Corrosion of Lead-Acid Battery Electrodes in Sulphuric Acid
Corrosion of Lead-Acid Battery Electrodes in Sulphuric Acid
Corrosion of Lead-Acid Battery Electrodes in Sulphuric Acid
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solution. Thus, corrosion was more <strong>in</strong>tense <strong>in</strong> the oxygenated acid<br />
solution as compared with the deaerated acid solution.<br />
2- The corrosion potentials and the corrosion current densities changed<br />
considerably <strong>in</strong> the presence <strong>of</strong> the additives which <strong>in</strong>volved :-<br />
1, H3PO4 ( 11g dm -3 ),<br />
2, A mixture <strong>of</strong> ( H3PO4(11g dm -3 )+ FeSO4(0.2 g dm -3 )),<br />
3, NaCl (4 g dm -3 ) and ,<br />
4, FeSO4 (0.2 g dm -3 ).<br />
In the stirred and the un-stirred oxygenated 0.56M sulphuric acid solution<br />
<strong>in</strong> the temperature range (298-318)K us<strong>in</strong>g the follow<strong>in</strong>g work<strong>in</strong>g<br />
electrodes:<br />
1, lead alloy electrode,<br />
2, grid lead electrode,<br />
3, cured positive electrode, and ,<br />
4, cured negative electrode.<br />
Values <strong>of</strong> the corrosion potential (Ec) became more negative <strong>in</strong> the<br />
presence <strong>of</strong> H3PO4 and less negative with NaCl additives, the values <strong>of</strong> the<br />
corrosion current densities for all the electrodes were higher with NaCl<br />
and lower with H3PO4 <strong>in</strong> the both media.<br />
3- The protection efficiency (p%) was <strong>in</strong>vestigated for the additives <strong>in</strong><br />
the stirred and the un-stirred oxygenated 0.56M sulphuric acid<br />
solution. Maximum values <strong>of</strong> p% were atta<strong>in</strong>ed with H3PO4 and the<br />
m<strong>in</strong>imum with NaCl.<br />
4- Values <strong>of</strong> the thermodynamic quantities (DG, DW and DH) were<br />
estimated for the corrosion <strong>of</strong> the electrodes. DG values were more<br />
negative <strong>in</strong> the deaerated acid solution <strong>in</strong> the absence <strong>of</strong> additives. In the<br />
presence <strong>of</strong> the H3PO4, DG values were more negative while <strong>in</strong> the<br />
presence <strong>of</strong> NaCl the values were less negative <strong>in</strong>dicat<strong>in</strong>g a greater<br />
corrosion feasibility <strong>in</strong> the former and smaller <strong>in</strong> the latter cases. DW