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In a batch electro-electrodialysis (EED), sodium sulphate solution with an initial concentration of 80.90 g/dm3 was converted to obtain solutions of sodium hydroxide (13.96%) and sulphuric acid (10.15%) and a dialysate (3.23 g/dm3 of sulphate ions). Changes in the EED process′ performance (temperature, cell voltage, concentrations, energy consumption) with an increasing conversion degree of salt are presented. Based on the presented results of the batch experiment, conditions necessary to run the process continuously are discussed. A single pass method is inapplicable due to excessive heating of the electro-electrodialyser. A cascade method enables interstage cooling of the solutions, providing temperatures suitable for ion-exchange membranes to work. Increasing the number of stages in the cascade reduces both the number of electro-electrodialysers and specific electric energy consumption, providing the same production capacity. However, this increases the investment cost.
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Tom
Strony
54--58
Opis fizyczny
Bibliogr. 10 poz., rys., tab.
Twórcy
autor
- New Chemical Syntheses Institute, Inorganic Chemistry Division „IChN” in Gliwice, Sowińskiego 11, 44-101 Gliwice, Poland
autor
- New Chemical Syntheses Institute, Inorganic Chemistry Division „IChN” in Gliwice, Sowińskiego 11, 44-101 Gliwice, Poland
autor
- New Chemical Syntheses Institute, Inorganic Chemistry Division „IChN” in Gliwice, Sowińskiego 11, 44-101 Gliwice, Poland
autor
- New Chemical Syntheses Institute, Inorganic Chemistry Division „IChN” in Gliwice, Sowińskiego 11, 44-101 Gliwice, Poland
autor
- New Chemical Syntheses Institute, Inorganic Chemistry Division „IChN” in Gliwice, Sowińskiego 11, 44-101 Gliwice, Poland
autor
- New Chemical Syntheses Institute, Inorganic Chemistry Division „IChN” in Gliwice, Sowińskiego 11, 44-101 Gliwice, Poland
Bibliografia
- 1. Morachevskii, A.G. (1997). New lines in lead battery scrap recycling. Russ. J. Appl. Chem. 70(1), 1-12.
- 2. Pisarska, B., Mikołajczak, W., Jaroszek, H. & Nowak, M. (2016). Processing of sodium sulfate solutions by electro-electrodialysis method. Przem. Chem. 95(6), 1167-1170. (in Polish) DOI: 10.15199/62.2016.6.17.
- 3. Jörissen, J. & Simmrock, K.H. (1990). The behaviour of ion exchange membranes in electrolysis and electrodialysis of sodium sulphate. J. Appl. Electrochem. 21, 869-876. DOI: 10.1007/BF01042453.
- 4. Cherif, A.T. & Gavach, C. (1989). Electrotransport of sulfuric acid by electro-electrodialysis. J. Electroanal. Chem. 265, 143-157. DOI: 10.1016/0022-0728(89)80185-8.
- 5. Mani, K.N., Chlanda, F.P. & Byszewski, C.H. (1988). Aquatech Membrane Technology for Recovery of Acid/ Base Values from Salt Streams. Desalination 68, 149-166. DOI: 10.1016/0011-9164(88)80051-1.
- 6. Dylewski, R. (2000). Electrochemical methods in environmental engineering. Gliwice, Poland: Wydawnictwo Politechniki Śląskiej. (in Polish).
- 7. Pisarska, B., Mikołajczak, W., Jaroszek, H., Nowak, M. & Dylewski R. (2016). Effect of electro-electrodialysis on sodium sulfate conversion. Przem. Chem. 95(7), 1322-1324. (in Polish) DOI:10.15199/62.2016.7.8.
- 8. Paleologou, M., Thbault, A., Wong, P.Y., Thompson, R. & Berry, R.M. (1997). Enhancement of the current efficiency for sodium hydroxide production from sodium sulphate in a two-compartment bipolar membrane electrodialysis system. Sep. Purif. Technol. 11, 159-171. DOI: 10.1016/S1383-5866(97)00018-X.
- 9. Lide, D.R., ed. (2004). CRC Handbook of Chemistry and Physics (85th ed.). Boca Raton, USA: CRC Press.
- 10. Stopa, H., Baran, P., Gruszka, M., Markowicz, P., Pisarska, B., Dylewski, R., Cichy, B., Nowak, M., Jaroszek, H. & Mikołajczak, W. (2016). Polish Pat. appl. No. P.416 008.
Uwagi
Opracowanie ze środków MNiSW w ramach umowy 812/P-DUN/2016 na działalność upowszechniającą naukę (zadania 2017).
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Bibliografia
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