imp load
TRANSCRIPT
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Calculating Radial Loads
Calculating Radial Loads on impellers in a volute
type casing.
CP-12
Total suction head psig = 25.000
Total suction head converted to psia = 39.700
sp. gr. = 0.765
Total suction head converted to feet of liquid, absolute = 119.827
Total discharge head psig = 432
Total discharge head converted to psia = 446.7
Total discharge head converted to feet of liquid, absolute = 1304
H = total head at Q gpm, in feet 1184
D2 = O.D. of impeller, in inches 11.875
B2 = width of impeller at O.D., in inches 1
Q = capacity, in gpm, at which radial thrust is to 432
Qn = capacity, in gpm, at best efficiency of pump 950
N = rotative speed, in rpm's 3560
hsv = net positive suction head required by 26
maximum diameter impeller at best
efficiency, in feet
K = radial thrust factor at shutoff, (from sheet 3) 0.18
Kq = capacity factor 0.36903
n = 0.58436
Ns = specific speed of pump 367
S = suction specific speed, ideal less than 12,000 9530higher values indicate less NPSH requirements
P = Resultant radial force, in pounds 309
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Calculating Radial Loads
psig
psia
feet
psig
psia
feet
feet **used to calculate Ns
*used to calculate Nsss (S) and **Ns
*used to calculate Nsss (S) and **Ns
*used to calculate Nsss (S)
where: Kq = 1 - (Q/Qn)(power n)
where: n = 0.7+2.6((Ns-500)/3000)
where: Ns = NQ(power.5/H (power.75)
where: S = NQ(power.5)/hsv(power.75)
where: P = Kq x K x (H x sp gr/2.31) x D2 x B2
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First Critical Speed
Estimating first critical speed,
overhung or centerhung
CP-12 impeller = 35 lbs.
w = weight of mass (impeller and/or impeller and loading) 50 pounds
d = shaft diameter 1.875 inches
L = shaft length 11.75 L = length of shafts = distance between bearings 9.375 inches
Y = maximum deflection, at end if (overhung) 0.0015 Y = WL (power3)/3EI
Y = maximum deflection, at center if (center hung) 0.0000 Y = WL (power3)/48EI
E = modulus of elasticity, 30,000,000 psi for steel 30,000,000 E = 30,000,000
I = moment of inertia of the shaft, in. (power 4) 0.607 I = pi*d(power4)/64
Ks = spring constant of the shaft if (overhung) 33659 Ks = 3EI/L(power3)
Ks = spring constant of the shaft if (center hung) 1060288 Ks = 48EI/L(power3)
M = mass divided by gravity 0.1295 M = weight / acceleration of gravity
w = first critical speed in rpm's if (overhung) 4868 w =(square root)Ks/M(60/2pi)
w = first critical speed in rpm's if (center hung) 27321 w =(square root)Ks/M(60/2pi)
Motor speed = 3560 + 15% = 4094 cpmMotor speed = 3560 - 15% = 3026 cpm
At 534 GPM CPM = 3873 109% of motor speed
To keep the bolt from breaking
At 829 GPM shaft deflection is .0015"
To keep the seal from leaking
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K - Radial Thrust Factor
0.125
0.175
0.225
0.250
0.280
0.300
0.3250.340
0.350
0.365
0.370
0.375
0.375
0.375
0.375
0.000
0.050
0.100
0.150
0.200
0.2500.300
0.350
0.400
K
-RadialThrustFactor
400 1000 2000 3000 4000Specific Speed Ns
Chart
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K - Radial Thrust Factor
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Test for Vaporization
Test for Vaporization
CP-12
Total suction head psig = 12.000 psig
Total suction head converted to psia = 26.700 psia
sp. gr. = 0.765
Total suction head converted to feet of liquid, absolute = 80.589 feetRequired NPSH in feet = 9.500 feet
Pressure experienced by the fluid particle
in the pump suction, absolute = 71.089 feet
Vapor pressure of product, absolute = 0.500 psia
Vapor pressure converted to feet of liquid, absolute = 1.509 feet
Available NPSH in feet = 79.079 feet
If less than required vaporization is occurring and suction
head should be increased.
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Bearing Load
Calculating radial loads on bearings
CP-12
w = weight of mass (impeller and/or impeller and loading) 79.00
L = shaft length 11.75
s = distance between bearings 9.38
R1 = load at bearing 1, in pounds 99.01R2 = load at bearing 2, in pounds 178.01
w = weight of mass (impeller and/or impeller and loading) 50.00
L = shaft length 11.75
s = distance between bearings 9.38
R1 = load at bearing 1, in pounds 62.67
R2 = load at bearing 2, in pounds 112.67
w = weight of mass (impeller and/or impeller and loading) 35.00
L = shaft length 11.75
s = distance between bearings 9.38
R1 = load at bearing 1, in pounds 43.87R2 = load at bearing 2, in pounds 78.87
At 534 GPM w = 79
At 829 GPM w = 50
At 950 w = 35
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Bearing Load
pounds
L = length of shaft from first bearing to center of mass
inches
R1 = Pa\sR2 = P(a+s)/s
pounds
L = length of shaft from first bearing to center of mass
inches
R1 = Pa\s
R2 = P(a+s)/s
pounds
L = length of shaft from first bearing to center of mass
inches
R1 = Pa\sR2 = P(a+s)/s
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Rotor Stiffness
Calculating Rotor Stiffness
CP-12
L = shaft length (overhung portion) 11.75
d = shaft diameter 1.875
L3D4 = measure of rotor stiffness 131
L = shaft length (overhung portion) 11.75
d = shaft diameter 1.918
L3D4 = measure of rotor stiffness 120
L = shaft length (overhung portion) 11.75
d = shaft diameter 2
L3D4 = measure of rotor stiffness 101
The lower the L3D4 the less the shaft deflection
seals are prone to leak with deflection of .0015
ANSI pumps have L3D4 ratios of 20 - 120
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Rotor Stiffness
inches
inches
L3D4 = Shaft length (power 3)/shaft diameter (power 4)
inches
inches
L3D4 = Shaft length (power 3)/shaft diameter (power 4)
inches
inches
L3D4 = Shaft length (power 3)/shaft diameter (power 4)
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BPD to GPM
To convert BPD to GPM To convert GPM to BPD
BPD = 11000 GPM = 100
Converted to GPM = 321 Converted to BPD = 4200
BPD = 4000 GPM = 200
Converted to GPM = 117 Converted to BPD = 8400
BPD = 6000 GPM = 300
Converted to GPM = 175 Converted to BPD = 12600
BPD = 8000 GPM = 400
Converted to GPM = 233 Converted to BPD = 16800
BPD = 10000 GPM = 500
Converted to GPM = 292 Converted to BPD = 21000
BPD = 12000 GPM = 600
Converted to GPM = 350 Converted to BPD = 25200
BPD = 14000 GPM = 700
Converted to GPM = 408 Converted to BPD = 29400
BPD = 16000 GPM = 200Converted to GPM = 467 Converted to BPD = 8400
BPD = 18000 GPM = 300
Converted to GPM = 525 Converted to BPD = 12600
BPD = 20000 GPM = 400
Converted to GPM = 583 Converted to BPD = 16800
BPD = 22000 GPM = 500
Converted to GPM = 642 Converted to BPD = 21000
BPD = 24000 GPM = 600
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BPD to GPM
Converted to GPM = 700 Converted to BPD = 25200
BPD = 26000 GPM = 700
Converted to GPM = 758 Converted to BPD = 29400
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Convert Feet of Liquid to psig
To convert feet to psi To convert psi to feet
Feet of head = 40.000 psig = 345.000
sp. gr. = 0.700 sp. gr. = 0.819
Converted to PSI = 12.126 Converted to feet of head = 972.656
Feet of head = 200.000 psig = 100.000
sp. gr. = 0.765 sp. gr. = 0.819
Converted to PSI = 66.262 Converted to feet of head = 281.929
Feet of head = 300.000 psig = 315.000
sp. gr. = 0.765 sp. gr. = 0.819
Converted to PSI = 99.394 Converted to feet of head = 888.077
Feet of head = 400.000 psig = 245.000
sp. gr. = 0.765 sp. gr. = 0.819
Converted to PSI = 132.525 Converted to feet of head = 690.726
Feet of head = 500.000 psig = 84.000
sp. gr. = 0.765 sp. gr. = 0.819
Converted to PSI = 165.656 Converted to feet of head = 236.821
Feet of head = 600.000 psig = 175.000
sp. gr. = 0.765 sp. gr. = 0.765Converted to PSI = 198.787 Converted to feet of head = 528.203
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Aprox. Flow Through Orifice
To Aproximate the flow through an orifice
(water)
Q=AV
Q= The flow in cubic feet per second (ft3/sec.)
A= The area of the orifice in square feet (ft2)
V= The velocity of the liquid in feet per second (ft/sec.)
Q=AVK
h=V(2)/2g or V=su.rt 2gh or V=8.02 sq.rt.h
g=32.2 ft/sec(2)
h= Head across the orifice
High pressure side = 285 psig
Low pressure side = 116 psig
Differiential psig = 169.000 psig
sp. gr. = 0.523
Differiential head = 746.120 feet
Differiential head = 746.120 Feet of LiquidArea = 0.14 Square Inches
K factor = 0.62
Flow = 59.274 GPM's
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To Estimate Force of Imbalance
To estimate the force of imbalance
Weight of component = 30 Pounds
Speed = 3600 Rpm's
Balance tolerance 4w/n = 0.0333 Ounce inches
Balance tolerance 4w/n = 0.9451 Gram inches
50% for symmetrical weight = 0.4725 Gram inchesFor non symmetrical rotors the individual journal load
must be calculated
Acceptable weight of imbalance = 0.4725 Gram inches
Weight of imbalance in grams converted to pounds = 0.0010 Pound inches
Acceleration of gravity = 386 Inches per second per second
Radius of gyration of imbalance = 1 Inches
Velocity = 22619.5 Inches per minute
Velocity = 377.0 Inches per second
Acceleration = 142122.3 Inches per second per second
Force = 0.4 Pounds
Force should be less that 5% of component weight
mm per second 2.5 mm per second
convert to inches per second 0.098425 Inches per second
Balance quality grade
Vibration
velocity in Rotor types
G
mm per
second General examples
Crankshaft drives of large Diesel engines
Complete engines for trucks and locomotives
G 40 40
Crankshaft drives for engines of trucks and
locomotives
Parts of crushing machinery
Parts of agricultural machinery
Fly-wheels
Fans
Aircraft gas turbine rotors
Electrical armatures
Process plant machinery
Pump impellers
Machine-tool drives
Turbo compressors
Small electric armatures
Turbine-driven pumps
Grinding machine drives
Textile bobbins
Automotive turbochargers
Gyroscopes
Disk-drives
Spindles for high-precision applications
ISO Grade 2.5 at 3600 RPM's
Balance quality grades are standardized in ISO 1940.
G 100
G 16
G 6.3
100
16
6.3
G 2.5
G 1
G 0.4
The smaller the number, the smoother the operation
1
0.4
2.5
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To Estimate Force of Imbalance
Acceptable weight of imbalance = 8 kg
Acceleration of gravity = 980.44 centimeters per second per second
Radius of gyration = 1 centimeter
Rpm's = 3600 revolutions per minute
Velocity = 22619.4671 centimeters per minute
Velocity = 376.991118 centimeters per secondAcceleration = 142122.303 centimeters per second per second
Force = 11.596614 kilograms
Force = 25.6 pounds
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Flow and Critical
CP-12 flow and its affect on the first critical of the pump shaft
GPM's BPD Resultant Load After Weight of Total Load First Critical % of Motor
Radial Loading Balancing Impeller of Pump Shaft Speed
Away 80% CPM's 3560
0 0 505 101 35 136 2952 83% Acceptable
100 3429 370 74 35 109 3297 93% Bad
200 6857 340 68 35 103 3392 95% Bad
300 10286 308 62 35 97 3495 98% Really Bad
400 13714 274 55 35 90 3628 102% Really Bad
500 17143 235 47 35 82 3801 107% Bad
600 20571 192 38 35 73 4029 113% Acceptable
700 24000 145 29 35 64 4303 121% Acceptable
800 27429 92 18 35 53 4728 133% Acceptable
900 30857 32 6 35 41 5376 151% Acceptable
950 32571 0 0 35 35 5818 163% Acceptable
1000 34286 34 7 35 42 5311 149% Acceptable
1100 37714 108 22 35 57 4559 128% Acceptable
1200 41143 190 38 35 73 4029 113% Acceptable
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Indicator Reverse Alignment
Turbex, Inc. 281-485-8255 Pump # KC-1
Date = August 26, 2013
Time = 6:25 AM
Button to Button = 16
Front foot to 1st. Button = 11
Rear foot to front foot = 32
Movable to fixed = 0 Fixed to movable = 0
Left & right of fixed = 0 RIM 0 Left and right of movable = 0 RIM 0
Movable to fixed = -6 Fixed to movable = 20
If plus add shims TAN of
Front shim change = 15 Ver. 0.00063 Misalignment fixed end Bad
Rear shim change = 29 Hor. 0.00000 Misalignment fixed end Good
If plus move to the right 0.00050 Acceptable to 3600 RPM's
Front lateral move = 0 Ver. -0.00019 Misalignment movable end Good
Rear lateral move = 0 Hor. 0.00000 Misalignment movable end Good
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Rim and Face alignment
Turbex, Inc. 281-485-8255 Pump # P-106-A
Date = August 26, 2013
Flex plane seperation = 7 Time = 6:25 AM
Sweep = 4.5
Front foot to face = 20
Rear foot to face = 34
Movable to fixed = 8 Movable to fixed = -2
Left & right of fixed = 4 RIM 4 Left & right of fixed = -1 FACE -1
Movable to fixed = 0 Movable to fixed = 0
If plus add shims TAN of
Front shim change = 13 Ver. 0.00029 Misalignment face Good
Rear shim change = 19 Hor. 0.00000 Misalignment face Good
If plus move to the right 0.00050 Acceptable to 3600 RPM's
Front lateral move = 0 Ver. -0.00057 Misalignment offset Bad
Rear lateral move = 0 Hor. 0.00000 Misalignment offset Good
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