Abstract
Corrosion of electrolytic tough‐pitch copper pipe was determined in aerated 2.1N sulfuric acid at 30°C. A closed loop circulating system was used, with 1 in., 3/4 in., and 1/2 in. diameter test sections. There was a gradual increase of corrosion rate with increasing Reynolds number in the laminar flow regime, ; a rapid increase in corrosion rate with increasing Reynolds number in the low turbulent flow regime, Re 2100 to 104; and a relatively constant corrosion rate due to polarization at . Reynolds number as a corrosion parameter permitted useful generalizations and comparisons with published heat and mass transfer correlations.
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