The electro-electrodialysis process (EED) is used to generate H2SO4 and NaOH from sulphate sodium salt Na2SO4. The key phenomenon limiting the current efficiency of this process is the proton leakage through the anion selective membrane was not observed. The electro-electrodialysis was carried out with a three-compartment cell with two platinum-coated titanium electrodes separated by three compartments. The couple membrane used in this work is AFN and CMX. The experiments were carried out for four current densities 8.33 mA.cm-2 11.11mA.cm-2, 13.88mA.cm-2 and 27.77 mA.cm-2. For each current density, a voltage variation of cell and concentrations of H2SO4 and NaOH in the two compartments with the current density was used. The concentration of H2SO4 and NaOH increases with current density and with time, but higher for NaOH. The current efficiency increases with the current applied to the cell. The request for the electro-electrodialysis operation power was calculated in terms of the electrical energy consumed to produce H2SO4 and NaOH for 6 hours of electro-electrodialysis and it was found floating with the current applied and concentration sodium sulphate used and the concentration of H2SO4 and NaOH products, but is comparable for both initial concentrations of sodium sulfate.
Published in | American Journal of Applied Chemistry (Volume 1, Issue 4) |
DOI | 10.11648/j.ajac.20130104.15 |
Page(s) | 75-78 |
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), 2013. Published by Science Publishing Group |
Electro-Electrodialysis, Sodium Sulphate, Sulfuric Acid, Sodium Hydroxide
[1] | Stanisław Koter, Separation of weak and strong acids by electro-electrodialysis-Experiment and theory, Separation and Purification Technology 60 (2008) 251–258. |
[2] | A. T. Cherif, C. Gavach, T. Cohen, P. Dagard, and L. Albert, Hydrometallurgy 21 (1988) 191±201. |
[3] | Seong-Dae Hong, Jeong-Keun Kim, Byeong-Kwon Kim, Sang-Il Choi, Ki-Kwang Bae, Gab-Jin Hwang, Evaluation on the electro-electrodialysis to concentrate HI from HIx solutionby using two types of the electrode, International Journal of Hydrogen Energy 32 (2007) 2005 – 2009. |
APA Style
Noureddine. Zouhri, Said. Ait Habzize, Mahacine. El Amrani, Mohamed. Taky, Azzeddine. Elmidaoui. (2013). Generation of Sulfuric Acid and Sodium Hydroxide from the Sodium Sulphate Salt by Electro-Electrodialysis(EED). American Journal of Applied Chemistry, 1(4), 75-78. https://doi.org/10.11648/j.ajac.20130104.15
ACS Style
Noureddine. Zouhri; Said. Ait Habzize; Mahacine. El Amrani; Mohamed. Taky; Azzeddine. Elmidaoui. Generation of Sulfuric Acid and Sodium Hydroxide from the Sodium Sulphate Salt by Electro-Electrodialysis(EED). Am. J. Appl. Chem. 2013, 1(4), 75-78. doi: 10.11648/j.ajac.20130104.15
AMA Style
Noureddine. Zouhri, Said. Ait Habzize, Mahacine. El Amrani, Mohamed. Taky, Azzeddine. Elmidaoui. Generation of Sulfuric Acid and Sodium Hydroxide from the Sodium Sulphate Salt by Electro-Electrodialysis(EED). Am J Appl Chem. 2013;1(4):75-78. doi: 10.11648/j.ajac.20130104.15
@article{10.11648/j.ajac.20130104.15, author = {Noureddine. Zouhri and Said. Ait Habzize and Mahacine. El Amrani and Mohamed. Taky and Azzeddine. Elmidaoui}, title = {Generation of Sulfuric Acid and Sodium Hydroxide from the Sodium Sulphate Salt by Electro-Electrodialysis(EED)}, journal = {American Journal of Applied Chemistry}, volume = {1}, number = {4}, pages = {75-78}, doi = {10.11648/j.ajac.20130104.15}, url = {https://doi.org/10.11648/j.ajac.20130104.15}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajac.20130104.15}, abstract = {The electro-electrodialysis process (EED) is used to generate H2SO4 and NaOH from sulphate sodium salt Na2SO4. The key phenomenon limiting the current efficiency of this process is the proton leakage through the anion selective membrane was not observed. The electro-electrodialysis was carried out with a three-compartment cell with two platinum-coated titanium electrodes separated by three compartments. The couple membrane used in this work is AFN and CMX. The experiments were carried out for four current densities 8.33 mA.cm-2 11.11mA.cm-2, 13.88mA.cm-2 and 27.77 mA.cm-2. For each current density, a voltage variation of cell and concentrations of H2SO4 and NaOH in the two compartments with the current density was used. The concentration of H2SO4 and NaOH increases with current density and with time, but higher for NaOH. The current efficiency increases with the current applied to the cell. The request for the electro-electrodialysis operation power was calculated in terms of the electrical energy consumed to produce H2SO4 and NaOH for 6 hours of electro-electrodialysis and it was found floating with the current applied and concentration sodium sulphate used and the concentration of H2SO4 and NaOH products, but is comparable for both initial concentrations of sodium sulfate.}, year = {2013} }
TY - JOUR T1 - Generation of Sulfuric Acid and Sodium Hydroxide from the Sodium Sulphate Salt by Electro-Electrodialysis(EED) AU - Noureddine. Zouhri AU - Said. Ait Habzize AU - Mahacine. El Amrani AU - Mohamed. Taky AU - Azzeddine. Elmidaoui Y1 - 2013/11/20 PY - 2013 N1 - https://doi.org/10.11648/j.ajac.20130104.15 DO - 10.11648/j.ajac.20130104.15 T2 - American Journal of Applied Chemistry JF - American Journal of Applied Chemistry JO - American Journal of Applied Chemistry SP - 75 EP - 78 PB - Science Publishing Group SN - 2330-8745 UR - https://doi.org/10.11648/j.ajac.20130104.15 AB - The electro-electrodialysis process (EED) is used to generate H2SO4 and NaOH from sulphate sodium salt Na2SO4. The key phenomenon limiting the current efficiency of this process is the proton leakage through the anion selective membrane was not observed. The electro-electrodialysis was carried out with a three-compartment cell with two platinum-coated titanium electrodes separated by three compartments. The couple membrane used in this work is AFN and CMX. The experiments were carried out for four current densities 8.33 mA.cm-2 11.11mA.cm-2, 13.88mA.cm-2 and 27.77 mA.cm-2. For each current density, a voltage variation of cell and concentrations of H2SO4 and NaOH in the two compartments with the current density was used. The concentration of H2SO4 and NaOH increases with current density and with time, but higher for NaOH. The current efficiency increases with the current applied to the cell. The request for the electro-electrodialysis operation power was calculated in terms of the electrical energy consumed to produce H2SO4 and NaOH for 6 hours of electro-electrodialysis and it was found floating with the current applied and concentration sodium sulphate used and the concentration of H2SO4 and NaOH products, but is comparable for both initial concentrations of sodium sulfate. VL - 1 IS - 4 ER -