knapee
Petroleum
- Mar 9, 2011
- 100
Dear Sir/Madam
I tried to used HTRI to simulate the AES horizontal exchanger.
Condition :
1. The shell side inlet condition is vapor(39000kg/hr),
liquid (90000kg/hr) 60 degree C
2. The shell side outlet condition vapor 33000 kg/hr (decrease)
liquid 95000 kg/hr(increase), 40 degree C,
3 The tube side is cooling water 250000kg/hr,
inlet/30 degree C, outlet/40 degree C.
Although this type is phase change problems and no-tube-in-window (NTIW) design may be used
for vibration problems, I tried to rating this exchanger with single segmental
baffles type.
The warning message I got is attached in the mail and almost are Bundle, Shell Entrance vibration problem.
I tried to increase the shell side diameter and baffle spacing but in vain.
Could you please help me this trivial problem?
Thank you so much.
I tried to used HTRI to simulate the AES horizontal exchanger.
Condition :
1. The shell side inlet condition is vapor(39000kg/hr),
liquid (90000kg/hr) 60 degree C
2. The shell side outlet condition vapor 33000 kg/hr (decrease)
liquid 95000 kg/hr(increase), 40 degree C,
3 The tube side is cooling water 250000kg/hr,
inlet/30 degree C, outlet/40 degree C.
Although this type is phase change problems and no-tube-in-window (NTIW) design may be used
for vibration problems, I tried to rating this exchanger with single segmental
baffles type.
The warning message I got is attached in the mail and almost are Bundle, Shell Entrance vibration problem.
I tried to increase the shell side diameter and baffle spacing but in vain.
Could you please help me this trivial problem?
Thank you so much.