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...
Thank you for your response, I have found very valuable information in this site and it is the first time I ask for advice
My case is as following
I have an existing 2" tap where the gas consumption will increase in the near future
Minimum main pipeline operating pressure: 476 psig
Excepted...
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
