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Affinity Laws For Centrifugal Pumps As Applicable To Variable Frequency Drives




Affinity Laws For Centrifugal Pumps As Applicable To Variable Frequency Drives Variable Frequency Drives (VFDs) or Variable Speed Induction Motors are frequently used in many applications for flow control through centrifugal pumps. One common factor associated with VFDs used for centrifugal pumps is rapidly changing flow to meet the process requirements and power savings at turndown flow rates where an oversized motor will provide poor motor efficiencies. In certain applications where very large volumetric capacities need to be pumped using a centrifugal pump the advantages of using a VFD become obvious and the payback period is typically less than 36 months. With costs related to solid-state electronics coming down over the years, utilizing VFDs for centrifugal pumps and fans gives large power savings for a relatively small change in speed according to the affinity laws and thus has become very attractive. For detailed understanding of the working of VFDs refer the "Wikipedia" article at the link provided below:

http://en.wikipedia....frequency_drive

If we say that a 3000 rpm motor is operating at the rated frequency of 60 Hz, then if we can vary the frequency from 30 to 90 Hz using a VFD the motor rpm could be varied from 1500 rpm to 4500 rpm.

However, centrifugal pump operations have limitations and cannot be operated for such a wide turn-down availabe from the driver or motor. The practical limit for deviation from the nameplate Brake Horse Power (BHP) is -50% and +5%. The following reasons can be attributed for the aforementioned limitations:

- Below 50% BHP rating the power factor and efficiency can deteriorate to unacceptable values

- Above 5% BHP rating the motor tends to "saturate" wherein the current rises to unpredictable and unacceptable levels.

Let us move on to the affinity laws. The following relationship exists for centrifugal pumps for frequency based on affinity laws and considering a rated frequency of 60 Hz

New Motor RPM = (New or Changed Frequency / 60 Hz)*Motor RPM at 60 Hz

New Flow Rate = (New or Changed Frequency / 60 Hz)*Flow rate at 60 Hz

New Differential Head = (New or Changed Frequency / 60 Hz)2*Differential Head at 60 Hz

New BHP = (New or Changed Frequency / 60 Hz)3*BHP at 60 Hz

Let us take an example. For a pump of 100 BHP operating at 60 Hz, the BHP corresponding to 30 Hz would be 12.5 hp and corresponding to 90 Hz would be 337.5 hp. As explained above the practical limit for operating the 100 bhp pump would be 50 hp and 105 hp which gives frequency values of 47.6 Hz and 61 Hz respectively.

Concluding this blog entry, VFDs have become an attractive option for power savings for rotary equipment in general and more so for centrifugal devices and design engineers should actively pursue the option of installing a VFD if the study provides good power savings and payback on capital investment for VFD.

Hoping to hear comments from all of you.

Regards,
Ankur.




Thank you very much for this valueable information.
Missed one point. TEFC motors should not go below 30% due to heat discipation. Most pumps use TEFC. Due the math on a smaller pump where the runout/curve could go to 1 hp and the motor becomes the limiting factor.

You can; however, notch them down with different motors (e.g. open) depending on their use. A Crane and a Conveyor Belt come to mind.
Greetings,

We are now in the process of installing many VFD controls for various processes of cooling and air compression.

With compression the signal source can be somewhat tricky if there is a needed minimum flow. Taking the signal from pressure may not always do the trick. We are exploring a dual signal operation for the compression where volume leads the pressure in order of importance.

Great posting.

Thanks

JO
Photo
sureshrajeshb
Nov 30 2012 11:53 AM
CAN WE USE VFD FOR RECIPORCATING PUMP ?
IF NO
WHY
sureshrajeshb,

You certainly can use VFD for reiprocating pump. But remember VFDs are expensive and if the function is continuously varying flow and very precise metering then only they can be justified.

If varibale flow and precision metering is not what you are looking for than manual (mechanical) stroke adjustment is sufficient for the reciprocating pump which is provided on the pump casing itself. The manual stroke adjustment will provide you a constant volume discharge for the given stroke setting.

Regards,
Ankur.

Dear Sir,

              i hv some issue about line sizing.in liquid line sizing velocity  8 ft/sec to 12 ft/sec is bst economical assumption but what for pump in and out line velocity criteria would be decided.

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