Hello everyone,
Is there any design rule to define the internal diameter of HRSG Economizer headers?
In two reference Boilers books, I have found that the axial velocity inside the Economizer header should be less than 6 m/s?
I think there should be a minimum internal diameter to ensure...
Hello,
We are implementing the NB-27 A Guide for Blowoff Vessels in our Purge tanks desings, but I have a question for people who use this document.
For the calculation of the diameter of the vessel, you calculate first the requiered cross-sectional area (AR), using the mass flow rate of the...