API 650, Appendix V, provides the normal operating external pressure range as 0.25 kPa (0.036 lbf/in2) to 6.9 kPa (1.0 lbf/in2). I understand API 620 tanks stipulates the maximum partial vacuum to be at least 1 in. wc. Is there an upper limit too on the design vacuum pressure for API 620 tanks?
|

Design Vacuum Pressure For Api 620 Tanks
Started by go-fish, Apr 24 2012 05:13 AM
3 replies to this topic
Share this topic:
#1
Posted 24 April 2012 - 05:13 AM
#2
Posted 24 April 2012 - 05:48 AM
go-fish,
No. Refer to API 620, sec.5.10.5.2 in which it is mentioned 1 ounce per square inch is the upper limit of partial vacuum for liquid storing. For storing gases or vapors alone, this standard doesn't contain provisions for design of relevant tanks may subject to partial vacuum.
Fallah
No. Refer to API 620, sec.5.10.5.2 in which it is mentioned 1 ounce per square inch is the upper limit of partial vacuum for liquid storing. For storing gases or vapors alone, this standard doesn't contain provisions for design of relevant tanks may subject to partial vacuum.
Fallah
#3
Posted 24 April 2012 - 08:24 AM
Does that mean for API 620 tanks storing liquids, the max. limit of vacuum (external pressure) is 4.3 mbar if my interpretation of 1 ounce per square inch vacuum is correct? However, I have seen in some previous projects, a design external pressure of 5 mbar on API 620 tanks storing hydrocarbon liquids. Is my interpretation correct or am I missing something?
Edited by go-fish, 24 April 2012 - 08:24 AM.
#4
Posted 25 April 2012 - 01:05 AM
go-fish,
I think 1 ounce per inch is almost equal to 5 mbar and then this value is the max limit of external pressure in tanks under API 620.
Fallah
I think 1 ounce per inch is almost equal to 5 mbar and then this value is the max limit of external pressure in tanks under API 620.
Fallah
Similar Topics
![]() Relief Path To Be Considered For Inlet Pressure Drop CalculationStarted by Guest_Ascanio E._* , 09 Jul 2025 |
|
![]() |
||
![]() Negative Pressure Discharge / Negative At High PointStarted by Guest_felderosfelder101021_* , 05 Jul 2025 |
|
![]() |
||
![]() Rupture Disc Failure Well Below Max PressureStarted by Guest_vaibhav02_* , 02 Jul 2025 |
|
![]() |
||
![]() Distillation Column Top PressureStarted by Guest_halkeshhulk_* , 27 Jun 2025 |
|
![]() |
||
Design Capacity Of Hydrogen Pullet During Hydroprocessing Units UpsetStarted by Guest_Divid Kelin_* , 18 Jun 2025 |
|
![]() |