Laith S Sabri

Dr. Laith S Sabri

University of Technology- Iraq, Baghdad, Baghdād, Iraq
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orcid

Research Focus & Metrics

Academic Career Length

9Years (2018-Present)

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

Representative Publications

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1 September 2018 in International Journal of Multiphase Flow
Verified
Journal Article
Closed access
Abbas J. SultanAbbas J. Sultan
Abbas J. Sultan
LSLaith S Sabri
Laith S Sabri
Muthanna Al-DahhanMuthanna Al-Dahhan
Muthanna Al-Dahhan

1 September 2019 in Chemical Engineering Research and Design
Verified
Journal Article
Closed access
LSLaith S Sabri
Laith S Sabri
ASAbbas J. Sultan
Abbas J. Sultan
MAMuthanna H. Al-Dahhan
Muthanna H. Al-Dahhan

12 May 2022 in Chemengineering
Verified
Journal Article
Open access
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Amer A. AbdulrahmanAmer A. Abdulrahman
Amer A. Abdulrahman
OMOmar S. Mahdy
Omar S. Mahdy
LSLaith S Sabri
Laith S Sabri
Abbas J. SultanAbbas J. Sultan
Abbas J. Sultan
HAHayder Al-Naseri
Hayder Al-Naseri
JAJamal Manea Ali
Jamal Manea Ali
The present study provides and examines an experimental and CFD simulation to predict and accurately quantify the individual phase holdup. The experimental findings demonstrated that the increase of solid beads has a significant influence on the (Umf), as comparatively small glass beads particles require a low (Umf) value, which tends to increase as the diameter of the beads increases. Besides that, the expansion ratio is proportional to the velocity of the liquid. Even though, the relationship becomes inversely proportional to the diameter of the beads. The liquid holdup was found to increase with increasing liquid velocity, however, the solid holdup decreased. The Eulerian–Eulerian granular multiphase flow technique was used to predict the overall performance of the liquid–solid fluidized beds (LSFBs). There was a good agreement between the experimental results and the dynamic properties of liquid–solid flows obtained from the CFD simulation, which will facilitate future simulation studies of liquid–solid fluidized beds. This work has further improved the understanding and knowledge of CFD simulation of such a system at different parameters. Furthermore, understanding the hydrodynamics features within the two-phase fluidization bed, as well as knowing the specific features, is essential for good system design, enabling the systems to perform more effectively.

13 October 2020 in Journal of Chemical Technology & Biotechnology
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Journal Article
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AOAastha Ojah
Aastha Ojah
LSLaith S Sabri
Laith S Sabri
MAMuthanna H. Aldahhan
Muthanna H. Aldahhan

1 January 2024 in Fluid Dynamics & Materials Processing
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Journal Article
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AMAyat N. Mahmood
Ayat N. Mahmood
AAAmer A. Abdulrahman
Amer A. Abdulrahman
LSLaith S Sabri
Laith S Sabri
ASAbbas J. Sultan
Abbas J. Sultan
HMHasan Shakir Majdi
Hasan Shakir Majdi
MAMuthanna H. Al-Dahhan
Muthanna H. Al-Dahhan
Hydrodynamics characterization in terms of flow regime behavior is a crucial task to enhance the design of bubble column reactors and scaling up related methodologies. This review presents recent studies on the typical flow regimes established in bubble columns. Some effort is also provided to introduce relevant definitions pertaining to this field, namely, that of “void fraction” and related (local, chordal, cross-sectional and volumetric) variants. Experimental studies involving different parameters that affect design and operating conditions are also discussed in detail. In the second part of the review, the attention is shifted to cases with internals of various types (perforated plates, baffles, vibrating helical springs, mixers, and heat exchanger tubes) immersed in the bubble columns. It is shown that the presence of these elements has a limited influence on the global column hydrodynamics. However, they can make the homogeneous flow regime more stable in terms of transition gas velocity and transition holdup value. The last section is used to highlight gaps which have not been filled yet and future directions of investigation.

14 September 2023 in Chemengineering
Verified
Journal Article
Open access
PDF file
LSLaith S Sabri
Laith S Sabri
Abbas J. SultanAbbas J. Sultan
Abbas J. Sultan
JAJamal Manea Ali
Jamal Manea Ali
HMHasan Majdi
Hasan Majdi
Muthanna Al-DahhanMuthanna Al-Dahhan
Muthanna Al-Dahhan
Fluidized bed reactors are essential in a wide range of industrial applications, encompassing processes such as Fischer–Tropsch synthesis and catalytic cracking. The optimization of performance and reduction in energy consumption in these reactors necessitate the use of efficient heat transfer mechanisms. The present work examines the considerable impact of tube end geometries, superficial gas velocity, and radial position on heat transfer coefficients within fluidized bed reactors. It was found that the tapered tube end configurations have been empirically proven to improve energy efficiency in fluidized bed reactors significantly. For example, at a superficial gas velocity of 0.4 m/s, the tapered end form’s local heat transfer coefficient (LHTC) demonstrated a significant 20% enhancement compared to the flat end shape. The results and findings of this work make a valuable contribution to the advancement of complex models, enhance the efficiency of fluidized bed reactor processes, and encourage further investigation into novel tube geometries.