centre for Applied Thermodynamics (ICAT) in International Journal of Thermodynamics
- Vol. 21 (4) , 188-189
On the occasion of 85th birthday of Prof. Sadık Kakaç
On the occasion of 85th birthday of Prof. Sadık Kakaç
- 4 December 2018
- Published by International Centre for Applied Thermodynamics (ICAT) in International Journal of Thermodynamics
- Vol. 21 (4) , 188-189
On the occasion of 85th birthday of Prof. Sadık Kakaç
On the occasion of 85th birthday of Prof. Sadık Kakaç
- 26 December 2006
- Published by Elsevier in Energy Conversion and Management
- Vol. 48 (4) , 1089-1105
Analytical solution for heat conduction problem in composite slab and its implementation in constructal solution for cooling of electronics
- 26 December 2006
- Published by Elsevier in Energy Conversion and Management
- Vol. 48 (4) , 1089-1105
Analytical solution for heat conduction problem in composite slab and its implementation in constructal solution for cooling of electronics
- 10 January 2006
- Published by Springer Nature in Heat and Mass Transfer
- Vol. 42 (12) , 1093-1101
Viscous dissipation effect on heat transfer characteristics of rectangular microchannels under slip flow regime and H1 boundary conditions
- 10 January 2006
- Published by Springer Nature in Heat and Mass Transfer
- Vol. 42 (12) , 1093-1101
Viscous dissipation effect on heat transfer characteristics of rectangular microchannels under slip flow regime and H1 boundary conditions