|

Pressure Vessel Design
#1
Posted 05 March 2016 - 02:23 PM
#2
Posted 05 March 2016 - 02:55 PM
What is the design Temperature of 340F?
siham,
It means the pressure vessel is subject to maximum temperature of 340F which cannot be less than the relevant maximum operating temperature at all...
#3
Posted 05 March 2016 - 03:12 PM
340F is the operting pressure
l need to know how l can convert to design
#4
Posted 05 March 2016 - 03:19 PM
No fallah
340F is the operting pressure
l need to know how l can convert to design
siham,
Certainly you mean operating temperature (not operating pressure); then if so you can convert the operating temperature to design temperature by adding a reasonable margin, say 30F, to maximum operating temperature...
#5
Posted 05 March 2016 - 03:24 PM
Yes l mean that

But can you learn me how it com 30F
#6
Posted 05 March 2016 - 03:31 PM
tell me
How
And thank you alot
#7
Posted 05 March 2016 - 03:32 PM
Thank you
Yes l mean that
But can you learn me how it com 30F
siham,
It's based on the relevant project design criteria and might be more or less than what i mentioned as typical...
#8
Posted 05 March 2016 - 03:38 PM
say by add 50F
But he did not say why

#9
Posted 05 March 2016 - 03:41 PM
do you thike that we have any stander for T
#10
Posted 05 March 2016 - 03:42 PM
Our Dr
say by add 50F
But he did not say why
siham,
He might be a little bit conservative; but you can ask him to explain about the added value...
#11
Posted 05 March 2016 - 03:44 PM
Ok

Similar Topics
![]() Distillation Tower Top And Bottom Temperature And PressureStarted by Guest_student55_* , 27 Mar 2016 |
|
![]()
|
||
Steam Pressure In Heat ExchangerStarted by Guest_mvanrijnbach_* , 15 Apr 2025 |
|
![]() |
||
![]() Scrubber DesignStarted by Guest_nasss_* , 07 Aug 2024 |
|
![]() |
||
Critical Pressure For Choke Valve SizingStarted by Guest_Sherif Morsi_* , 07 Nov 2017 |
|
![]() |
||
Refinery Lpg Deethanizer Column DesignStarted by Guest_Ilyes_* , 15 Feb 2025 |
|
![]() |