Pepijn1976
Petroleum
- Sep 17, 2012
- 2
Hello,
According to API 521 I'm trying to calculate if it is neccesary to install a thermal relief valve on a line that can be blocked in.
The line is made of carbon steel so I found the linear expansion coefficient and modulus of elasticity.
But I can't find any figures for the isothermal compressibility coefficient (don't have Lange's Handbook).
Does anyone have a figure for heavy nafta? Or, can tell me how to calculate this coefficient via API 521
API 521 gives an equation (5) on page 35: x= 1/v1*(v1-v2/(p2-p1).
v1 and v2 are specific volume = 1/density @ T. If I'm correct this value will always be negative (for expansion of a liquid by temperature).
What should I take for p1 and p2: I thought p1= initial pressure at start of blocked line and p2=pressure at max temperature due to solar heating (70°C).
Can someone help me on this?
Thanks in advance!
According to API 521 I'm trying to calculate if it is neccesary to install a thermal relief valve on a line that can be blocked in.
The line is made of carbon steel so I found the linear expansion coefficient and modulus of elasticity.
But I can't find any figures for the isothermal compressibility coefficient (don't have Lange's Handbook).
Does anyone have a figure for heavy nafta? Or, can tell me how to calculate this coefficient via API 521
API 521 gives an equation (5) on page 35: x= 1/v1*(v1-v2/(p2-p1).
v1 and v2 are specific volume = 1/density @ T. If I'm correct this value will always be negative (for expansion of a liquid by temperature).
What should I take for p1 and p2: I thought p1= initial pressure at start of blocked line and p2=pressure at max temperature due to solar heating (70°C).
Can someone help me on this?
Thanks in advance!