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Calculators

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Torque	0.00
HP
RPM

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HP Torque	0.00 0.00
GPM
TDH
EFF %
RPM

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GPM	0.00
HP
TDH
EFF %

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TDH	0.00
GPM
HP
EFF %

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EFF	0%
GPM
THD
HP

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$ / Day Annual OP Cost	0.00 0.00
TDH
$/KWH
EFF(pump) %
EFF(motor) %
GPM
Run Time/Day (hr)

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Q(CFS) DIA(IN) Q(GPM) HEAD(PSI)	0.0000 0.00 0.00 0.00
Area(FT)
Head(FT)
C

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Q(GPM) AREA(SF) Q(CFS) Q(GPD) HEAD(PSI)	0.00 0.000 0.00 0 0.00
DIA(IN)
Head(FT)
C

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Q(GPM) AREA(SF) Q(CFS) Q(GPD) HEAD(FT)	0.00 0.000 0.00 0 0.00
DIA(IN)
Head(PSI)
C

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HEAD LOSS	0.00
Length(FT)
(Q)GPM
C
DIA(IN)

C= 150 - PVC, 120 - ACP, 75 - CIP

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HEAD LOSS	0.0
Length(FT)
(Q)GPM
C
DIA(IN)
SHAFT O.D.(IN)

C= 150 - PVC, 120 - ACP, 75 - CIP

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VEL(F/S)	0.00
FLOW DIA.(IN)
Q(GPM)
I.D.(IN)

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SUCTION VELOCITY HEAD(FT) CALC. VELOCITY(FPS)	0.00 0.0
FLOW DIA.(IN)
Q(GPM)

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SPECIFIC SPEED(FT/SEC)	0.00
Q(GPM)
RPM
HEAD(FT)
NO OF STAGES/IMP

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SUCTION SPECIFIC SPEED(FT/SEC)	0.00
Q(GPM)
RPM
NPSHr(FT)

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VOL(GAL) WT(LB) VOL(CU FT)	0.00 0 0.00
O.D.(FT)
H OR L (FT)
I.D. (FT)

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Pump Suction Barrel (Type 1)

D(MIN)	0.00
Flow Rate (GPM)
d2 (IN)

General Notes:

1. Applications with flows greater than or equal to 3,000 GPM at normal operating conditions require a minimum of two flow straightening vanes centered on the inlet to the barrel and extending to the max. Water level or top of the barrel.

2. For applications without a basket type vortex suppressor having a solid bottom, vanes should extend across barrel bottom and an additional vane across barrel bottom at 90 degrees to other vane.

3. For barrels with inside dimensions physically too small to weld vanes to barrel I.D., attach vanes to pump.

4. We recommend a good basket type vortex suppressor on all barrel applications regardless of size or flow conditions.

5. Minimum five (5) X D pipe diameters straight run at suction inlet.

6. Velocity between barrel and pump should be less than 5 FPS.

Specific Notes:

A. Inlet velocity less than 4 ft/sec. vertical splitter place recommended in suction nozzle.

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Pump Suction Barrel (Type 2)

D(MIN)	0.00
Flow Rate (GPM)
d2 (IN)

General Notes:

2. For applications without a basket type vortex suppressor having a solid bottom, vanes should extend across barrel bottom and an additional vane across barrel bottom at 90 degrees to other vane.

3. For barrels with inside dimensions physically too small to weld vanes to barrel I.D., attach vanes to pump.

4. We recommend a good basket type vortex suppressor on all barrel applications regardless of size or flow conditions.

5. Minimum five (5) X D pipe diameters straight run at suction inlet.

6. Velocity between barrel and pump should be less than 5 FPS.

Specific Notes:

A. Inlet velocity less than 4 ft/sec. vertical splitter place recommended in suction nozzle.

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Pump Suction Barrel (Type 3)

D(MIN) h(MAX)	0.00 0.000
Flow Rate (GPM)
d2 (IN)

General Notes:

1. FOR BARRELS WITH INSIDE DIMENSIONS PHYSICALLY TOO SMALL TO WELD VANES TO BARREL I.D., ATTACH VANES TO PUMP.

2. WE RECOMMEND A GOOD BASKET TYPE VORTEX SUPPRESSOR ON ALL BARREL APPLICATIONS REGARDLESS OF SIZE OR FLOW CONDITIONS.

3. MINIMUM FIVE (5) X d1 PIPE DIAMETERS STRAIGHT RUN AT ALL SUCTION INLETS.

4. APPLICATIONS WITH FLOWS GREATER THAN OR EQUAL TO 3,000 GPM AT NORMAL OPERATING CONDITIONS REQUIRE A MINIMUM OF TWO FLOW STRAIGHTENING VANES CENTERED ON THE INLET TO THE BARREL AND EXTENDING FROM BARREL BOTTOM TO THE MAX. WATER LEVEL OR TOP OF THE BARREL.

5. FOR APPLICATIONS WITHOUT A BASKET TYPE VORTEX SUPPRESSOR HAVING A SOLID BOTTOM, VANES SHOULD EXTEND ACROSS BARREL BOTTOM AND AN ADDITIONAL VANE ACROSS BARREL BOTTOM AT 90 DEGREES TO OTHER VANE.

Specific Notes:

A. INLET VELOCITY LESS THAN 4 FT/SEC. VERTICAL SPLITTER PLATE RECOMMENDED IN SUCTION NOZZLE.

B. CAUTION: SOME SUCTION BELL BEARINGS PROTRUDE BELOW BELL.

C. FLOW VELOCITY BETWEEN PUMP O.D. AND BARREL I.D. SHOULD BE LESS THAN OR EQUAL TO 5 FT/SEC.

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Pump Suction Barrel (Type 4)

D(MIN) h(MAX)	0.00 0.000
Flow Rate (GPM)
d2 (IN)

General Notes:

2. For applications without a basket type vortex suppressor having a solid bottom, vanes should extend across barrel bottom and an additional vane across barrel bottom at 90 degrees to other vane.

3. For barrels with inside dimensions physically too small to weld vanes to barrel I.D., attach vanes to pump.

4. We recommend a good basket type vortex suppressor on all barrel applications regardless of size or flow conditions.

5. Minimum five (5) X D pipe diameters straight run at suction inlet.

6. Velocity between barrel and pump should be less than 5 FPS.

Specific Notes:

A. CAUTION: SOME SUCTION BELL BEARINGS PROTRUDE BELOW BELL

B. FLOW VELOCITY BETWEEN PUMP AND BARREL BOTTOM SHOULD BE GREATER THAN OR EQUAL TO 5 FPS.

Fill in the fields below and click the Calculate button to view the answer.

Pump Suction Barrel (Type 5)

D(MIN)	0.00
Flow Rate (GPM)
d2 (IN)

General Notes:

2. For applications without a basket type vortex suppressor having a solid bottom, vanes should extend across barrel bottom and an additional vane across barrel bottom at 90 degrees to other vane.

3. For barrels with inside dimensions physically too small to weld vanes to barrel I.D., attach vanes to pump.

4. We recommend a good basket type vortex suppressor on all barrel applications regardless of size or flow conditions.

5. Minimum five (5) X D pipe diameters straight run at suction inlet.

6. Velocity between barrel and pump should be less than 5 FPS.

Specific Notes:

A. WE RECOMMEND INLET VELOCITY LESS THAN 2 FT/SEC