Kathia Buena
Industrial
- Sep 3, 2023
- 6
Hello,
[ol 1]
[li]Client requested 8” WN flange nozzle Outlet, Flush-type shell connection.[/li]
[li]According to table 5.12b: h(height of opening) = 8 5/8” or 219,1 mm.[/li]
[li]5.7.8.4 g) says “The corroded thickness of the nozzle neck and transition piece, tn, shall be not less than 16 mm (5/8 in.)”.[/li]
[/ol]
If I use an 8” pipe as nozzle neck, in order to comply with 5.7.8.4 g), I would need to use an 8” sch 120 pipe (wall thickness = 18,26 mm), this would imply that h real = 219,1-(2x18,26) = 182,55 mm.
Would this application be correct, since h “opening height” would not be the value indicated in table 5.12b and figure attach?
Tank Data: D=16 m, H=12 m, Product: vegetal raw oil G=0,928
Regards,
KB
[ol 1]
[li]Client requested 8” WN flange nozzle Outlet, Flush-type shell connection.[/li]
[li]According to table 5.12b: h(height of opening) = 8 5/8” or 219,1 mm.[/li]
[li]5.7.8.4 g) says “The corroded thickness of the nozzle neck and transition piece, tn, shall be not less than 16 mm (5/8 in.)”.[/li]
[/ol]
If I use an 8” pipe as nozzle neck, in order to comply with 5.7.8.4 g), I would need to use an 8” sch 120 pipe (wall thickness = 18,26 mm), this would imply that h real = 219,1-(2x18,26) = 182,55 mm.
Would this application be correct, since h “opening height” would not be the value indicated in table 5.12b and figure attach?
Tank Data: D=16 m, H=12 m, Product: vegetal raw oil G=0,928
Regards,
KB