Hi,
I am new to this forum, can anyone point me in the right direction......?
I am trying to calculate the pressure surge of a fast closing valve to identify the pipe period in order to reduce the water hammer effect by increasing the flow stoppage rate. To do this I am using the Joukowski formula...... I have all the details I need but it has proven difficult to obtain the Bulk Modulus of elasticity of Liquid Natural Gas, LNG.
Does anyone know or know where I can find the Bulk modulus of elasticity of LNG?
Many Thanks
|

Bulk Modulus Of Elasticity Of Lng?
Started by Windswept, Jul 24 2012 03:48 AM
4 replies to this topic
Share this topic:
#1
Posted 24 July 2012 - 03:48 AM
#3
Posted 24 July 2012 - 06:38 AM
Windswept,
Refer the attachment for "Liquid Bulk Modulus" as a function of density and the liquid temperature.
Regards,
Ankur.
Refer the attachment for "Liquid Bulk Modulus" as a function of density and the liquid temperature.
Regards,
Ankur.
Attached Files
#4
Posted 24 July 2012 - 09:44 AM
Breizh,
Thank you for your reply, the thread was interesting although for LPG and not LNG.
Anuk,
The graph was a good indicator to quantify and value I finally managed to find,
This is what I found for interest or future reference: Bulk modulus of LNG 0.848 GPA @ -160 ºC
Many thanks
Windswept
Thank you for your reply, the thread was interesting although for LPG and not LNG.
Anuk,
The graph was a good indicator to quantify and value I finally managed to find,
This is what I found for interest or future reference: Bulk modulus of LNG 0.848 GPA @ -160 ºC
Many thanks
Windswept
#5
Posted 25 July 2012 - 01:09 AM
(isothermal) bulk modulus is the inverse of isothermal compressibility,
if you know (or can characterize) the composition any software capable to calculate isothermal compressibility can give accurate results, differently a generic value is the last resource.
Some software for fluid flow analysys requires only one value for bulk modulus not a table, for these cases I prefer to calculate several values of isothermal compressibility with Prode Properties then I select an average value (in the expected range of pressures and temperatures)
if you know (or can characterize) the composition any software capable to calculate isothermal compressibility can give accurate results, differently a generic value is the last resource.
Some software for fluid flow analysys requires only one value for bulk modulus not a table, for these cases I prefer to calculate several values of isothermal compressibility with Prode Properties then I select an average value (in the expected range of pressures and temperatures)
Similar Topics
Bulk Residence Time In Naphtha CrackingStarted by Guest_mehul_* , 19 Oct 2018 |
|
![]() |
||
Simulating A Liquid Mud Plant And A Dry Bulk PlantStarted by Guest_ebi4exploit_* , 07 Aug 2018 |
|
![]() |
||
![]() Particle Size Vs Bulk DensityStarted by Guest_sateeshkumar830_* , 20 Aug 2015 |
|
![]()
|
||
Bulk Bleach Delivery SystemStarted by Guest_Subject_Name_Here_* , 03 Jun 2016 |
|
![]()
|
||
![]() Recommended Valve Type For 32% Hydrochloric Acid Bulk Storage Main OutStarted by Guest_cravindran_* , 11 Nov 2015 |
|
![]()
|