current real measured numbers with the theoretical 0.66 cu in pump and the real 5.5" pulley are approx. 4 seconds at idle, 3.5 seconds at 1500 rpm and 3 seconds at 2000 rpm.
so somewhere it's pretty far off. 3.87 is basically 4, but is 2.9 at 1,000 rpm really comparable to 3.5 at 1500 rpm or 3 seconds at 2000 rpm? assuming that ~1700 shaft rpm is at or near all in on the regulation of the pump
My speculation is it's already getting flow regulated somewhere around 1k if it's really pushing 3.78gpm. With my testing today I was hoping to get a distinct feel for where the flow regulation is actually kicking in, but the numbers weren't fine enough to tell. Also note that I'm turning lock to lock with one hand and holding my phone as a stopwatch with the other, so assume my timing estimates are pretty loose.
Have you considered adding the extra hole in the fitting to increase idle flow?
Good to see people that get it, nice work. Since there is so much talk about pump displacements, here is what I have measured and know to be true to help you guys keep your numbers accurate:
- TC pumps: 0.64 in3 (10.5cc)
- SPX-1/CBR XR race pump: 0.67 in3 (11.3cc)
- Cast iron CB pumps including my CB-X series: 0.80 in3 (13.1cc)
- P pumps: 0.95 in3 (15.6cc)
- CBR pumps: Varies... I have found everything from 0.67in3 to 0.95in3 in the ones I have opened up including new and rebuilt PSC models
- "Trophy Truck" pumps (based on a Saginaw big bearing model referred to as P235 although they go by a few names): 1.22 in3 (20.0cc)
Good to see people that get it, nice work. Since there is so much talk about pump displacements, here is what I have measured and know to be true to help you guys keep your numbers accurate:
- TC pumps: 0.64 in3 (10.5cc)
- SPX-1/CBR XR race pump: 0.67 in3 (11.3cc)
- Cast iron CB pumps including my CB-X series: 0.80 in3 (13.1cc)
- P pumps: 0.95 in3 (15.6cc)
- CBR pumps: Varies... I have found everything from 0.67in3 to 0.95in3 in the ones I have opened up including new and rebuilt PSC models
- "Trophy Truck" pumps (based on a Saginaw big bearing model referred to as P235 although they go by a few names): 1.22 in3 (20.0cc)
I'm interested to see how the flow is at the higher RPM range when cavitation starts to ramp up and calculated displacement does not match actual. I would assume that it would be different for each systems plumbing style and restriction levels.
I'm interested to see how the flow is at the higher RPM range when cavitation starts to ramp up and calculated displacement does not match actual. I would assume that it would be different for each systems plumbing style and restriction levels.
edit2: just taking on some notes from Danfoss
Oil temperature Oil life will be drastically reduced because of oxidizing if the operating temperature exceeds 60 °C [140°F] for long periods. A rule of thumb is that oil life is halved for each 8 °C [46.4°F] in excess of 80 °C [176°F] . Impurities in the oil, e.g. particles or water, will further reduce its life.
min. rec'd oil temperature 86*F
viscosity rec'd 12-80 mm2/s = ISO 12 to 80, or ISO 15 to 68 to stay within limits oil grade
Oil temperature Oil life will be drastically reduced because of oxidizing if the operating temperature exceeds 60 °C [140°F] for long periods. A rule of thumb is that oil life is halved for each 8 °C [46.4°F] in excess of 80 °C [176°F] . Impurities in the oil, e.g. particles or water, will further reduce its life.
min. rec'd oil temperature 86*F
viscosity rec'd 12-80 mm2/s = ISO 12 to 80, or ISO 15 to 68 to stay within limits oil grade
and this is why crisbee1 recommended previously Mobil DTE 25 with it's fancy pants ISO 46
i've always been kind of curious what "too hot" actually is for hydraulic oil and such, temporary over 140 isn't bad, 180+ is bad, change the oil eventually. makes for a good reason to put a system together and run it for a bit while monitoring the temperature in, say the reservoir, and seeing what it is actually doing.
VISCOSITY CLASSIFICATIONS (premiumgrades.com)
ISO derivations.
you could, the extra cost would be adding in a bit more resistance for that valve. I honestly don't see much benefit for it though. you'd have all the extra cost and line's of going full external regulation with just a fraction of the benefit
To those in the know, what would be wrong with a gear pump with a bypass valve when it gets to XXXX PSI ?