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Page 1: Filters Seals & Bearings

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Page 2: Filters Seals & Bearings

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Filters, Seals & BearingsFilters, Seals & Bearings ( S )( S )

EMPDS Progress:EMPDS Progress:

Overall is 64.3 %Overall is 64.3 %

Core is 69.1 %Core is 69.1 %

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OIL  FILTER 2. AIR PANEL FILTER

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Micron is a unit of measurement used to express the degree of filtration. A micron equals one millionth of a meter or 0.0000394 inch. For comparison value, consider that the normal lower level of visibility to the naked eye is about 40 microns. (A grain of table salt measures about 100 microns; the thickness of a human hair is about 70 microns

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A mechanical seal is a sealing device which forms a running seal between rotating and stationary parts. Leakage can be reduced to a level meeting environmental standards of government regulating agencies and maintenance costs can be lower.

Advantages of mechanical seals over conventional packing are as follows:

•Zero or limited leakage of product (meet emission regulations.)• Reduced friction and power loss.• Elimination of shaft or sleeve wear.• Reduced maintenance costs.• Ability to seal higher pressures and more corrosive environments.• The wide variety of designs allows use of mechanical seals in almost all pump applications.

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PUMP SHAFT

BEARINGSIMPELLER

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AS THE PUMP SHAFT ROTATES

A LIQUID IS SUPPLIED TO THE PUMP “SUCTION”

CENTRIFUGAL FORCE EXPELS THE LIQUID OUT FROM THE IMPELLER

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• With the introduction of mechanical seals, this leakage could be controlled to a much greater degree.

• Let’s look at the same pump with a mechanical seal installed. Note that the seal shown is an L1 with O-Ring type stationary and a set screw collar.

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SEALING THE LIQUIDSEALING THE LIQUID

• It is a fact, all mechanical seals leak. Like packing, the mechanical seal “faces” must also be lubricated. With proper application and design however, the leakage is so minute that actual droplets of liquid are not detected. Instead, the lubricating liquid will vaporize as it crosses the seal faces and the leakage is a gas or vapor.

• Since we are discussing the sealing of the liquid at the faces, let’s take a look at the sealing points of a typical mechanical seal. Again, viewing the same pump and seal, note that there are four sealing points to consider.

ALLMECHANICAL SEALS

LEAK

Page 22: Filters Seals & Bearings

Sealing on the shaftO.D. of the stationary

The seal gland to the stuffing box

And finally, the seal faces

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BRIEF DISCUSSION BRIEF DISCUSSION ABOUT ABOUT

MECHANICAL SEAL MECHANICAL SEAL FACE DYNAMICSFACE DYNAMICS

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• The mechanical seal faces are obviously the most critical sealing point of a mechanical seal assembly.

• Although the faces can be manufactured from a variety of different materials, one is typically carbon, while the other is usually a hard material. (i.e. Alox (Aluminum Oxide Ceramic), Tungsten Carbide, Silicon Carbide, etc.)

• Flatness is measured in “Light Bands”. After lapping, the faces are placed on an “Optical Flat”, a clear glass surface where a monochromatic light is shined on the face. This single wavelength light will produce an image of rings or lines on the face. Each ring/line is “One Light Band”. Each light band is equivalent to .000011” or eleven millionths of an inch. This refers to the variations in the surface of the face. On most face materials, one to three light bands is LE-CON’s standard.

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• This illustration shows a face being inspected on an Optical Flat.

• Take notice of the light bands that are visible on the reflection of the face.

• Laying a straight edge on a tangent to the inside circumference of the face, how many light bands are crossed?

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Optically Flat Faces

0 psi

RotaryFace

StationaryFace

100 psi

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0 psi

25 psi

50 psi

Liquid

Liquid + Vapor

Vapor + Liquid

Vapor

Pressure Drop & Vaporization

100 psi

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ASME B16.2

• Gasket Seals • Spiral Wound Gaskets

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• Both pusher and non-pusher types can be either shaft mounted or cartridge assemblies.

• The basic difference between pusher and non-pusher types have to do with the dynamics of the shaft packing or O-ring and whether or not it moves as the seal wears.

• As the seal faces wear down over time, they must be closed to compensate for lost face material. If the shaft O-ring must move when this compensation takes place, it is pushed forward by the components of the seal and by stuffing box pressure. If the seal is configured with a “dynamic” O-ring of this type the seal is called a pusher type.

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• Pusher

• Non-Pusher

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Illustrated here is a common pusher seal. As the seal springs and other pressures in the stuffing box are exerted on the seal, closure of the faces is achieved.

Rotating face and dynamic O-ring.

Hard Stationary Face

Closing forces exerted on the seal faces

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As the softer carbon face wears down, the rotating face must move to maintain face closure.

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Minute particles of carbon and solids from the process liquidthat migrate across the seal faces build up on the shaft.

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This build up will ultimately cause the seal to “hang up” and in most cases, failure will occur well before the seal is actually “worn out”.

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• Metal bellows are constructed by welding “leaflets” into a series of “convolutions”. This series of convolutions is referred to as the “Bellows Core”.

• The photo shown here is a shaft mounted seal (Equivalent to John Crane Type 680).

• Now take a look at how a bellows seal compensate for face wear.

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Metal bellows

Carbon rotating face

Hard stationary face

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The bellows core expands to compensate for face wear.

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Debris can build up without causing hang up.This feature is probably the most notableselling point when comparing a bellows sealto a pusher type seal.

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• Dual seals can be either pressurized or non-pressurized. This is in reference to the artificial environment that is provided to exist “between” the seals.

• A non-pressurized dual seal, also known as a “Tandem” arrangement, means that the inner, or primary seal is functioning as would a single seal. It is subject to stuffing box conditions, i.e. stuffing box pressure, process liquid to lubricate the faces and usually immersion of seal components in the process liquid. The secondary, or outside seal runs in a non-pressurized “Buffer” liquid that is supplied from an outside source, typically a nearby supply tank.

• In a non-pressurized dual arrangement, the outside seal is primarily there as a containment device in the event that the inside or primary seal is lost. A “Back up” or safety mechanism if you will.

• Let’s look at a Dual Cartridge Seal.

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Inside or Primary seal

Outside or Secondary Seal

Immersed in process liquid in the stuffing box

Buffer fluid warmedby seal generatedheat returns to thebuffer supply tank

Cool buffer fluid from the buffer supply tank entersvia the inlet port

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• Since the outside or secondary seal runs in a non-pressurized clean lubricating liquid, it will generally last for an extended period of time. When the inside or primary seal fails, the leakage through the faces will be contained by the secondary seal until the pump can be shut down for seal replacement.

• Failure indication and shutdown devices can be attached to the buffer supply so that the pump operators know when the primary seal has failed.

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• When pumping volatile liquids, hazardous, corrosive, abrasive, etc. it is sometimes necessary to insure that the process liquid does not enter the atmosphere or the artificial environment created for the seal or even the seal faces.

• Pressurizing the artificial environment, 20 to 30 psi. above the pump stuffing box pressure will prevent process liquid from crossing the primary seal faces. Instead, boundary layer film liquid is supplied to the primary seal by the artificial environment or “Barrier”.

• The arrangement of seals can be the same as a non-pressurized in most cases. The difference is in how the seals perform.

• In a pressurized dual seal, the outboard or secondary has the tougher job of the two. It operates sealing high barrier pressure while the inboard or primary seal has clean lubricating liquid applied at differential pressure of only 20 to 30 psi.

• Now let’s look at the environmental controls for operating dual seals.

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Pressurized Dual Seal

Artificial Environment“Barrier” System

Non-Pressurized Dual Seal

Artificial Environment“Buffer” System

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TO FLARE / TO FLARE / RECOVERY SYSTEMRECOVERY SYSTEM

DISCHARGEDISCHARGE

SU

CT

ION

SU

CT

ION

NON-PRESSURIZEDNON-PRESSURIZEDBUFFER FLUIDBUFFER FLUIDPLAN PLAN 5252 / / 73527352

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PRESSURIZED BARRIER FLUIDPRESSURIZED BARRIER FLUIDPLAN PLAN 5353 / / 73537353

PRESSURIZED GAS INPRESSURIZED GAS IN

DISCHARGEDISCHARGE

SUCTIONSUCTION

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• It is split radially as shown in this photo.

• All internal components are also split and they are assembled onto the equipment shaft without removing the equipment from it’s operating position or tearing down it’s major components.

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System design issues

80% of seals fail prematurely because of contamination The seal manufacturer is rarely consulted on the system

design

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Process Gas

FI FI

FILTER MODULE

PROCESSGAS

EXTERNALGAS

Filtered Process Gas For extended reliability

clean / dry seal gas is the MOST important• Gas should be filtered

to around 2 micron• Coalescing filters can

be used to dry the gas• Heaters can be used to

provide superheat• Heat tracing should be

used to prevent heat loss

• SEPro type systems can be used to provide static gas flow

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AF 15256 Gas Composition

0

20

40

60

80

100

120

140

160

180

-180 -160 -140 -120 -100 -80 -60 -40 -20 0 20 40 60

Temperature (C)

Pre

ssur

e (b

ar)

dew line bubble line Adiabatic Expansion Hydrate Curve (1% H2O)

• Check adiabatic expansion

• Check hydrate formation

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AF 15254-59°C Dew Point

0

20

40

60

80

100

120

140

160

180

-200 -150 -100 -50 0 50 100 150

Temperature (C)

Pre

ss

ure

(b

ar)

dew line bubble line Adiabatic Expansion Hydrate Curve

Gas from Skid Seal Gas DE Seal Gas NDE

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AF 15254-59°C Dew Point

0

20

40

60

80

100

120

140

160

180

-200 -150 -100 -50 0 50 100 150

Temperature (C)

Pre

ss

ure

(b

ar)

dew line bubble line Adiabatic Expansion Hydrate Curve

Gas from Skid Seal Gas DE Seal Gas NDE

Measured operating points from Data capture system

Predicted worst case expansion line

Actual worst case expansion line passing through liquid region

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• A knock out pot will effectively drop out free liquids in the gas

• This design incorporates a level gauge

A knockout pot recently supplied by John Crane Germany

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• Use a coalescing filter – It effectively get rid of

liquids– It needs a continuous

drain– It produces a saturated

gas with no free liquid

A John Crane Coalescing filter element

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• Use a heater to provide superheat to the gas– As long as the temperature in the seal does not drop below the temp

at the coalescing filter the seal will operate on clean dry gas– This will dramatically prolong seal life

Don't forget to lag and heat trace the lines down stream of the filter

Don’t leave the seal pressurised without clean gas flow – it will cool down and liquids will occur• If long periods of pressurised standby are

envisaged use a SEPro system to circulate the gas

A John Crane seal gas heater unit recently supplied to Trinidad

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Rotoflow turbo expanders are equipped with magnetic bearings, which offer an alternative to conventional oil bearing systems for many applications.

This bearing requires no lubrication, oil system components, pumps, filters, coolers, etc and the risk of process contamination is eliminated.

In magnetic bearing system the rotor is suspended by electromagnetic forces and there is no contact between the stator and rotor. The standard S2M magnetic bearings are active and consists of two radial bearings and an axial thrust bearing.

The magnetic bearing is a mechanical device with its control electronics.

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attraction

attraction

Magnetic radial bearings

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Signal controller

Power amplifier

1

Power amplifier

2

Magnetic radial bearings control system

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Magnetic thrust bearing system

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Bearings Mounting

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Bearings Mounting

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Bearings Mounting

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Dismounting Bearings

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Dismounting Bearings

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QUESTIONS

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