1997
DOI: 10.1016/s1383-5866(97)00018-x
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Enhancement of the current efficiency for sodium hydroxide production from sodium sulphate in a two-compartment bipolar membrane electrodialysis system

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Cited by 65 publications
(28 citation statements)
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“…The current efficiency of a process is directly linked to proton leakage, ion leakage and equipment structure. This value of current efficiency is similar to the one obtained by Paleologou et al [25] with a two-compartment BMED process for the production of sodium hydroxide from sodium sulphate. However, these authors found that, for a sodium hydroxide concentration maintained at about 1 M in the basified compartment, the loss in current efficiency was 20%.…”
Section: Current Efficiency and Relative Energy Consumptionsupporting
confidence: 89%
“…The current efficiency of a process is directly linked to proton leakage, ion leakage and equipment structure. This value of current efficiency is similar to the one obtained by Paleologou et al [25] with a two-compartment BMED process for the production of sodium hydroxide from sodium sulphate. However, these authors found that, for a sodium hydroxide concentration maintained at about 1 M in the basified compartment, the loss in current efficiency was 20%.…”
Section: Current Efficiency and Relative Energy Consumptionsupporting
confidence: 89%
“…Alternatives to disposal have been developed, for instance production of Na 2 SO 4 and H 2 SO 4 by metathesis (Thompson et al, 1995), and production of NaOH and H 2 SO 4 by bipolar membrane electrodialysis, as discussed in detail by Paleologou et al (1997). Another potential option of H 2 SO 4 separation is the short-bed ion exchange process introduced by Bucher et al (2009), which enables the Na 2 SO 4 to be utilized in the pulping process and the sulfuric acid to be reused e.g.…”
Section: Recovery Boiler Esp Salt: Source Of Na and Smentioning
confidence: 99%
“…This process is favored for treatment of spent acidic solutions containing metal salts (such as metal pickling liquors) without any waste disposal needed as it produces both hydroxide for metal precipitation and regenerated acid to recirculate to the process [111][112][113]. BMED was also applied for the splitting of sodium sulfate [114,[115][116][117], sodium chloride [9,[118][119][120][121], sodium chlorate [122,123], sodium nitrate [124], sodium and potassium iodide salts [125], KF in the production of uranium fluoride [126] to treat nitrate wastewaters [127,128], spent caustics to regenerate NaOH [129,130] and to produce silica acid from sodium metasilicate [131]. However, despite lower energy requirements reported, BMED still possesses many of the disadvantages of EED/EM [132].…”
Section: Inorganic Acid and Base Production And Recoverymentioning
confidence: 99%