@anchorsales I have a pump that can pump 10m3 of water per hour at a head
pump of 15 meters(flanges of 38 mm diameter for inlet and outlet). I want
to pump water through a serpentine with a length of 18 meters and 50
"elbows" of 90 degrees with a pipe diameter of 15 mm made of copper. Could
this pump do the job(pump at least 2 liters/minut) or the head pump is not
enough and the flow would stall before exiting the 18 meter pipe? Thank you
kindly!
do u know of any resources that will help me learn more of these priciples
.. i have a friend that has some positions open for applications engineer
and I have absolutely no experience or schooling in dealing with these
concepts.. but if i can get up to par I have a job waiting.. thnx for ur
input
Man, I've learned so much from this video. Wish my professor used this
style of approach, with the questions and the pacing and the conciseness. .
. Still struggling to wrap my brain around the reason for the answer of the
3 pump parallel question (18:40) and the plotting of afinity lines (my
textbook provides pump curve plots in the back but it's just the pump
curves for different impeller diameters and one efficiency curve, then of
course the NPSH and power curves on plots underneath).
+Randall Manteufel Thanks for the reply! Ok based off what you said, I think I'm now seeing that these 3 pumps in parallel must all be rotating on one single axle, thereby meaning each impeller shares the same RPM, thereby meaning that the maximum head that the system can reach is limited to the lowest head that one of the pumps can produce.Before, I was thinking of parallel pumps as being independent, like, say, the twin turbo setup on a Nissan 300zx.
+cbh148 hope this additional explanation helps: for the problem with 3 pumps in parallel, the weakest pump is capable of producing a maximum head (at zero flowrate) that is lower than the needed head, so don't use it. Thanks for your positive feedback.
12. System curve
How to plot a system curve and how to use it. www.pumpfundamentals.com.
What would happen to the system curve if you ran another length of pipe of
the exact same specifications parallel to it and used a WYE or TEE to
connect your pump to a common manifold right off the pump where it's output
could flow down both pipes. Would this flatten out the system curve for
more flow at same pressure? Would it be the square of the flows at each
pressure from your original system curve?
PV Diagrams
Overview of the types of thermodynamic processes and how they look in a PV diagram. Subscribe: https://www.youtube.com/user/ProfKeester.