pita
Chemical
- May 31, 2000
- 2
We operate a continuous sodium hypo chlorite manufacturing plant. Caustic is circulated over a packed tower which is mounted directly to top of the recirc tank . Both vessels are PVC lined FRP. The PVC liner has suffered extensive corrosion after only 13 mnths operation. Corrosion on this duty is usual but 5 to 8 yr life is the norm. <br>Corrosion is generally in form of close spaced vertical grooving around the inside of the tank – above the main liquid level (there is no corrosion below liquid), similar but deeper than hydrogen grooving of carbon steel acid tanks. Preferential attack of welds is evident.<br>We believe the problem is associated with overchlorination, followed by decomposition, of the recirculating hypo/excess caustic solution. <br>We are trying to identify the corrosion mechanism: is it from heat of decomp and/or corrosive products formed after decomp? Also believe free radicals may be released in the above reactions - do these try to combine with the PVC? Can anyone help please?<br>