Billc wrote:You really have to look at the manufacturers specs. to really determine if the pump is over rated for the machine. In some cases a pump that is rated for 700 L/hr may only achieve 10 L/hr at 9 bar.
Very true and good point. Trying to bring my original comment to bear on your advice, I think
this document from Fluid-O-Tech paints a pretty accurate picture of your average espresso machine's rotary pump's ability to produce flow at pressure. This is for a compact F-O-T pump like the one found in the GS3. I believe the GS3 is an MA074, that is a 70 L/h brass pump with a balanced bypass valve mounted. This pump is a lower-flow pump than you'd see on your average machine, particularly multigroup ones, from what I've seen, but typical of smaller 1-group 'home' machines that sport rotary pumps, such as the QM Vetrano, La Spaziale S1, Izzo Alex, etc.

As the graph shows, the GS3 pump in the US (60 Hz AC/1725 rpm, C' on the graph) can output ~70 L/h @ 16 bars.A 150 L/h pump (again, US, E' on the graph) can put out ~170 L/h at 16 bars. As I said before, from what I understand of rotary pumps as they are used in the espresso machines, their potential flow is all but entirely untapped 99-100% of the time, and instead the balanced bypass on the pump (for the uninitiated, this is the screw with the lock-nut that points out at a 90° angle to the inlet line of the pump) regulates the pump so that it holds local pressure very roughly constant, at least at low output flow rates. In my experience, seems like you see a pump put out (upstream of the gicleur, as measured by a machine's pressure gauge) about 0.5 bars less pumping against 'nothing' (no portafilter in the group) vs. pumping with no flow (i.e. against a blind filter).
Of course, at the top of the puck is a whole other story, as you say, because things get more complicated when you put flow restrictors in a series and measure in between them and throw in the added curve ball that there's a transition from pumping a compressible medium (the air in the tube between the 3-way valve and the puck) to pumping a relatively incompressible medium (the water that pushes the air out). But it seems to me that appreciating and tweaking what's going on there is mostly a matter of changing your pump's bypass setting or changing the gicleur and/or your tamping/dosing/grinding. Changing your rotary pump's flow rating among the above doesn't seem likely to change much of this, as, again, every one of the pumps on the graph above is "spinning its wheels" to some degree or another when it's got its bypass at 9 bars and you're pulling a shot of espresso.
Getting back to the topic at hand, I'm pretty sure that if you get a Fluid-O-Tech or Procon pump rated for 30+ L/h, you will be able to brew espresso at one group at a time with no trouble at all. However, with those lower-flow pumps (I am thinking the 30-70, and maybe the 100), if the boiler autofill kicks in on you, or another barista flushes at another group during your shot, you will see a potentially large pressure drop on your shot. So the big multi-group machines put high-rated 150, 175 L/h pumps on their machines. So, your minimum is going to depend on the number of groups that your machine has, and to some extent whether you expect the autofill on the steam boiler to ever kick in during the shot (some nice espresso machines have controls that prevent this).
What I really have a poor handle on is "how much is too much?" I would think it'd be the point where the flow rate of the pump was so high that you couldn't set the bypass to hold as low as 9 bars during operation where the net output is ~3 mL/sec. I don't know at what point a rotary pump does that, but I'd guess a 100 gph pump might work, *if* it has a balanced bypass valve on it. If you don't have a bypass, don't even bother. If you have a 'regular' bypass, I think those work but are a lot more sensitive to inline pressure fluctuations, which might make a huge difference with a pump like that. The other thing that I can see being a real problem is cavitation. If you have a filter or some narrow tubing upstream that is rated for less than what the pump wants to put out (not necessarily its 'rating' so much as the output rates that it sustains at the pressure you set it to and the rate it can push through the fattest opening it's pushed out of, usually the steam boiler fill line), you risk cavitation. Seems like a bad idea that can damage things.
Does that sound right, Bill? That's what I've gleaned from my own tinkering, looking at these graphs, and talking to EricS and rotary pump vendors in conjunction with the
pressure profiling project. Apologies to the OP if this is way more technical than you were looking for...