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Prof. Sivanesan Subramanian

Anna University, India

 

Prof. Hassan Karimi-Maleh

University of Electronic Science
and Technology of China (UESTC)

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Home > Archives > Vol 4, No 1 (Published) > Original Research Article
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2021-04-07

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Vol 4, No 1 (Published)

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Original Research Article

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How to Cite

Abdel-Ghafar, H. M., Abdel-Aal, E. A., El-Sayed, D., & Hoinkis, J. (2021). Optimization of electrodialysis unit for partial desalination: Batch and continuous operation. Applied Chemical Engineering, 4(1), 1–8. https://doi.org/10.24294/ace.v4i1.479
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Optimization of electrodialysis unit for partial desalination: Batch and continuous operation

H. M. Abdel-Ghafar

Central Metallurgical Research and Development Institute (CMRDI)

E. A. Abdel-Aal

Central Metallurgical Research and Development Institute (CMRDI)

D. El-Sayed

Central Metallurgical Research and Development Institute (CMRDI)

J. Hoinkis

Karlsruhe University of Applied Sciences (HSKA)


DOI: https://doi.org/10.24294/ace.v4i1.479


Keywords: Electrodialysis, Partial Desalination, Potential Difference, Energy Consumption


Abstract

In recently few years, application of membrane technologies in sea water desalination is increased compared to other desalination technologies. Electrodialysis membrane technology is still limited in seawater desalination due to the high operation cost and its limitations for high salty water. Electrodialysis desalination cost is proportional to the amount of salt, which must be carried out through the membrane. Seawater desalination with high salt content of NaCl (42 g/L) was applied using IonTech electrodialysis unit. Partial desalination process was studied in two separate experiments, batch and continuous operation. Operation parameters like voltage applied, electrolyte concentration and time of desalination were studied under batch mode process. Continuous operation process was carried out to confirm the partial desalination process of electrodialysis. The limited current density is determined, 1.49 A/m2 and 1.15 A/m2 for theoretical and experimental, respectively. The specific energy consumption was calculated, 7.15 kWh/m3. 


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