sheiko
Chemical
- May 7, 2007
- 422
Dear all,
I was wondering if you could help me clarify some ideas about compressible flow:
1/ Incompressible flow assumption:
I used to think that when the Mach number is below 0.3, one could use the incompressible flow equations when calculating pressure drop for compressible fluid flow (as shown in various books such as White F.M., "Fluid Mechanics", McGraw-Hill, 4th Ed., 1998).
But according the following sources we can read:
Reference 1: Green D.W., Perry R.H., "Perry's Chemical Engineers´Handbook", 8th Ed., 2008:
Compressibility effects are important when the Mach number exceeds 0.1 to 0.2. A common error is to assume that compressibility effects are always negligible when the Mach number is small. The proper assessment of whether compressibility is important should be based on relative density changes, not on Mach number.
Reference 2: Darby R., "Chemical Engineering Fluid Mechanics", 2nd Ed., 2001:
For gases, if the pressure change is such that the density does not change more than about 30%, the incompressible equation can be applied with reasonable accuracy by assuming the density to be constant at a value equal to the average density in the system.
Does this mean that the criteria based on Mach number should be considered as misleading?
2/ Sonic velocity definition
In various books such as reference 1 (see above), we can read that chocking occur in different conditions for isentropic and isothermal (i.e. chocking does not occur at Mach = 1 under isothermal conditions) and that sonic velocity is independent of the process, thus is unique. For ideal gas it can be approximated as c ~ sqrt(kRT/M).
With:
k = Cp/Cv
T = Temperature
R = Gas constant
M = Molecular weight
However, in the reference nº2 (see above), the author states that the speed of sound in an ideal gas is different for an isentropic process than for an isothermal process. Which would mean that, whatever the process conditions, chocking always occur at Mach 1. Thus,
- under isentropic conditions: c ~ sqrt(kRT/M).
- under isothermal conditions: c ~ sqrt(RT/M).
I think Dr Darby is correct. What about you?
For info., API Std 521 (Jan. 2007) has shown that by considering isothermal flow, the k factor should be ommited from the Mach number and critical pressure calculation (see "
Kind regards
"We don't believe things because they are true, things are true because we believe them."
"Small people talk about others, average people talk about things, smart people talk about ideas and legends never talk."
I was wondering if you could help me clarify some ideas about compressible flow:
1/ Incompressible flow assumption:
I used to think that when the Mach number is below 0.3, one could use the incompressible flow equations when calculating pressure drop for compressible fluid flow (as shown in various books such as White F.M., "Fluid Mechanics", McGraw-Hill, 4th Ed., 1998).
But according the following sources we can read:
Reference 1: Green D.W., Perry R.H., "Perry's Chemical Engineers´Handbook", 8th Ed., 2008:
Compressibility effects are important when the Mach number exceeds 0.1 to 0.2. A common error is to assume that compressibility effects are always negligible when the Mach number is small. The proper assessment of whether compressibility is important should be based on relative density changes, not on Mach number.
Reference 2: Darby R., "Chemical Engineering Fluid Mechanics", 2nd Ed., 2001:
For gases, if the pressure change is such that the density does not change more than about 30%, the incompressible equation can be applied with reasonable accuracy by assuming the density to be constant at a value equal to the average density in the system.
Does this mean that the criteria based on Mach number should be considered as misleading?
2/ Sonic velocity definition
In various books such as reference 1 (see above), we can read that chocking occur in different conditions for isentropic and isothermal (i.e. chocking does not occur at Mach = 1 under isothermal conditions) and that sonic velocity is independent of the process, thus is unique. For ideal gas it can be approximated as c ~ sqrt(kRT/M).
With:
k = Cp/Cv
T = Temperature
R = Gas constant
M = Molecular weight
However, in the reference nº2 (see above), the author states that the speed of sound in an ideal gas is different for an isentropic process than for an isothermal process. Which would mean that, whatever the process conditions, chocking always occur at Mach 1. Thus,
- under isentropic conditions: c ~ sqrt(kRT/M).
- under isothermal conditions: c ~ sqrt(RT/M).
I think Dr Darby is correct. What about you?
For info., API Std 521 (Jan. 2007) has shown that by considering isothermal flow, the k factor should be ommited from the Mach number and critical pressure calculation (see "
Kind regards
"We don't believe things because they are true, things are true because we believe them."
"Small people talk about others, average people talk about things, smart people talk about ideas and legends never talk."