Preface
We have written this book to help provide you, the user of a WGI reciprocating pump, with the knowledge of how a reciprocating pump works and guidance in your selection and operation of a reciprocating power pump. For specific recommendations which are not covered within, please contact our applications department and provide them with all pertinent information regarding your pumping application.
Thanks to all the persons and companies who have provided reference material used in this book. Our further thanks and acknowledgment is extended to the "Hydraulic Institute", for their section on Hydraulic Institute Standards - Reciprocating Pumps, Power (Types, Nomenclature, Ratings, and Applications).
We sincerely hope this book will give you some insight into how your reciprocating pump works and why reciprocating pumps are still one of the most efficient and effective way of transporting liquids of all types.
Although all the information in this book generally applicable to all reciprocating pumps, the specific data within applies only to WGI pumps.
Wheatley Gaso Inc. (WGI)
Tulsa, Oklahoma, USA
Updated 10-10-96
Introduction
We believe the commonly accepted conventional nomenclature and descriptions of liquid supply systems for reciprocating pumps is often misleading and provides an inaccurate description of the pumping action. This nomenclature often describes attributes of the pump which do not exist. Intellectually, we all understand the conventional notations and descriptions, however the concept of the pump being a machine which takes action on a liquid often confuses and deceives the intellect into believing that the pump has control over the amount of liquid being introduced into the pump.
The pump relies upon outside forces to push the liquid through the inlet manifold and inlet valve into the liquid chamber of the pump. The pump cannot pull the liquid into the liquid chamber as there is no tensile strength to the liquid. The pump merely creates a partial vacuum in the liquid chamber which is then filled by the forces acting upon the liquid on the inlet side of the pump.
Also, please remember when reading this manual, that liquids remain liquids only so long as outside pressure remains high enough to keep the liquid from boiling. If the pressure on the liquid is reduced below the pressure at which the liquid boils at the pumping temperature, the liquid changes to its vapor state and is no longer a liquid. It is the responsibility of the liquid supply system to provide liquid to the pump inlet at sufficient pressure to keep the liquid from boiling during the pumping cycle. Doing this will prevent many dollars from being spent on repair of the pump, the supply system, and the discharge system.
This manual is not intended to solve all the problems which come up in applications involving WGI reciprocating pumps. We do hope it does provide enough insight to allow the reader to place the action of a reciprocating pump in its proper perspective.
Table of Contents
I. Warnings and Precautions Before and After Starting a WGI Reciprocating Pump 1
A. Safety Precautions 1
B. Warnings before starting a reciprocating pump 1
C. Warnings after starting a reciprocating pump 3
II. Fundamentals of Operation 4
A. How a reciprocating Pump Works 4
B. Plunger or Piston Rod Load 4
C. Calculations of Volumetric Efficiency 5
D. Horsepower Calculations 8
E. Devices for Liquid Pulsation Control - Suction and Discharge 12
III. Pump Material Selection 13
A. Plunger Pumps 13
B. Piston Pumps 15
IV. Pump Applications 17
A. Types of Reciprocating Pumps 17
B. Where Reciprocating Pumps are Used 17
C. Sizing and Selecting a Reciprocating Pump 17
D. Pump Storage 18
E. Sizing a Pump for High Suction Pressure Conditions 20
V. Supply System Considerations 21
A. Pressure 21
B. Head 21
C. Viscosity 22
D. Frictional Head Losses 22
E. Reynolds Number 22
F. Acceleration Head 23
G. NPSHR (Net Positive Suction Head Required) 25
H. NPSHA (Net Positive Suction Head Available) 25
I. Pump Cavitation 25
J. Liquid supply System Relationships 26
VI. Installation Suggestions 39
A. Supply System Piping Design 39
B. Discharge Piping Design 39
C. Recommended Safety Devices 40
VII. Trouble Locating of Reciprocating Pumps 41
VIII. Appendix
A. Reciprocating Pumps (Hydraulic Institute, 14th Edition 1983) A1..A39
B. Reciprocating Pump Flow Characteristics B1
C. Equivalent Length in feet of 100 % Opening Valves and Fittings C1
D. Pressure Drop in Liquid Lines D1
E. Vapor/Saturation Pressure of Water E1
F. Data Required by Pump Manufacturers for Proper Selection of Material F1..F2
G. Conversion Factors G1..G4
h. Useful Formulas H1..H2
i. Preventive Maintenance Schedule for Reciprocating Pumps I1..I2
ix. index & Bibliography ix1..ix4
You will want to look your pump over very carefully and get acquainted with the pump prior to starting. Also refer to "Operating Instructions and Maintenance Suggestions" or "Operators Manual" published by WGI for the specific pump type and model.
I. WARNINGS AND PRECAUTIONS BEFORE AND AFTER STARTING A WGI RECIPROCATING PUMP.
A. Safety Precautions
1. Never start or operate a pump against a closed discharge line. Catastrophic destruction of piping or pump will promptly occur.
2. Avoid starting against a full discharge load. Bring pump up to speed using a bypass, then gradually place pump on line.
3. Bleed air from pump and piping before starting pump.
4. The cradle cover must be in place while pump is running.
5. Stand clear of pump while operating under pressure.
6. Do not operate pump above "maximum design pressure" indicated on metal tag. Operating above the maximum design pressure will result in damage to pump, person or property. Notify WGI at the first sign of a suspected malfunction.
7. Contact WGI immediately if operating conditions or type of service change. Upon request you can receive recommendations to meet the new specifications and a new application tag can be sent.
B. Warnings
Before starting a WGI reciprocating pump.
1. Packing for piston and plunger pumps:
a. Piston Pumps - Piston pump stuffing boxes are not packed when shipped from the factory. These pumps must be packed before starting. If the pump is to be placed in storage before use, the piston rods should be coated with grease to prevent rusting. See the Pump Storage section for other steps to take before placing pump in storage.
b. Plunger Pumps - These pumps are packed prior to shipment for immediate service. If temporary storage is intended, the plunger must be protected by taking the following steps: rotate the crankshaft slightly more than one revolution, and apply a film of oil to each plunger surface as the plunger moves out of and into the stuffing box packing. Change the position of the plungers periodically/or at least once a week and reapply oil onto each plunger. These steps will help prevent pitting of the plunger from chemical reactions between the packing and the metal surface of the plunger, during periods of inactivity. See Pumps Storage section for more information.
2. Crankcase has been drained by WGI before shipping pump to you. Fill with lubricant as recommended by operating instructions to ensure proper lubrication of gears, chain, crossheads, connecting rods and shaft bearings. Then rotate the crankshaft by hand at least once a week until starting in order to avoid rust formation from water condensation on unpainted internal parts. Shaft bearings requiring a separate oil bath have been filled at factory with recommended lubricant but should be checked for proper oil level before starting. Check oil levels daily. Change lubricant at least every six months. Drain and thoroughly flush the crank case and bearing housings when making this change.
3. Pump must set level for proper lubrication and alignment.
4. Read Operating Instructions and Maintenance Suggestions or Operator Manual for the specific pump model. If misplaced or lost, please contact your nearest WGI distributor or contact WGI direct for a copy.
5. A pressure relief valve must be installed in the discharge piping between the pump and any other pipe fittings. See page 40 set pressure suggestions.
6. All belt and coupling guards must be firmly in place.
7. Be sure that all pipe joints and fasteners are definitely tight before putting the pump into operation.
8. Check connecting rod bearings for proper adjustment - according to operating instructions.
9. Check main bearings for proper adjustment - according to operating instructions.
C. Warnings
After starting a WGI reciprocating pump.
1. New non-adjustable lip type packing rings (plunger pumps only) may be expected to leak slightly for a day or so, but will gradually seat. The packing gland must be retightened and periodically checked after the packing has seated.
DO NOT attempt to adjust packing while pump is running.
2. Piston pump packing is available in several different configurations. All are adjustable type packing. Care must be taken to ensure that this packing is not overtightened. On most installations, a very slight drip is desirable to aid in lubrication and as visual proof that the packing is not too tight.
3. After Two (2) Hours Operation (also refer to Appendix I)
a. Check all the crank end connecting rod bearings for proper adjustment. Check connecting rod bolt nut torque and adjust if necessary.
b. Check lubricant level and pressure gauge (if forced lubrication system is furnished).
II. FUNDAMENTALS OF OPERATION
A. How a reciprocating pump works
A reciprocating pump is a positive displacement mechanism, liquid discharge pressure being limited only by the strength of the structural parts. Liquid volume or capacity delivered is constant regardless of pressure, and is varied only by driver speed, speed reduction, and/or plunger/piston size changes.
Reciprocating motion is imparted to a plunger/piston by a slider crank linkage which results in a piston motion closely approximating simple harmonic motion, as shown in Appendix B. This reciprocating motion alternately lowers the pressure in front of the plunger/piston when filling the pump, and increases the pressure when emptying the pump. The incoming liquid opens the suction/inlet valve. At the same time the discharge valve is held closed by the downstream line pressure. Outgoing liquid closes the inlet valve and opens the discharge valve. This simple mechanism provides high volumetric efficiency, approximately 95 percent, for most incompressible liquids.
Characteristics of a WGI reciprocating pump are;
(a) positive liquid displacement
(b) high pulsations caused by the sinusoidal motion of the plunger/piston
(c) high volumetric efficiency
(d) high mechanical efficiency
(e) low pump maintenance cost
B. Plunger or Piston Rod Load
Plunger or piston rod load is an important power end "design" consideration for WGI reciprocating pumps. Rod load is the force caused by the liquid pressure acting on the face of the plunger/piston. This load is transmitted through the adapter or piston rod to the crosshead, then to the crosshead pin, wrist pin bushing, connecting rod, crank shaft, main bearings and power frame. This load is directly proportional to the discharge gauge pressure and the square of the plunger/piston diameter.
Occasionally, allowable liquid end pressures limit the "allowable" rod load to a value below the "design" rod load. It is important that liquid end pressure DOES NOT exceed WGI's latest published recommendations.
Rod loads are not generally used when "applying" the pump. They are used to establish the power frame design - not to determine the allowable pressures, in most cases, for each size plunger/piston.. Also see the Sizing pumps in high inlet pressure conditions section.
C. Calculations of Volumetric Efficiency
Volumetric Efficiency (EV) is defined as the ratio of actual pump capacity to ideal pump displacement. The EV calculation depends upon the internal configuration of each individual liquid end cylinder, plunger/piston size, and the liquid being pumped. Given full details regarding differential pressure, pumped liquid mixture, and expected temperature rise on the discharge stroke - WGI can calculate this efficiency.
1. Calculating EV for Water
See TABLE 4 Page A31 for the water compressibility chart. An example of volumetric efficiency calculation for water is also shown.
2. Calculating EV for Hydrocarbons
See TABLE 6 Page A34 for the physical properties of hydrocarbons. For compressible liquids such as these, horsepower calculations are slightly more complex than for incompressible liquids. However, the magnitude of the horsepower required will be slightly less than if calculated for the full displacement.
3. Displacement TableTable 1 can be used to determine pump displacement and whether or not the proper efficiency is being obtained.
Example 1:Find the capacity (Q), in Barrels Per Hour (BPH), for a single acting 3-1/2" x 4" triplex plunger pump operating at 95% volumetric efficiency (Ev ) and a speed of 350 rpm.
From TABLE 1 a 3-1/2" plunger with a 4" stroke will displace
0.167 gallons per stroke. This type of pump will displace liquid at a rate of 3 forward
strokes only per revolution. Therefore, the displacement per revolution is 0.167
gal./stroke x 3 strokes/rev. = 0.501 gal./rev. (gpr). At 350 rpm, the total displacement
is 175.35 gallons per minute (GPM). Dividing by 0.7 gives 250.5 BPH displacement (D).
Therefore, the pump capacity at a 95% volumetric efficiency is
Q = D Ev = 250.5 (95)
(100) (100)
Q = 237.9 BPH
Displacement Table |
|||||||||||
Plunger |
Plunger |
Stroke Length - inches |
|||||||||
Diameter |
Area |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
12 |
Displacement per Stroke - U.S. Gallons or Decimal Parts Thereof |
|||||||||||
inches |
sq. inches |
||||||||||
0.500 |
0.196 |
0.002 |
0.003 |
0.003 |
0.004 |
0.005 |
0.006 |
0.007 |
0.008 |
0.009 |
0.010 |
0.625 |
0.307 |
0.003 |
0.004 |
0.005 |
0.007 |
0.008 |
0.009 |
0.011 |
0.012 |
0.013 |
0.016 |
0.750 |
0.442 |
0.004 |
0.006 |
0.008 |
0.010 |
0.011 |
0.013 |
0.015 |
0.017 |
0.019 |
0.023 |
0.875 |
0.601 |
0.005 |
0.008 |
0.010 |
0.013 |
0.016 |
0.018 |
0.021 |
0.023 |
0.026 |
0.031 |
1.000 |
0.785 |
0.007 |
0.010 |
0.014 |
0.017 |
0.020 |
0.024 |
0.027 |
0.031 |
0.034 |
0.041 |
1.125 |
0.994 |
0.009 |
0.013 |
0.017 |
0.022 |
0.026 |
0.030 |
0.034 |
0.039 |
0.043 |
0.052 |
1.250 |
1.227 |
0.011 |
0.016 |
0.021 |
0.027 |
0.032 |
0.037 |
0.043 |
0.048 |
0.053 |
0.064 |
1.375 |
1.485 |
0.013 |
0.019 |
0.026 |
0.032 |
0.039 |
0.045 |
0.051 |
0.058 |
0.064 |
0.077 |
1.500 |
1.767 |
0.015 |
0.023 |
0.031 |
0.038 |
0.046 |
0.054 |
0.061 |
0.069 |
0.077 |
0.092 |
1.625 |
2.074 |
0.018 |
0.027 |
0.036 |
0.045 |
0.054 |
0.063 |
0.072 |
0.081 |
0.090 |
0.108 |
1.750 |
2.405 |
0.021 |
0.031 |
0.042 |
0.052 |
0.062 |
0.073 |
0.083 |
0.094 |
0.104 |
0.125 |
1.875 |
2.761 |
0.024 |
0.036 |
0.048 |
0.060 |
0.072 |
0.084 |
0.096 |
0.108 |
0.120 |
0.143 |
2.000 |
3.142 |
0.027 |
0.041 |
0.054 |
0.068 |
0.082 |
0.095 |
0.109 |
0.122 |
0.136 |
0.163 |
2.125 |
3.547 |
0.031 |
0.046 |
0.061 |
0.077 |
0.092 |
0.107 |
0.123 |
0.138 |
0.154 |
0.184 |
2.250 |
3.976 |
0.034 |
0.052 |
0.069 |
0.086 |
0.103 |
0.120 |
0.138 |
0.155 |
0.172 |
0.207 |
2.375 |
4.430 |
0.038 |
0.058 |
0.077 |
0.096 |
0.115 |
0.134 |
0.153 |
0.173 |
0.192 |
0.230 |
2.500 |
4.909 |
0.043 |
0.064 |
0.085 |
0.106 |
0.128 |
0.149 |
0.170 |
0.191 |
0.213 |
0.255 |
2.625 |
5.412 |
0.047 |
0.070 |
0.094 |
0.117 |
0.141 |
0.164 |
0.187 |
0.211 |
0.234 |
0.281 |
2.750 |
5.940 |
0.051 |
0.077 |
0.103 |
0.129 |
0.154 |
0.180 |
0.206 |
0.231 |
0.257 |
0.309 |
2.875 |
6.492 |
0.056 |
0.084 |
0.112 |
0.141 |
0.169 |
0.197 |
0.225 |
0.253 |
0.281 |
0.337 |
3.000 |
7.069 |
0.061 |
0.092 |
0.122 |
0.153 |
0.184 |
0.214 |
0.245 |
0.275 |
0.306 |
0.367 |
3.250 |
8.296 |
0.072 |
0.108 |
0.144 |
0.180 |
0.215 |
0.251 |
0.287 |
0.323 |
0.359 |
0.431 |
3.500 |
9.621 |
0.083 |
0.125 |
0.167 |
0.208 |
0.250 |
0.292 |
0.333 |
0.375 |
0.417 |
0.500 |
3.750 |
11.045 |
0.096 |
0.143 |
0.191 |
0.239 |
0.287 |
0.335 |
0.383 |
0.430 |
0.478 |
0.574 |
4.000 |
12.566 |
0.109 |
0.163 |
0.218 |
0.272 |
0.326 |
0.381 |
0.435 |
0.490 |
0.544 |
0.653 |
4.250 |
14.186 |
0.123 |
0.184 |
0.246 |
0.307 |
0.368 |
0.430 |
0.491 |
0.553 |
0.614 |
0.737 |
4.500 |
15.904 |
0.138 |
0.207 |
0.275 |
0.344 |
0.413 |
0.482 |
0.551 |
0.620 |
0.689 |
0.826 |
4.750 |
17.721 |
0.153 |
0.230 |
0.307 |
0.384 |
0.460 |
0.537 |
0.614 |
0.690 |
0.767 |
0.921 |
5.000 |
19.635 |
0.170 |
0.255 |
0.340 |
0.425 |
0.510 |
0.595 |
0.680 |
0.765 |
0.850 |
1.020 |
5.250 |
21.648 |
0.187 |
0.281 |
0.375 |
0.469 |
0.562 |
0.656 |
0.750 |
0.843 |
0.937 |
1.125 |
5.500 |
23.758 |
0.206 |
0.309 |
0.411 |
0.514 |
0.617 |
0.720 |
0.823 |
0.926 |
1.029 |
1.234 |
5.750 |
25.967 |
0.225 |
0.337 |
0.450 |
0.562 |
0.674 |
0.787 |
0.899 |
1.012 |
1.124 |
1.349 |
6.000 |
28.274 |
0.245 |
0.367 |
0.490 |
0.612 |
0.734 |
0.857 |
0.979 |
1.102 |
1.224 |
1.469 |
6.250 |
30.680 |
0.266 |
0.398 |
0.531 |
0.664 |
0.797 |
0.930 |
1.063 |
1.195 |
1.328 |
1.594 |
6.500 |
33.183 |
0.287 |
0.431 |
0.575 |
0.718 |
0.862 |
1.006 |
1.149 |
1.293 |
1.437 |
1.724 |
6.750 |
35.785 |
0.310 |
0.465 |
0.620 |
0.775 |
0.929 |
1.084 |
1.239 |
1.394 |
1.549 |
1.859 |
7.000 |
38.485 |
0.333 |
0.500 |
0.666 |
0.833 |
1.000 |
1.166 |
1.333 |
1.499 |
1.666 |
1.999 |
7.250 |
41.283 |
0.357 |
0.536 |
0.715 |
0.894 |
1.072 |
1.251 |
1.430 |
1.608 |
1.787 |
2.145 |
7.500 |
44.179 |
0.383 |
0.574 |
0.765 |
0.956 |
1.148 |
1.339 |
1.530 |
1.721 |
1.913 |
2.295 |
7.750 |
47.173 |
0.408 |
0.613 |
0.817 |
1.021 |
1.225 |
1.429 |
1.634 |
1.838 |
2.042 |
2.451 |
8.000 |
50.266 |
0.435 |
0.653 |
0.870 |
1.088 |
1.306 |
1.523 |
1.741 |
1.958 |
2.176 |
2.611 |
8.250 |
53.456 |
0.463 |
0.694 |
0.926 |
1.157 |
1.388 |
1.620 |
1.851 |
2.083 |
2.314 |
2.777 |
8.500 |
56.745 |
0.491 |
0.737 |
0.983 |
1.228 |
1.474 |
1.720 |
1.965 |
2.211 |
2.457 |
2.948 |
8.750 |
60.132 |
0.521 |
0.781 |
1.041 |
1.302 |
1.562 |
1.822 |
2.083 |
2.343 |
2.603 |
3.124 |
9.000 |
63.617 |
0.551 |
0.826 |
1.102 |
1.377 |
1.652 |
1.928 |
2.203 |
2.479 |
2.754 |
3.305 |
Example 2:
Find the rpm (n) required for a single acting 3" x 5" triplex plunger pump
operating at EV = 85% and capacity (Q) = 200 BPH.
D = displacement = Q (100)
Ev
D = 200 = 235.29 BPH
0.85
gpr = (0.153 gal./stroke) (3 strokes/rev.)
gpr = 0.459
GPM = BPH x 0.7 = 235.29 x 0.7
GPM = 164.7
At the given displacement and volumetric efficiency, the pump speed (n) is
n = GPM = 164.7 rpm gpr 0.459
n = 358.8 rpm
Note 1: One barrel equals 42 U.S. gallons. Gallons per minute (GPM) divided by 0.7 equals barrels per hour (BPH). Displacement is the ideal volume swept by the plunger or piston on the discharge stroke during any selected time period.
Note 2: Under the conditions and definitions given above, the pump must run at a higher rpm in order to displace enough volume to deliver the required amount of liquid.
D. Horsepower Calculations (see Notes 3, 4, 5, and 6 at the end of this section)
1. The required horsepower (hp) for driving a single acting reciprocating pump is calculated by the following equation:
hp = Pd Q (100) - Pi
Q (Em-5)
1714 Em 1714 (100)
Where:
D = pump displacement, U.S. gallons per minute (GPM)
Q = pump capacity, (GPM). Where Q = D x Ev
Pd = liquid pressure at pump discharge, lbs/in2
gauge (PSIG).
Pi = liquid pressure at pump inlet, lbs/in2 gauge (PSIG).
If Pi < 50 PSIG, then
Pi Q (Em - 5) = 0
1714 x (100)
Em = mechanical efficiency of pump, percent (for the above Pd and Pi
< 50 PSIG):
a. 90% for pumps without built-in reducer (power input from crankshaft).
b. 85% for pumps with built-in or bolted-on gear reduction (power input
from pinion shaft).
c. Reduce Em by the mechanical efficiency losses of any
intermediate speed reduction between drive and pump.
General Em values::
V-belt drive 5%
HTD drive 5%
Parallel shaft gear reducer 5%
Etc...
Em - 5 = efficiency of power recovery due to liquid pressure at pump inlet.
Ev = volumetric efficiency, where Ev = Q
Example 4:
Find the required horsepower (hp) and speed (rpm) for driving a single acting 2-3/4" x 5" triplex plunger pump under the following operating conditions:
Pump displacement = D = 138.9 GPM
Pressure at pump inlet = Pi = 200 psig
Pressure at pump discharge = Pd = 2020 psig
Mechanical efficiency of pump = Em = 75%
Volumetric efficiency of pump = Ev = 80%
Q = D x Ev = 138.9 x 0.8 = 111.12 GPM
hp = (Q x Pd) (100) - (Q x Pi
) ( Em - 5)
1714 x (Em) 1714 x (100)
hp = (111.12 x 2020) (100) - (111.12 x 200) (75-5)
1714 x (75) 1714 x (100)
hp = 165.53
gpr = 0.129 gal./plunger x 3 plungers/rev.
gpr = 0.387 gal./rev. (see Table 1)
n = GPM = 138.9 = 358.9 rpm
gpr 0.387
2. The required horsepower (hp) for driving a double acting duplex piston pump is
calculated by the following equation:
hp = (Q) (Pd - Pi)
(100)
1714 (Em)
Where,
D = pump displacement, gallons per minute (GPM)
Q = pump capacity, GPM where (Q = D / Ev )
Pd = liquid pressure at pump discharge, lbf/in2
gauge (psig).
Pi = liquid pressure at pump inlet, lbf/in2
gauge (psig).
Em = pump mechanical efficiency, percent (for above Pd and Pi).
a. 90% for pumps without built-in reducer
(with power input from crankshaft)
b. 85% for pumps with built-in reducer
(with power input from pinion shaft)
3. Reduce Em by the mechanical
efficiency losses of any intermediate speed reduction between driver and pump
General Em values:
V-Belt drive 5%
HTD drive 5%
Parallel shaft gear reducer 5%
Etc...
EV = pump volumetric efficiency, % = Q (100)
D
Example 5:
Find the required horsepower (hp) and pump speed (n) for driving a double acting 5" x 10" duplex piston pump with the following conditions.
Pump capacity = Q = 281.7 GPM
Liquid pressure at pump inlet = Pi = 50 psig
Liquid pressure at pump outlet = Pd = 330 psig
Mechanical efficiency of pump = Em = 90%
Volumetric efficiency of pump = EV = 85%
Piston Rod diameter = d = 1-1/2"
hp = Q (Pd - Pi)
100 = 281.7 (330-50) 100
1714 (Em) 1714 (90)
hp = 51.13
gpr = [0.850 x 4] - [ p (1.5)2 ] x 10 x 2 x 1
= 3.24
4 231
D = ( Q x 100 ) / EV = (281.7 x 100) / 85 = 331.41 GPM
n = D = 331.4 = 102.3 rpm
gpr 3.24
3. Quick calculation of horsepower requirement of a reciprocating pump.
Where the above formulas are very accurate, they are somewhat detailed. A quick and easy
method of calculating horsepower which is almost as accurate as the other methods, is as
follows:
A flow of one barrel per hour (1 BPH) of any specific gravity liquid against one pound per square inch gauge pressure (1 psig) requires 0.00040833 correction factor for theoretical horsepower. If the pump mechanism is approximately 90% mechanically efficient, the conversion factor can be corrected, for convenience, to 0.00045 to reflect this efficiency loss.
Therefore,
hp = 0.00045 x Pd x BPH capacity
BPH capacity = D Ev = (BPH displacement x EV)
100 100
Where,
Pd = liquid pressure at pump discharge, psig
EV = pump volumetric efficiency, %
Example 6:
Find the required horsepower (hp) to displace 100 gallons per minute (GPM) against a Pd = 1000 psig at a Ev = 95%.
hp = 0.00045 x 1000 x 100 x 95 = 61.1
0.7 x 100
Note 3: One barrel is 42 U.S. gallons. Gallons per minute (GPM) divided by 0.7 equals barrels per hour (BPH). Displacement is the theoretical volume swept by the plunger or piston on the discharge stroke during any selected time period.
Under the conditions and definitions given above, the pump speed must be a higher rpm in order to displace enough volume to deliver the required amount of liquid.
Note 4: Mechanical efficiency (Em) expressed as a percentage of total horsepower requirement can be used only if the pump is to be applied at or near its maximum designed rating. The horsepower required to operate a large pump at a small horsepower will usually be a considerably higher percentage of the total horsepower for the application.
We suggest that if the hydraulic horsepower - calculated without correction for mechanical efficiency - is less than 50% of the maximum design rating for the pump, you contact WGI for our recommendation for the driver horsepower.
Note 5: If the horsepower requirement is less than 15, as calculated by any of the above methods, we recommend that the motor driver be one size larger than the calculated requirement. This is because the horsepower required by a speed reduction device (belt, gear reducer, etc.) is relatively fixed and cannot be factored into the equation as a percentage of the smaller horsepower requirements.
Note 6: These computations are intended as a guide to standardization and may be modified if efficiency ratings for the pump application are lower than Ev = 95% and/or Em = 90%.
E. Devices for liquid pulsation control, Suction/Inlet and discharge.
A good inlet/suction and discharge pipe layout for reciprocating pumps of conventional type frequency require no pulsation control devices to compensate for normal variations in velocity flow in the complete piping system.
Where the suction or discharge lines are of considerable length, or the inlet has sufficient head, or liquid handled is hot - a suction or discharge dampening device of suitable size may sometimes be necessary to ensure smooth, quite operation. Dampening devices should be considered as a part of the piping system, rather than as a pump accessory.
The size and pre-charge of the dampener device will depend upon the type of pump, the liquid and the layout of the piping system. Recommendations as to size and type of device(s) should be obtained from the device manufacturer. Be sure to provide full information on the piping installation. Without complete knowledge of the piping system, it is impossible to determine the size and precharge of the dampeners. For bladder type dampeners, provisions should be made to keep the unit(s) charged with nitrogen or similar inert gas, in accordance with the device manufacturers recommendations. An exhausted device is of no value.
Dampeners, particularly on the suction (which are required more frequently than discharge), should be located as-close-as-possible to the pump and in such a position that they will absorb the impact of the moving liquid column and thus cushion the pulsations in the most efficient manner.
A properly sized, located and charged device may reduce the length of pipe used in the acceleration head equation to a value of 5 to 15 nominal pipe diameters. Figure 52 in Appendix A is a suggested piping system for power pumps.
III. PUMP MATERIAL SELECTION
The following material selection charts; TABLE 2 (for plunger pumps) and TABLE 3 (for piston pumps), are general recommendations. For more detailed or alternate recommendations, please consult WGI.
Material Selection Chart for Plunger Pumps |
|||||||||
Liquid |
R |
Liquid |
Valves |
Plungers |
Packing |
||||
Description |
E |
End |
"J" |
"V" |
Braid |
Thd |
|||
F |
Style |
Style |
Style |
Gland |
|||||
Amine |
(9) |
(7) |
(3) |
(4) |
(4) |
(4) |
(6) |
||
DEA |
CS |
D/CD, H/TD |
HS |
NA |
SF = 4511-4 |
232 |
CS or |
||
CF8M SS |
SSF = 4516-4 |
DI |
|||||||
MEA |
(1) |
CS |
D/CD, H/TD |
HS |
NA |
SF = 6618-4 |
232 |
CS or |
|
CF8M SS |
SSF = 1043-4 |
DI |
|||||||
Carbon Dioxide |
(7) |
(3) |
(4) |
(4) |
(4) |
(6) |
|||
Dry or Wet |
(5) |
CS |
D/CD, H/TD |
HC/HT |
NA |
SF=805-4 |
8921-K |
Temp. |
|
CF8M SS |
Var. |
||||||||
Condensate |
(5) |
(7) |
(3) |
(4) |
(4) & (9) |
(4) |
(6) |
||
n-Butane/iso-Butane |
CS or |
D/CD, H/TD |
HC/HT |
845 |
SF=809-4 |
238 |
CS or |
||
SS |
CF8M SS |
SSF=1068-4 |
DI |
||||||
Ethane/Methane |
CS or |
D/CD, H/TD |
HC/HT |
845 |
SF=809-4 |
8921-K |
CS or |
||
SS |
CF8M SS |
SSF=1068-4 |
DI |
||||||
Liquid Propane Gas |
LPG |
CS or |
D/CD, H/TD |
HC/HT |
838/835 |
SF=809-4 |
217 |
Temp. |
|
or Natural Gas Liquid |
NGL |
SS |
CF8M SS |
SSF=1068-4 |
Var. |
||||
Lean Oil |
CS or |
D/CD, H/TD |
HC/HT |
||||||