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Latest Technology for Longer Pump Life • 33 Model Sizes • Flows to 26,000 GPM • Heads to 410 feet • Pressure to 232 PSIG Large Process Pump Design
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  • Latest Technologyfor Longer Pump Life

    33 Model Sizes Flows to 26,000 GPM Heads to 410 feet Pressure to 232 PSIG

    Large Process Pump Design

  • Total Cost of Ownership

    Purchase

    5%

    Installation

    24%

    Operating

    30%

    Maintenance

    41%

    Purchase

    5%

    Installation

    24%

    Operating

    30%

    Maintenance

    41%

    20-Year Life Cycle CostsBased on 6000 hr/year

    20-Year Life Cycle CostsBased on 6000 hr/year

  • Pump Reliability

    Liquid end Seal chamber Power end Baseplate

  • 33 pump sizes

    Maximizes pump reliability

    Coverage ensures efficient operation

    Only 4 power frames

    Hydraulic Coverage

  • Open impellers (standard) Solids, fiber & air applications Full back shroud for

    mechanical integrity Balance holes for low

    axial thrust Engineered back pump out

    vanes for low bearing loads

    Closed impellers (optional) Maximized efficiency Replaceable rings

    Impeller Design

  • EXPANDINGVOLUTECASING

    SEMICONCENTRICCASING

    Pump Flow BestEfficiencyPoint

    LowDeflection

    HighDeflection

    ExpandingVoluteCasing

    SemiConcentricCasing

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    Casing Design

  • z Problem wear areas have always included the casing cutwater and wearplate surface.

    z Computer solidification modeling allows extra thickness at crucial wear points for extended life.

    Extra Thickness

    Solidification Modeling

  • z Corrosion has less effect on large section components such as our impeller lock nut.

    z Crevice corrosion is reduced through the use of o-rings at the critical fluid joints.

    Corrosion Reliability

  • Attachment Requirements

    Transmit torque

    Prevent Leakage

    Prevent loosening during reverse rotation

    Threaded Acme Thread

    Impeller Attachment Methods

    Keyed

  • Goulds External Clearance Adjustment provides:

    Precision fit between impeller and sideplate

    Sideplate is clamped and sealed Performance reliability maintained Moving parts move in a sealed and

    lubricated environment Proven in over one million

    installations over 50 years

    Maintain High Performance

  • Our Impeller back vanes are engineered in shape and height to be insensitive to impeller adjustments.

    Common in recessed impeller pump designs

    Proven on Test

    1X 2X 3X

    Performance Assured

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    Back Vane Clearance

  • O-ring moves over the corroded & fouled casing surface

    Sideplate floats on studs- cocking in casing- studs can shear- not precise adjustment

    Leakage past o-ring has leakage path through studs

    Adjustment Direction

    Sideplate Adjustment(Method used by another pump manufacturer)

  • Closed Impellerwith casing rings

    Open Impellerfloating sideplate

    Evolution of Sideplate Adjustment

    Converting closed impellers to open was economically accomplished using adjustable sideplates.

  • The majority of pump downtime is due to mechanical

    seal or packing failure.

    Seal Chamber Design

  • Mechanical Seal Considerations

    Seal Selection

    Shaft Deflection

    Seal Environment

  • Frame SPower end

    Frame MPower end

    Frame LPower end

    Frame XLPower end

    Goulds 3180 Competitor A

    Group 3Power end

    Group 4Power end

    Group 5Power end

    L3/D4 =44

    L3/D4 =40

    L3/D4 =25

    L3/D4 =19

    L3/D4 =41

    L3/D4 =41

    L3/D4 =17

    Pump manufacturers frequently imply L3/D4ratios yield longer seal life.

    Shaft deflection is a function of low L3/D4 and lower radial loads.

    All reputable pump manufacturers have deflections under 0.002 in.

    L3/D4 < 55 = Industry Target

    Shaft Stiffness Deflection

  • EXPANDINGVOLUTECASING

    SEMICONCENTRICCASING

    Pump Flow BestEfficiencyPoint

    LowDeflection

    HighDeflection

    ExpandingVoluteCasing

    SemiConcentricCasing

    R

    a

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    F

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    Low radial load = low deflections

    Shaft Deflection

  • Leading seal manufacturersreport that shaft deflection is NOT

    the cause of seal failures!The problem is SEAL ENVIRONMENT!

    Mechanical Seals

  • Seal Environment is Criticalfor Extended Seal Life

  • Seal Chambers Initially

    Designed for Packing

  • Big Bore Seal Chamber Taper Bore Seal Chamber

    (Introduced in the mid 1980s)

    Evolution to Large Bore Seal Chambers to Extend Seal Life

  • Conventional taper bore seal chamber mechanical seals fail when vapor or solids are present

    Modified tapered bore seal chamber with axial ribs good for services containing air, minimum solids

    Goulds standard tapered bore plus seal chamber the best solution for services containing solids and air or vapors

    Taper Bore Evolution

  • 1) Solids/liquid mixture flowstoward seal chamber

    2) Turbulent zone

    3) Clean liquid flows towards seal

    4) Low pressure zone createdby vane particle ejector

    5) Seal faces flush with clean liquid

    Taper Bore Plus How it Works

  • Engineered seal chamber with vane particle ejector

    Goulds TaperBore Plus Patented: No.5,336,048

  • Research & Development

  • Zero Flush Water

    The 3180 has a revolutionary seal chamber design guaranteedto operate on 6% OD stock without flush water!PATENTED!

    Hard TungstenCarbide Seal Faces

    Patented Vane Particle Ejector Springsnot in fluid

  • Why is zero flush important? Is the pump remotely located?

    How reliable is the flush water? Plugging, Freezing, Lines shut off

    How clean is the flush water?

    What is the cost of flushing? Water treatment Product dilution

    Flush Water Considerations

  • Cover

    Back Plate

    Repeller

    Dynamic Seals

  • When Pump is OperatingDynamic Seal

    Hydrodynamic Sealby Repeller PROVIDES

    Air-PumpageInterface

  • Diaphragm Secondary Sealfor Dynamic Seal

    SleeveFollower

    Gland Diaphragm

    Dynamic Seals Secondary SealingStuffing Box

  • z The 3180 includes a dynamic seal option design that seals the shaft on 6%OD stock without flush water! Unique grooves allow operation on recycled fibers. *patented

    Zero Flush Water

  • 12" S 14" S, MSpeed 1780 1470 1180 960 1780 1470 1180 960Repeller Diameter 8" 9.75"Max Suction Head (ft) 23 13 6 45 28 15 8(above atmospheric)Repeller BHP 1.1 0.61 0.3 2.4 1.3 0.7 0.4

    Model 3180 Dynamic SealCapability Chart

  • Vacuum Services

    Liquids at or near their boiling point

    Highly viscous liquids

    Liquids that crystallize when exposed to air

    Liquids that become corrosive when exposed to air

    Severe corrosives

    Zero leakage applications

    Dynamic Seal Application Limitations

  • Bearing design life Bearing environment Bearing temperature

    Power ends

  • Bearing companies reveal that fatigue failure is extremely rare.Contamination and lack of lubrication are the major cause of failure, plus....

    Bearing Size

    Bea

    ring

    Life

    Fatig

    ue Li

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    Bearing Life (Fatigue/Theoretical)

  • Non-optimized bearings will be susceptible to skidding, cage stresses and higher operating temperatures that lead to failure.

    Pump Bearing Life(True Service Life)

    Skidding

  • Measured on Test

    Bearing Loads

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    Bearing Size

    The Right SizeKeeping the pumploads minimizedand selecting theright bearings willkeep temperaturesunder control.

    Watch the Temperature

  • 120F

    140F

    160F

    180F

    Model 3180Pumps operateat an averagetemperatureof 120 F

    High

    Typical

    Low

    Bearing Frame Oil Temperatures

  • Labyrinth oil seals are standard.

    Carbon-filled Teflon is impervious to fluid corrosion.

    Prevents lubricant contamination.

    Oil Seals

  • Only the Goulds seal passed every test while competitive labyrinth seals failed.

    Oil containment testLabyrinth sealing paths

    Goulds Labyrinth Seal Torture Testing

    Water exclusion test Dust exclusion test

  • Best in the Industry

    Bearing design life >100,000 hrs

    Bearing temperatures under 120F

    Superior labyrinth oil seal design

    Guaranteed like no other!

    Power End Reliability

  • Fabricated baseplatedesigns with high torsional stiffness.

    Machined surfaces 0.002 inch flatness.

    Horizontal motor adjusters & vertical jacking screws

    Engineered Baseplates

  • Model 3180

    Additional Maintenanceand Reliability Features

  • Integral frame eliminates adapter and provides better seal access. Swing away lugs secure the seal chamber Casing bolts do not have to be removed Swing away lugs also act as jacking bolts

    Ease of Maintenance

  • Monitoring sites for vibration and temperature are provided as standard for accurate and repeatable readings.

    Monitor Sites

  • G2.5 impeller balance (routinely done!) Engineered shaft (alternating keyways) Keys and keyways engineered to eliminate voids Patented arbor designs ensure repeatability Technicians certified to ISO 9001 standards Vibration < 0.15 inches/sec

    We Take Balancing Seriously

  • The Frame Support is a solid cast machined foot.

    Alignment can be assured & maintained.

    Rigid Support

  • No one in the industry offers the broad rangeof process pumps that Goulds does.....

    Pick Your Perfect Process Pump

  • Model LF3196 Designed for Low Flow Services

  • Not all pumps aredesigned for low flows

    LF3196 designed specifically for trouble-free operation at low flows

    Off design operation range

    Recommended operation range

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    FLOWTYPICAL END SUCTION PUMP CURVE

    System Curve Actual Throttled Operation

    Rated Performance

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    FLOWLF 3196 PUMP CURVE

    System Curve Actual Throttled

    Model LF3196 Designed for Low Flow Services

  • Goulds Model JC Designed for Handling aWide Range of Corrosive/Abrasive Slurries

  • Model 3298 Magnetic Drive Pump

  • Model 3298 Magnetic Drive Pump

  • Model 3298 Tefzel Construction for Extreme Corrosion Resistance

  • Capacity to 2400 tons/day

    Model 3500 Medium Consistency Pump(to 16% Bone Dry)

  • Latest Technologyfor Longer Pump Life

    33 Model Sizes Flows to 26,000 GPM Heads to 410 feet Pressure to 232 PSIG

    Large Process Pump Design