Navid Sharifi
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
Research Subjects
Research Interests
Navid Sharifi has a total of 14 co-authors. Here are the top co-authors by number of shared publications:
Masoud Boroomand
8 shared publicationsMajid Sharifi
7 shared publicationsRamin Kouhikamali
3 shared publicationsDavid Buttsworth
2 shared publicationsHassan Gholami
2 shared publicationsKavous Ariafar
2 shared publications
Latest Publications
- 30 September 2025
- Published by Elsevier in International Journal of Refrigeration
- Vol. 180, 548-563
Off-design modeling of gas turbines integrated with reverse Brayton refrigeration cycle for inlet air cooling
- 30 September 2025
- Published by Elsevier in International Journal of Refrigeration
- Vol. 180, 548-563
Off-design modeling of gas turbines integrated with reverse Brayton refrigeration cycle for inlet air cooling
- 1 December 2019
- Published by Elsevier in International Journal of Thermal Sciences
- Vol. 146
Study of drying process a vertical porous channel by developing a numeric solver in OpenFOAM
- 1 December 2019
- Published by Elsevier in International Journal of Thermal Sciences
- Vol. 146
Study of drying process a vertical porous channel by developing a numeric solver in OpenFOAM
- 21 August 2019
- Published by Wiley in Heat Transfer
- Vol. 48 (8) , 3682-3707
Numerical study of effective parameters on the drying process in a vertical porous channel
Comprehensive understanding of evaporation in porous channels is important for the design of modern heat exchangers and thermal systems such as heat pipes. This paper presents a numerical study of evaporation in a vertical porous channel. The volume of the fluid method was applied to capture the interface between phases. The multi‐dimensional limiter for explicit solution method, in which there are additional constraints based on the flux‐corrected transfer method, was used to solve the interface transfer equation. Pressure drop, Nusselt number, and the drying rate were considered as performance parameters. Comparing simulation results with experimental data showed that this new solver can precisely solve the thermal phase change in a porous medium. The influence of parameters effective on the drying process, such as porosity, permeability, the dynamic contact angle was investigated. Based on the results of the pressure profile in the final state, four different regions are visible. Because of the close fit of the wall temperature to the average cross‐sectional temperature, the Nusselt number increases sharply at transition points from the liquid to the vapor phase. By increasing the dynamic contact angle, the average drying rate in the channel is reduced.
- 21 August 2019
- Published by Wiley in Heat Transfer
- Vol. 48 (8) , 3682-3707
Numerical study of effective parameters on the drying process in a vertical porous channel
Comprehensive understanding of evaporation in porous channels is important for the design of modern heat exchangers and thermal systems such as heat pipes. This paper presents a numerical study of evaporation in a vertical porous channel. The volume of the fluid method was applied to capture the interface between phases. The multi‐dimensional limiter for explicit solution method, in which there are additional constraints based on the flux‐corrected transfer method, was used to solve the interface transfer equation. Pressure drop, Nusselt number, and the drying rate were considered as performance parameters. Comparing simulation results with experimental data showed that this new solver can precisely solve the thermal phase change in a porous medium. The influence of parameters effective on the drying process, such as porosity, permeability, the dynamic contact angle was investigated. Based on the results of the pressure profile in the final state, four different regions are visible. Because of the close fit of the wall temperature to the average cross‐sectional temperature, the Nusselt number increases sharply at transition points from the liquid to the vapor phase. By increasing the dynamic contact angle, the average drying rate in the channel is reduced.
- 1 November 2015
- Published by Springer Nature in Journal of Mechanical Science and Technology
- Vol. 29 (11) , 4691-4699
An investigation on the supersonic ejectors working with mixture of air and steam
- 1 November 2015
- Published by Springer Nature in Journal of Mechanical Science and Technology
- Vol. 29 (11) , 4691-4699
An investigation on the supersonic ejectors working with mixture of air and steam
- Open Access
- 1 May 2015
- Published by Elsevier in Desalination and Water Treatment
- Vol. 54 (7) , 1782-1792
Thermodynamic evaluation of high compressible steam flow in vapor compression systems used in desalination processes
- 1 May 2015
- Published by Elsevier in Desalination and Water Treatment
- Vol. 54 (7) , 1782-1792
Open AccessThermodynamic evaluation of high compressible steam flow in vapor compression systems used in desalination processes
- 1 October 2014
- Published by Elsevier in Applied Thermal Engineering
- Vol. 71 (1) , 519-527
Ejector primary nozzle steam condensation: Area ratio effects and mixing layer development
- 1 October 2014
- Published by Elsevier in Applied Thermal Engineering
- Vol. 71 (1) , 519-527
Ejector primary nozzle steam condensation: Area ratio effects and mixing layer development
- Open Access
- 1 September 2014
- Published by Elsevier in Desalination and Water Treatment
- Vol. 52 (31-33) , 5731-5739
Geometrical analysis of thermo-compressors in multiple-effects distillation units based on the second law of thermodynamics
Thermo-compressors are used instead of mechanical compression devices in many industries and play a main role in the process. Through the process of designing desalination systems, amount of exergy dissipation is a very important economical factor. Most of the exergy losses in multi-effect distillation systems with thermal vapor compression (multiple-effect desalination–TVC) occur in the thermo-compressor. The aim of this article is to investigate geometrical effects in thermo-compressors by numerical methods based on the second law of thermodynamics to obtain lower exergy loss and consequently, higher entrainment ratio. A lot of geometrical parameters such as converging and diverging angles in mixing section, diffuser, nozzle location and also its throat area ratio affect thermo-compressors’ performance. The modifications in the above-mentioned parameters were applied to a thermo-compressor established in a desalination unit in Kavian petrochemical company which is working with 15 barg of motive pressure. Numerical simulation of the base model has an accurate agreement with experimental data with about 1.3% discrepancy in maximum discharge pressure and just 6.7% in entrainment ratio. Results of the analysis indicate that thermo-compressor’s performance is sensitive to the mixing area converging angle. The other parameter which mostly affects the performance is the location of nozzle in thermo-compressor’s body.
- 1 September 2014
- Published by Elsevier in Desalination and Water Treatment
- Vol. 52 (31-33) , 5731-5739
Open AccessGeometrical analysis of thermo-compressors in multiple-effects distillation units based on the second law of thermodynamics
Thermo-compressors are used instead of mechanical compression devices in many industries and play a main role in the process. Through the process of designing desalination systems, amount of exergy dissipation is a very important economical factor. Most of the exergy losses in multi-effect distillation systems with thermal vapor compression (multiple-effect desalination–TVC) occur in the thermo-compressor. The aim of this article is to investigate geometrical effects in thermo-compressors by numerical methods based on the second law of thermodynamics to obtain lower exergy loss and consequently, higher entrainment ratio. A lot of geometrical parameters such as converging and diverging angles in mixing section, diffuser, nozzle location and also its throat area ratio affect thermo-compressors’ performance. The modifications in the above-mentioned parameters were applied to a thermo-compressor established in a desalination unit in Kavian petrochemical company which is working with 15 barg of motive pressure. Numerical simulation of the base model has an accurate agreement with experimental data with about 1.3% discrepancy in maximum discharge pressure and just 6.7% in entrainment ratio. Results of the analysis indicate that thermo-compressor’s performance is sensitive to the mixing area converging angle. The other parameter which mostly affects the performance is the location of nozzle in thermo-compressor’s body.
- 15 November 2013
- Published by ASME International
CFD Evaluation of Steam Properties Within Thermo-Compressors With Two Different Numerical Approches
Thermo-compressors are among the most important facilities in thermal desalination systems. Such devices are compressing and recycling the useless vapors and hence effectively enhancing the efficiency of desalination units. Since the connection between the evaporator box and suction surface is not perfectly symmetric, it is necessary to consider the effect of this curved path on pressure loss at the inlet boundary. In this study, a numerical procedure is developed to achieve reliable results in thermo-compressors through using CFD simulations. Two approaches are examined: axisymmetric and full three-dimensional method. The results are compared and the deviations of velocity, pressure and temperature are evaluated in both methods. The flow pattern in the steam collector is investigated afterwards. The distributions of velocity and pressure through this canal are illustrated and the critical point where pressure loss originates is revealed. In the meantime, the effect of this non-symmetric path on the flow is compared with the axisymmetric results. Finally, it is shown that the influence of the curved-shape inlet on flow properties is insignificant such that it can be neglected, because the flow swirl at the inlet is very negligible. Therefore, the axisymmetric model is capable of producing reliable results for thermo-compressors in a more advantageous way with a simpler mesh generation and reduced computational cost.
- 15 November 2013
- Published by ASME International
CFD Evaluation of Steam Properties Within Thermo-Compressors With Two Different Numerical Approches
Thermo-compressors are among the most important facilities in thermal desalination systems. Such devices are compressing and recycling the useless vapors and hence effectively enhancing the efficiency of desalination units. Since the connection between the evaporator box and suction surface is not perfectly symmetric, it is necessary to consider the effect of this curved path on pressure loss at the inlet boundary. In this study, a numerical procedure is developed to achieve reliable results in thermo-compressors through using CFD simulations. Two approaches are examined: axisymmetric and full three-dimensional method. The results are compared and the deviations of velocity, pressure and temperature are evaluated in both methods. The flow pattern in the steam collector is investigated afterwards. The distributions of velocity and pressure through this canal are illustrated and the critical point where pressure loss originates is revealed. In the meantime, the effect of this non-symmetric path on the flow is compared with the axisymmetric results. Finally, it is shown that the influence of the curved-shape inlet on flow properties is insignificant such that it can be neglected, because the flow swirl at the inlet is very negligible. Therefore, the axisymmetric model is capable of producing reliable results for thermo-compressors in a more advantageous way with a simpler mesh generation and reduced computational cost.