I have a possible problem with a condenser I have on a current project.
The Condenser is PED certified with notified body nameplate etc.
The nameplate states
Des. Temp. (Int/Ext)(TS Max) °C Shell Side 200 / 200 Tube side 80 / --
The problem I have is that in one case of coolant pump...
Hello All,
I am working on line sizing for the purpose of putting together a guideline and I have been looking at Darby's 3-K method as the 'latest and greatest'. Working out if it makes a significant impact over the various other methods is separate to this question I want to ask here.
The...
Background:
The project I am on is investigating the use of multi point ground flares (MPGF) for combusion of relief streams from cracker and aromatics units on a proposed chemical site. Maximum relief rates are of the order of 1000 tons per hour for emergency cases. Some cases include...
I am working on sizing a seawater intake sump. Design of teh sump itself according to HI standards has been systematic, but I have drawn a blank on the anticipated head loss across the travelling screen.
I have proposed two dual flow screens for the duty (28000 m3/h ) and I am hoping for a...
