For normal process PLANT design LIQUID pump discharges, look for velocities in the range 5-7 ft/sec. probably not a bad idea to keep design VAPOR velocities below 125 ft/sec. These guidelines might be applied by an engineering company for design. If you are looking at plant operation, it is common to find velocities in the 9-12 ft/sec range. EROSION problems can also complicate the answer to this question. Erosion is highly dependent on the nature of the fluid. For example, 98% FI2S04 is not corrosive to carbon steel pipe, however it very erosive at "normal design" velocities. Design criteria for 98% H2S04 might be 0.70 ft/sec MAXIMUM. However, it is also well known that if the same 98% FI2S04 has a little emulsified hydrocarbon, it is substantially LESS erosive.

For normal process plant design liquid pump discharges, look for velocities in the range 5-7 ft/sec. probably not a bad idea to keep design vapor velocities below 125 ft/sec. These guidelines might be applied by an engineering company for design. If you are looking at plant operation, it is common to find velocities in the 9-12 ft/sec range. Erosion problems can also complicate the answer to this question. Erosion is highly dependent on the nature of the fluid. For example, 98% FI2S04 is not corrosive to carbon steel pipe, however it very erosive at "normal design" velocities. Design criteria for 98% H2S04 might be 0.70 ft/sec MAXIMUM. However, it is also well known that if the same 98% FI2S04 has a little emulsified hydrocarbon, it is substantially less erosive.