Charles,
Had a question for you that I hope is not too much of a hijack,
I pulled up two compressor maps off of Bullseye' s sight that are probably close to what I'm thinking of using to make the same sort of pressures (roughly 70# boost).
Using a S476 primary and S258 secondary the PR numbers look great. The PRs are right in the sweet spot of both maps (If anything a little higher PR would be good on the secondary). Looking at the LBS/Min of air moved. it's roughly 70# for the primary stage (2.71 PR) and 40# for the secondary stage (2.13 PR)
Are the LBS/Min for 2 compounded chargers roughly additive? I have seen calculations where people started with desired horsepower and could make charger choices based on the amount of air required.
Thanks
You bring up a VERY good point. Something I have thought about myself a good bit,
especially when I was initially sizing my chargers as you seem to be doing now. Ask yourself this.... how can you have 70lbs/min coming down a pipe and then only have 40lbs/min going down that same pipe after it goes through another compressor? Where did the other 30lbs of air physically go? Are we to believe that over 360 cubic feet of air literally went poof and dissapeared? 30 lbs of substance went goodbye? Anyone familiar with the equation E = MC^2 can attest to the fact that we're talking about a LOOTTTA energy if that kind of mass just up and dipped out.
No matter how you slice it.... the second stage is moving
every bit as much mass flow as the first stage. No way around that, period. Unless your intercooler is a nuclear reactor anyway... This is because mass flow is always constant at all parts of the system from first stage inducer right to the intake manifold inlet (assuming no additional mass is added via water injection or similar). What is
not constant throughout is
Volume flow.
Which leads to the inevitable posting of a somewhat arrogant remark on my part...
The compressor maps are wrong.
Although it is
preached at you from all angles that mass flow (most often in lbs/min) is the
correct measure of compressor outflow, as you very well see for yourself, it's simply incorrect.
Here's my rationale:
The compressor moves an amount of air per rev @ ___rpm largely based on it's own size (holding blade design/shape constant). This holds true so well, that we even have competition classifications based solely on the inducer size of the compressor (2.6, 2.8, 3.0...). This is because a given compressor can only move as much air as it can physically "grab". For any given shaft speed I can't see any compelling reasons to believe that the wheel cares what the air density is. Now as density increases I could see that additional turbine power may be required to accelerate this denser media, but I don't see the wheel itself caring in terms of efficiency, or in terms of shaft speed required for a given volume flow.
The problem occurs when you notice that while your second stage map might stop abruptly at say 50 or so lbs/min, you may very well be pulling in 100+lbs/min across your first stage compressor. Being that mass flow is maintained (else physical laws be damned) you now have a serious conflict here.
In my mind, the solution is simple. This whole "mass flow is correct" deal, and the practice of producing compressor maps in units of mass flow is simply incorrect.
The first thing to do when you see a compressor map is to immediately convert it from mass flow to volume flow. Good old CFM units will prove very practical, and highly useful. I cannot say the same for mass flow units.
I can't explain how lbs/min is correct, when my GTP38R is moving around twice the maximum mass flow listed on it's map each and every day sitting just downstream of the GT47.
However..... you will find that the volume flow rates are SPOT ON! As this is what the wheel is
actually doing. Grabbing a given volume of air per rev @ ____ shaft rpm.
That's all I've got.