Yeah, but the trench is just 700 mm below grade as I understood. I do not have direct contact with the client, management has, so they take as a law whatever client pays for...I am more concerned about safety issues and how to design it. Yes, initial thought was to include a vertical section of...
Hi LittleInch: unfortunately, I do not have any more data than what is shown on P&ID. Plus I do not have datasheets of vessels. The main client concern is the splashing of a big volume of hot water liquid on the floor outdoor creating a potential hazard. So what you would propose as technical...
Hi LitteInch, you got me here....suction flange, not nozzle for the PSV. I was referring to nozzle at the BFW tank rather. But at 3am in the morning, you can excuse me for above. Anyway, the isometrics attached also explains what I meant by 5 m drop from the vessel, and also the PSV data sheet...
Hi Latexman: thanks for your reply.
I just attached the PID for a better visual of the system. Client wants to discharge not directly at grade but rather first in a tank, then in a drain trench...
There you can see the same info I specified above about the set pressure and elevation of...
Dear All,
Thank you in advance if you can guide me for a PSV (set at 300 kPag) sized for blocked discharge protecting a BFW deaerator designed at 250 kPag. The suction nozzle of PSV is at 5000 mm below the suction PSV lateral nozzle at the drum...Client complained that this PSV discharges at...
