CSM diesel
Engineer
- Joined
- Jun 1, 2007
- Messages
- 479
What?
What?
That is bass-akwards.
Mass flow is unchanging, measured in lbs/min. Mass of working fluid per unit time.
Volume flow is dependent, measured in CFM, m^3/s, etc. The measurement of which takes fluid density, friction, pressure, and flow regimes into account. Compressible flow makes this a little funny to deal with.
It is useless at these conditions. The conditions seen by the secondary pump are attributed to by the primary pump, which flows above and beyond what the second stage is capable of. So you are in a sense trying to plot something that is not possible by that particular pump at standard temp and PRESSURE.
The flow rates are not additive. For this to happen, the pumps would have to be hooked up in parallel, both working ends sharing the same discharge.
The big pump is pushing through the little one, and that is why we waste-gate around the little pump when it has done it part.
You are CORRECTING the flow of the pump using the pressure ratios supplied by the first stage.
You answered your own question to weather or not Mass flow is constant and volume flow is dependent with the statement above.
:ft:
You take the exact same scenario of shaft speed and PR that you tested before. Now only change two things, the pressure and temperature of the room in which the test is performed. Double the ambient temperature and double the ambient pressure and re-record your mass flow reading.
Do you suppose that the mass flow will be the exact same when the exact same shaft speed and PR are tested? As you stated that mass was constant and volume depended on pressure and temp?
Of course not. The reality is that mass flow would be around half what you recorded the first time, whereas the volume flow would still match what you had noted on test one.
What?
That is bass-akwards.
Mass flow is unchanging, measured in lbs/min. Mass of working fluid per unit time.
Volume flow is dependent, measured in CFM, m^3/s, etc. The measurement of which takes fluid density, friction, pressure, and flow regimes into account. Compressible flow makes this a little funny to deal with.
So help me out here...
However, as I have stated more than once in this thread, if mass is the correct unit of measure for compressor wheel flow performance, then why does the map become completely useless as soon as you begin dealing with a compressor working under non STP conditions, such as is the case with any second stage compressor?
It is useless at these conditions. The conditions seen by the secondary pump are attributed to by the primary pump, which flows above and beyond what the second stage is capable of. So you are in a sense trying to plot something that is not possible by that particular pump at standard temp and PRESSURE.
Or, another way of reasoning out this issue as I see it:
Having noted the max flow for each respective wheel as shown on their compressor maps, while my first stage compressor is capable of moving ~140lbs/min, my second stage is only capable of flowing ~72lbs/min max.
This should raise concern, I would hope. Because either one of two subsequent issues must be addressed in that case.
1. Is my second stage being operated at a point around two times the maximum value shown on it's compressor map at all times when I am running WOT in my truck? If so, what in God's name is the shaft speed at that time? Since ~72lbs/min occurs at a shaft speed of 110,000rpm, if I was fully utilizing my first stage compressor, and moving roughly twice that mass through the system, am I to assume that the second stage compressor is then approaching 200,000rpm? I think we can all rule that out right now.
2. If I pull in ~140lbs/min on the first stage, and the second stage is only capable of moving ~72lbs/min at max flow (so says the compressor map) then is it possible that close to 70lbs/min of atmosphere is consumed by the system somewhere between the first stage compressor inlet and the second stage compressor inlet? I don't think we need to delve into E = MC^2 to see the magnitude of nuclear reactor that would entail... So no, the mass is not disappearing between stages, so we still cannot explain how the second stage is moving roughly twice the max flow listed on it's map.
The flow rates are not additive. For this to happen, the pumps would have to be hooked up in parallel, both working ends sharing the same discharge.
The big pump is pushing through the little one, and that is why we waste-gate around the little pump when it has done it part.
This is only made more clear in the fact that the entire mess above, that is unexplainable (at least by me) in terms of mass flow maximum for a second stage wheel, is simultaneously Perfectly explained if the wheel is instead viewed in terms of volume flow. All of a sudden compressor flows make perfect sense, and plotting the operational point for the second stage goes from a point 8 inches to the right of the paper/screen to a point coincidentally right where you expected one to be. And coincidentally, right to a point where outlet temps and shaft speeds are right where they should have been all along.
You are CORRECTING the flow of the pump using the pressure ratios supplied by the first stage.
You answered your own question to weather or not Mass flow is constant and volume flow is dependent with the statement above.
:ft: