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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

    Page 8

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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)

    Page 10

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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

    Page 13

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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

    Page 14

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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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