The triethylene glycol (TEG) in the operated Bruce platform glycol dehydrator towers was
seen to steadily increase to over pH 10. This rise in pH was found to be attributable to the
carry over of triazine based H2S scavenger chemical, used to treat sour process gas. This
paper details the root cause failure analysis as well as the various mitigation strategies
researched and developed and the final field deployment.
High glycol pH increased the risk of process upsets because it had an affect on the resultant
gas dew point and therefore promoted concern over the dehydration efficiency at re-boiler
temperatures of 200°C. Further potential issues included foaming, regeneration efficacy,
solids precipitation and increased scale potential.