Compositepro
The car analogy may be simplistic, but it makes sense to me.
And please educate me where I am wrong. I want to learn more.
As I understand it, running at constant speed, the pump has a single curve it runs on (higher pressure at lower flow). This is dependent of course on other factors, but let's keep it simple. The system curve is based on piping, fittings, flow rate. Where they intersect is what determines the actual flow conditions which includes hydraulic efficiency. Choosing a pump where this point is maximizing the hydraulic efficiency is the ideal. Total efficiency includes both hydraulic and motor (electric) efficiencies.
So, if my design point is 100 gpm and 50 psig boost, but at times the actual flow required is 25 gpm, the system curve will change, but the pump curve will not. I know such a reduction in flow will likely be a big hit on the efficiency and the affinity laws don't like that, but it is real world (at least in my world). It will follow its curve to the new intersection, which will be a higher pressure. But, if i am required to stay below 80 psig (it is plumbing in my world) and my static head is around 30 psig, then I have to put in a PRV, throttling valve, etc. to keep the total pressure less than 80 psig. But I have now wasted that energy the constant speed motor is inputting to the impeller.
But, with the VFD, the pump slows, changing its curve and the intersection of the two curves is at a lower pressure and less energy being used.
I admit I am not knowledgeable about the electrical aspects of how the VFD works - I deal with the water in the pump. But if I put energy into pushing the water, but then throttle it back, how is that different than having your foot on the accelerator and brake at the same time. Wouldn't it be better to pull off the gas and run at a lower rpm?
Please tell me where I am wrong.