Masoud Ziabasharhagh

Prof. Masoud Ziabasharhagh

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Research Focus & Metrics

Academic Career Length

35Years (1992-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 February 2014 in Experimental Thermal and Fluid Science
Verified
Journal Article
Closed access
MMMohammad Salemi Mojarrad
Mohammad Salemi Mojarrad
AKAli Keshavarz
Ali Keshavarz
MZMasoud Ziabasharhagh
Masoud Ziabasharhagh
MRMohammad Mehdi Raznahan
Mohammad Mehdi Raznahan

1 January 2021 in Energy Conversion and Management
Verified
Journal Article
Closed access
AEArmin Ebrahimi
Armin Ebrahimi
BGBahram Ghorbani
Bahram Ghorbani
FSFatemeh Skandarzadeh
Fatemeh Skandarzadeh
MZMasoud Ziabasharhagh
Masoud Ziabasharhagh


1 October 2020 in Energy Conversion and Management
Verified
Journal Article
Closed access
BGBahram Ghorbani
Bahram Ghorbani
AEArmin Ebrahimi
Armin Ebrahimi
MMMostafa Moradi
Mostafa Moradi
MZMasoud Ziabasharhagh
Masoud Ziabasharhagh

22 November 2011 in International Journal of Energy Research
Verified
Journal Article
Closed access
PDF file
MHMehdi Hosseini
Mehdi Hosseini
IDIbrahim Dincer
Ibrahim Dincer
PAPouria Ahmadi
Pouria Ahmadi
HAHasan Barzegar Avval
Hasan Barzegar Avval
MZMasoud Ziabasharhagh
Masoud Ziabasharhagh
In this article, an integrated solid oxide fuel cell (SOFC) and micro gas turbine (MGT) with a multi‐effect desalination (MED) system is proposed, and its comprehensive thermodynamic modelling, through energy and exergy analyses, is conducted. In addition, the effects of some design parameters on the hybrid system are investigated. The results show that fuel cell stack pressure has a significant effect on the combined system power and distilled water capacity. It also increases the SOFC‐MGT energy efficiency. Moreover, the pressure of the inlet heating steam to the multieffect desalination system affects the pure water production in a positive way. An increase in the steam pressure results in a lower steam mass flow rate generated in the heat recovery steam generator. However, it increases desalination product capacity. Copyright © 2011 John Wiley & Sons, Ltd.