International Journal of Mechanical Engineering and Applications

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Modelling and Simulation of the Multi-effect/Thermal Vapor Compression Distillation Process

Received: 14 September 2020    Accepted: 29 September 2020    Published: 12 October 2020
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Abstract

The Multi-effect distillation (MED) associated with thermal vapor compression (TVC) process has recently been applied for a number of desalination plants in the GCC countries and emerged as a strong competitor to the multistage flash distillation (MSF) process. The MED/TVC desalination process is characterized by low power consumption compared to the MSF process. It is currently operated at low TBT of 65°C to avoid scale formation compared to MSF technology which operate at top brine temperature of 110°C, this lead to lower tendency to scale formation and less fouling risk. The use of more efficient pretreatment to MED/TVC desalination plants such as nano-filtration or high performance additive antiscalant would allow operating MED at higher TBT which allow increasing the performance ratio. A simulation steady-state program has been established to analyze the thermodynamic behavior of parallel feed flow MED/TVC unit at a wide range of TBT from 65°C up to 125°C and different number of effects with different condition of motive steam pressure on the performance ratio, and specific heat transfer and therefore the best design of MED for the future different design options were considered to optimize the operational of MED system to enhance the economics and performance of MED technology.

DOI 10.11648/j.ijmea.20200804.12
Published in International Journal of Mechanical Engineering and Applications (Volume 8, Issue 4, August 2020)
Page(s) 103-110
Creative Commons

This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.

Copyright

Copyright © The Author(s), 2024. Published by Science Publishing Group

Keywords

MED-TVC, Desalination, Simulation, Heat and Mass Balance

References
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Author Information
  • Thermal Department, Desalination Technologies Research Institute (DTRI-SWCC), Jubail, Saudi Arabia

  • Thermal Department, Desalination Technologies Research Institute (DTRI-SWCC), Jubail, Saudi Arabia

  • Thermal Department, Desalination Technologies Research Institute (DTRI-SWCC), Jubail, Saudi Arabia

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  • APA Style

    Khalid Bamardouf, Osman Ahmed Hamed, Amro Mohammed Mahmoud. (2020). Modelling and Simulation of the Multi-effect/Thermal Vapor Compression Distillation Process. International Journal of Mechanical Engineering and Applications, 8(4), 103-110. https://doi.org/10.11648/j.ijmea.20200804.12

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    ACS Style

    Khalid Bamardouf; Osman Ahmed Hamed; Amro Mohammed Mahmoud. Modelling and Simulation of the Multi-effect/Thermal Vapor Compression Distillation Process. Int. J. Mech. Eng. Appl. 2020, 8(4), 103-110. doi: 10.11648/j.ijmea.20200804.12

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    AMA Style

    Khalid Bamardouf, Osman Ahmed Hamed, Amro Mohammed Mahmoud. Modelling and Simulation of the Multi-effect/Thermal Vapor Compression Distillation Process. Int J Mech Eng Appl. 2020;8(4):103-110. doi: 10.11648/j.ijmea.20200804.12

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  • @article{10.11648/j.ijmea.20200804.12,
      author = {Khalid Bamardouf and Osman Ahmed Hamed and Amro Mohammed Mahmoud},
      title = {Modelling and Simulation of the Multi-effect/Thermal Vapor Compression Distillation Process},
      journal = {International Journal of Mechanical Engineering and Applications},
      volume = {8},
      number = {4},
      pages = {103-110},
      doi = {10.11648/j.ijmea.20200804.12},
      url = {https://doi.org/10.11648/j.ijmea.20200804.12},
      eprint = {https://download.sciencepg.com/pdf/10.11648.j.ijmea.20200804.12},
      abstract = {The Multi-effect distillation (MED) associated with thermal vapor compression (TVC) process has recently been applied for a number of desalination plants in the GCC countries and emerged as a strong competitor to the multistage flash distillation (MSF) process. The MED/TVC desalination process is characterized by low power consumption compared to the MSF process. It is currently operated at low TBT of 65°C to avoid scale formation compared to MSF technology which operate at top brine temperature of 110°C, this lead to lower tendency to scale formation and less fouling risk. The use of more efficient pretreatment to MED/TVC desalination plants such as nano-filtration or high performance additive antiscalant would allow operating MED at higher TBT which allow increasing the performance ratio. A simulation steady-state program has been established to analyze the thermodynamic behavior of parallel feed flow MED/TVC unit at a wide range of TBT from 65°C up to 125°C and different number of effects with different condition of motive steam pressure on the performance ratio, and specific heat transfer and therefore the best design of MED for the future different design options were considered to optimize the operational of MED system to enhance the economics and performance of MED technology.},
     year = {2020}
    }
    

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    T1  - Modelling and Simulation of the Multi-effect/Thermal Vapor Compression Distillation Process
    AU  - Khalid Bamardouf
    AU  - Osman Ahmed Hamed
    AU  - Amro Mohammed Mahmoud
    Y1  - 2020/10/12
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    DO  - 10.11648/j.ijmea.20200804.12
    T2  - International Journal of Mechanical Engineering and Applications
    JF  - International Journal of Mechanical Engineering and Applications
    JO  - International Journal of Mechanical Engineering and Applications
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    EP  - 110
    PB  - Science Publishing Group
    SN  - 2330-0248
    UR  - https://doi.org/10.11648/j.ijmea.20200804.12
    AB  - The Multi-effect distillation (MED) associated with thermal vapor compression (TVC) process has recently been applied for a number of desalination plants in the GCC countries and emerged as a strong competitor to the multistage flash distillation (MSF) process. The MED/TVC desalination process is characterized by low power consumption compared to the MSF process. It is currently operated at low TBT of 65°C to avoid scale formation compared to MSF technology which operate at top brine temperature of 110°C, this lead to lower tendency to scale formation and less fouling risk. The use of more efficient pretreatment to MED/TVC desalination plants such as nano-filtration or high performance additive antiscalant would allow operating MED at higher TBT which allow increasing the performance ratio. A simulation steady-state program has been established to analyze the thermodynamic behavior of parallel feed flow MED/TVC unit at a wide range of TBT from 65°C up to 125°C and different number of effects with different condition of motive steam pressure on the performance ratio, and specific heat transfer and therefore the best design of MED for the future different design options were considered to optimize the operational of MED system to enhance the economics and performance of MED technology.
    VL  - 8
    IS  - 4
    ER  - 

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