Designing Natural gas industrial users metering and regulating station, for years I have been using a rule I found in a Dresser meter brochure to determine the industrial design load. This rule considers a coincidence factor that decreases with the number of connected equipment. See below
Qty...
What is the maximum velocity that should be used to determine the diameter of a tap on a natural gas pipeline. We use 60 ft/sec as maximum velocity for the pipeline itself, Is there a diffrentet condition for the tap itself?
Thank you