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Positive Displacement Pumps Chad Wunderlich Viking Pump Calgary Pump Symposium 2013

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Calgary Pump Symposium 2013

Positive Displacement Pumps

Chad Wunderlich Viking Pump

Calgary Pump Symposium 2013

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Calgary Pump Symposium 2013 Calgary Pump Symposium 2013

Chad Wunderlich Viking Pump Engineering Manager – Technical Customer Service 13 Years Experience

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Calgary Pump Symposium 2013

Agenda

• Define the difference between positive displacement (PD) and kinetic pump technologies.

• Explore the strengths and weaknesses of each • List examples of where PD pump technology is

typically favored and why.

Calgary Pump Symposium 2013

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Calgary Pump Symposium 2013

Agenda

• Look at various positive displacement principles.

• Explore how they operate, each one’s strengths and weaknesses, and list applications where each is commonly used.

Calgary Pump Symposium 2013

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Calgary Pump Symposium 2013

PUMPS

POSITIVE DISPLACEMENT KINETIC

CENTRIFUGAL REGENERATIVE TURBINE ROTARY RECIPROCATING

Pump “Family Tree”

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Calgary Pump Symposium 2013

Pump Sales

010203040506070

%

Centrifugal

Rotary PD

Diaphragm

Reciprocating

Turbine

Other

Centrifugal 67%, Other 33%

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Calgary Pump Symposium 2013

Centrifugal Pump Principle

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Calgary Pump Symposium 2013

Centrifugal Pump Principle A centrifugal pump

generates a low pressure area in the impeller to draw fluid in. (The same as a PD Pump)

The fluid velocity is increased as it travels outward along the Impeller.

Velocity is converted to pressure in the diffuser or volute. The pump is a pressure source.

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Calgary Pump Symposium 2013

Centrifugal Pump Principle

Centrifugal pumps generate head (pressure) and flow results.

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Calgary Pump Symposium 2013

Positive Displacement Pump Principle

Volume of liquid displaced by the ball

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Calgary Pump Symposium 2013

Rotary PD Pump Principle A Positive Displacement (PD) pump displaces a known

quantity of liquid with each revolution of the pumping elements. This is done by trapping liquid between the pumping elements and a stationary casing

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Calgary Pump Symposium 2013

Rotary PD Pump Principle A PD pump creates

flow. Pressure created is a result of system restrictions such as pipe shear, liquid shear, or work required (hydraulic systems)

PD pumps generate flow and pressure results.

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Calgary Pump Symposium 2013

Centrifugal / PD Comparison PUMP

CHARACTERISTICS

PUMP PRINCIPLE

Kinetic (Centrifugal)

Rotary (Positive Displacement)

Viscosities Handled Typically water-thin

30-3,000 SSU (1-750 cSt)

Typically lubricating liquids 30-Millions SSU (1-1M cSt)

Pressure Low

Up to 500 PSI (34 BAR)

High Up to 3,000 PSI (200 BAR)

Speed High

1150-3450 RPM Medium

1750 RPM or less

Capacity High

To 100,000 GPM (20k M³/hr)

Medium To 3,000 GPM (700 M³/hr)

Efficiency Rapidly drops with increasing viscosity / pressure Relatively High

Performance (Flow) Smooth Smooth

Suction Characteristics Not Self Priming Very Good

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Calgary Pump Symposium 2013

Centrifugal to PD Comparison

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Calgary Pump Symposium 2013

Review – Low NPSH or Suction Lift Applications – High Viscosity Applications – High Pressure Applications – Low Flow, High Head Applications – Flow Rate Control Required (Metering) – Variable Service Conditions (Pressures,

Viscosities, etc.) – Energy Usage Concerns (Efficiency) – Shear Sensitive Liquids

When to Use PD Pumps

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Calgary Pump Symposium 2013

Positive Displacement Pump Principles

• There are over 100 different PD principles and variations available. Each with their own unique advantages and disadvantages.

• Due to time I will be discussing only a few of the most common types. Each is commonly used in oil and gas applications.

Calgary Pump Symposium 2013

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Calgary Pump Symposium 2013

PD Pumps to be Covered

• Rotary – Gear

• Internal Gear • External Gear

– Vane – Timed Lobe

• Reciprocating – Hydraulically Actuated Diaphragm – AOD (Air Operated Diaphragm)

Calgary Pump Symposium 2013

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Calgary Pump Symposium 2013

Internal Gear Pumps

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Calgary Pump Symposium 2013

Internal Gear Pump Operating Principle

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Calgary Pump Symposium 2013

Internal Gear Pump Operating Principle

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Calgary Pump Symposium 2013

Internal Gear Pump Design

Relief Valve

Relief Valve • Provides over-pressure

protection • All positive displacement

pumps need to have some form of over-pressure protection

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Calgary Pump Symposium 2013

Internal Gear Pump Advantages

• ADVANTAGES • DISADVANTAGES

• Only one stuffing box • Ideal for high-viscosity liquids • Operates well in either direction • Can be made to operate with one

direction of flow with either rotation

• Low NPSH required • Single adjustable end clearance • Flexible design offers application

customization

• Usually requires moderate speeds • Medium pressure limitations • One bearing runs in the product

pumped • Overhung load on shaft bearing

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Calgary Pump Symposium 2013

Internal Gear Pump Performance Range

FLOW RANGE 0.5 TO 1600 GPM

VISCOSITY RANGE

0.1 cPs - 1,000,000 cPs

MAXIMUM DIFFERENTIAL PRESSURE 400 PSI (2800 kPa)

TEMPERATURE RANGE -100°F to 800°F (-80°C to 425°C)

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Calgary Pump Symposium 2013

Example Applications

Asphalt refining, transfer, blending, and delivery

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Calgary Pump Symposium 2013

Example Applications

Pipeline sampling

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Calgary Pump Symposium 2013

Example Applications

• Well Stimulation (hot oil trucks)

• Shale Fracturing (frac trucks)

• Gathering (wellhead to local storage)

• Transfer (local storage to terminal, barge or refinery)

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Calgary Pump Symposium 2013

Example Applications

Lube oil blending, loading/unloading

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Calgary Pump Symposium 2013

External Gear Pumps

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Calgary Pump Symposium 2013

External Gear Pump Operating Principle

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Calgary Pump Symposium 2013

External Gear Pump Operating Principle

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Calgary Pump Symposium 2013

Gear Cuts

Spur Gears Helical Gears Herringbone Gears

• Lowest Cost • No thrust

• Moderate Cost • Lower noise • Lower NPSH • Thrust in opposite

directions

• Highest Cost • Lower noise • Lower NPSH • No thrust

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Calgary Pump Symposium 2013

Double Pumps

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Calgary Pump Symposium 2013

External Gear Pump Advantages

ADVANTAGES DISADVANTAGES

• High speed • High pressure capability • No overhung bearing loads • Design accommodates wide

variety of materials • Sections can be stacked for

multiple inlets and outlets • Bi-Directional

• Four bushings in liquid area • No solids allowed • Fixed end clearances

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Calgary Pump Symposium 2013

External Gear Pump Performance Range

FLOW RANGE 0.001 TO 1500 GPM

VISCOSITY RANGE

0.1 cPs - 1,000,000 cPs

MAXIMUM DIFFERENTIAL PRESSURE 3000 PSI (20,000 kPa)

TEMPERATURE RANGE -100°F to 500°F (-80°C to 260°C)

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Calgary Pump Symposium 2013

Example Applications

Fuel oil & Lube oil filtering, dewatering, and dispensing

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Calgary Pump Symposium 2013

Example Applications

Injection of additives into pipeline. (i.e. dyes, mercaptum, etc.)

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Calgary Pump Symposium 2013

Example Applications

Acid or caustic transfer (composite pump)

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Calgary Pump Symposium 2013

Example Applications

Duplex fuel oil skids for backup power gen sets or burner systems

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Calgary Pump Symposium 2013

Example Applications

Rust preventative or lube oil delivery to multiple points with a single pump

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Calgary Pump Symposium 2013

Vane Pumps

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Calgary Pump Symposium 2013

Vane Pump Operating Principle

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Calgary Pump Symposium 2013

Vane Pump Operating Principle

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Calgary Pump Symposium 2013

How the Vanes Work

1. Push rods initiate the vane extension when the opposing vane is pushed into its slot.

2. Centrifugal force, slings the vanes to the outside.

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Calgary Pump Symposium 2013

How the Vanes Work

1. Push rods initiate the vane extension when the opposing vane is pushed into its slot.

2. Centrifugal force, slings the vanes to the outside.

3. Grooves in each vane’s leading edge allow liquid to feed in under pressure to push behind the vane.

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Calgary Pump Symposium 2013

Self Compensating for Wear

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Calgary Pump Symposium 2013

Vane Pump Advantages

ADVANTAGES DISADVANTAGES

• Sliding contact of vanes make this pump good for thin liquids

• Can run dry for short periods • Pump normally has one seal

chamber

•Can have two seal chambers •Not suitable for high

pressures •Not suitable for high viscosity •Not good with abrasives •Failure mode is catastrophic

when vanes fail

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Calgary Pump Symposium 2013

Vane Pump Performance Range

FLOW RANGE 5 to 2000 GPM

VISCOSITY RANGE 0.1 cPs – 25,000 cPs

MAXIMUM DIFFERENTIAL PRESSURE

150 PSI (1000 kPa)

TEMPERATURE RANGE -60°F to 225°F (-50°C to 110°C)

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Calgary Pump Symposium 2013

Example Applications

Propane, Butane, Liquid CO2, and other liquefied gases.

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Calgary Pump Symposium 2013

Example Applications

Water

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Calgary Pump Symposium 2013

Lobe Pumps

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Calgary Pump Symposium 2013

Lobe Pump Operating Principle

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Calgary Pump Symposium 2013

Lobe Profiles

Bi-Wing (or Scimitar) Tri-Lobe Multi-Lobe Multi-Lobe

(SIP)

Twin-Wing Rotor Single-Wing Rotor

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Calgary Pump Symposium 2013

Lobe Pump Advantages

ADVANTAGES DISADVANTAGES

• Pass medium solids • No metal-to-metal contact • Superior CIP/SIP

capabilities • Long term dry run (with

lubrication to seals)

• Requires timing gears • Requires two seals • Reduced lift with thin

liquids

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Calgary Pump Symposium 2013

Lobe Pump Performance Range

FLOW RANGE 5 to 800 GPM

VISCOSITY RANGE

0.1 cPs – 1,000,000 cPs

MAXIMUM DIFFERENTIAL PRESSURE 400 PSI (2800 kPa)

TEMPERATURE RANGE -40°F to 400°F (-40°C to 200°C)

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Calgary Pump Symposium 2013

Example Applications

• Sanitary • Food • Personal Care • Pharmaceutical

• Industrial • Chemical • Pulp and Paper

• Municipal • Sludge • Slurry

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Calgary Pump Symposium 2013

Example Applications

Wax in shale oil refinery

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Calgary Pump Symposium 2013

Hydraulically Actuated Diaphragm Pumps

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Calgary Pump Symposium 2013

Diaphragm Pump Operating Principle

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Calgary Pump Symposium 2013

Diaphragm Pump Advantages

ADVANTAGES DISADVANTAGES

• No shaft seal required • High pressure capability • Excellent metering capability • Variable flow (either

mechanically or speed) • High temperature capacity

•Pulsing flow •Internal hydraulic system to

maintain •Potential for contamination

when diaphragm fails •High cost, especially for large

flows

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Calgary Pump Symposium 2013

Diaphragm Pump Performance Range

FLOW RANGE 0.001 to 70 GPM

VISCOSITY RANGE 0.1 cPs – 10,000 cPs

MAXIMUM DIFFERENTIAL PRESSURE

6000 PSI (40,000 kPa)

TEMPERATURE RANGE -60°F to 800°F (-50°C to 425°C)

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Calgary Pump Symposium 2013

Example Applications

Polymer metering

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Calgary Pump Symposium 2013

Air Operated Diaphragm Pumps

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Calgary Pump Symposium 2013

AOD Pump Operating Principle

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Calgary Pump Symposium 2013

AOD Pump Operating Principle

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Calgary Pump Symposium 2013

Is an AOD a PD pump or not?

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Calgary Pump Symposium 2013

AOD Pump Advantages

ADVANTAGES DISADVANTAGES

• No shaft seal required • Portable • Handles solids and abrasives • Can run dry • Easy to run • Explosion proof • Inexpensive

•Pulsing flow •Inconsistent flow due to

system changes •May be expensive to operate •Diaphragm failure causes

immediate leakage •Limited diaphragm life due to

constant flexing •Discharge pressure limited by

air pressure

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Calgary Pump Symposium 2013

Diaphragm Pump Performance Range

FLOW RANGE 0.5 to 300 GPM

VISCOSITY RANGE 0.1 cPs – 17,500 cPs

MAXIMUM DIFFERENTIAL PRESSURE

125 PSI (850 kPa)

TEMPERATURE RANGE -40°F to 212°F (-40°C to 100°C)

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Calgary Pump Symposium 2013

Example Applications

Waste water / sludge

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Calgary Pump Symposium 2013

Comparison of Technologies

Principle High Flows Low Flows High Pressure High Temperature

Internal Gear 1600 GPM 0.5 GPM 400 PSI 800°F

External Gear 1500 GPM 0.001 GPM 3000 PSI 500°F

Vane 2000 GPM 5 GPM 150 PSI 225°F

Lobe 800 GPM 5 GPM 400 PSI 400°F

3 Screw 3400 GPM 1 GPM 4500 PSI 500°F

2 Screw 5000 GPM 20 GPM 1500 PSI 650°F

Progressive Cavity 2400 GPM 1 GPM 1500 PSI 350°F

Hydraulic Diaphragm 70 GPM 0.001 GPM 6000 PSI 800°F

Air Diaphragm (AOD) 300 GPM 0.5 GPM 125 PSI 212°F

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Calgary Pump Symposium 2013

Comparison of Technologies

Principle High Viscosity Low Lubricity Dry Run Multiphase

Internal Gear Excellent Good Short No

External Gear Excellent Good Short No

Vane Fair Excellent Short No

Lobe Excellent Excellent Yes Yes

3 Screw Good Poor Short No

2 Screw Good Excellent Yes Yes

Progressive Cavity Excellent Good No Yes

Hydraulic Diaphragm Fair Excellent Yes Yes

Air Diaphragm (AOD) Fair Excellent Yes Yes

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Calgary Pump Symposium 2013

Comparison of Technologies

Principle Abrasive Liquids Liquids w/ Solids Shear Sensative

Internal Gear Yes No Yes

External Gear No No No

Vane No No No

Lobe Yes Yes Yes

3 Screw No No No

2 Screw Yes Yes Yes

Progressive Cavity Yes Yes Yes

Hydraulic Diaphragm Yes Yes Yes

Air Diaphragm (AOD) Yes Yes Yes

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Calgary Pump Symposium 2013

Comparison of Technologies

Principle Smooth Output Sealless Option Sanitary Option

Internal Gear Steady Output Yes Yes

External Gear Steady Output Yes NSF Options

Vane Steady Output Yes NSF Options

Lobe Slight Pulsing No Yes

3 Screw Steady Output Yes No

2 Screw Steady Output No Yes

Progressive Cavity Steady Output No Yes

Hydraulic Diaphragm Pulsed Output Inherently Sealless Yes

Air Diaphragm (AOD) Pulsed Output Inherently Sealless Yes

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Calgary Pump Symposium 2013

Other Considerations For Selection

• Frequency of maintenance and ease of repair • Spare part consistency/availability • Mechanical Efficiency • Total cost of ownership

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Calgary Pump Symposium 2013

Thank You

• UNDERSTAND LIQUID CHARACTERISTICS

• UNDERSTAND THE PUMPING SYSTEM

• UNDERSTAND THE PUMP PRINCIPLE