Dry Gas Seals 101 - Presentation

52
INTRODUCTION TO DRY GAS SEALS Mark Slotnick/Sales Engineer

Transcript of Dry Gas Seals 101 - Presentation

Page 1: Dry Gas Seals 101 - Presentation

INTRODUCTION TO DRY GAS SEALS

Mark Slotnick/Sales Engineer

Page 2: Dry Gas Seals 101 - Presentation

Introduction to DGS

• Compressor shaft sealing

• Dry gas seal history

• Dry gas seal features and operation

• Operating principals

• Dry gas seal arrangements

• Barrier seals

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Compressor Compressor

Shaft Shaft

Sealing Sealing

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Compressor Shaft Sealing

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• To isolate bearing cavity from the process cavity:– to prevent process gas from entering the

atmosphere– to prevent bearing oil contamination of the

process

Compressor shaft sealing

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Compressor Shaft Sealing-Oil Ring

Lube Oil Seal Oil Buffer Gas

Seal & Lube Oil

Seal Oiland

Buffer Gas

JournalBearing

CarbonSeal

Seal and Lube Oil System with Buffer Gas

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• Power loss due to oil shear

• Power loss due to seal oil pump and fans

• High seal gas decompression / venting and booster blowdowns rates- environmental considerations / loss of product

• Product contamination / pipe oil contamination

Compressor Shaft Sealing-Oil Ring

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• High cost of maintenance and downtime

• Fire hazards associated with wet oil systems

• High cost of oil disposal and spill cleanups - environmental protection

Compressor Shaft Sealing-Oil Ring

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Dry Gas SealDry Gas Seal

HistoryHistory

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Gas seal history

• 1968 First patent• 1975 First field applications

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Gas seal history

• 1968 First patent• 1975 First field applications• 1981 First beam type compressor• 1985 First steam turbine• 1985 First Mag brg / Dry seal• 1991 Bi-directional seal

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• 1968 First patent• 1975 First field applications• 1981 First beam type compressor• 1985 First steam turbine• 1985 First Mag brg / Dry seal• 1991 Bi-directional seal• 1992 XP seal - 123 to 200 bar

Gas seal history

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• 1968 First patent• 1975 First field applications• 1981 First beam type compressor• 1985 First steam turbine• 1985 First Mag brg / Dry seal• 1991 Bi-directional seal• 1992 XP seal - 123 to 200 bar• 1994 Type 82 barrier seal

Gas seal history

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Worlds Largest Gas Seal (330mm)

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• 1968 First patent• 1975 First field applications• 1981 First beam type compressor• 1985 First steam turbine• 1985 First Mag brg / Dry seal• 1991 Bi-directional seal• 1992 XP seal - 123 to 200 bar• 1994 Type 82 barrier seal introduced• 1997 Worlds Largest 330mm Gas Seal • 1997 Cranite 2000• 1997 500 bar test rig

Gas seal history

Page 16: Dry Gas Seals 101 - Presentation

• 1968 First patent• 1975 First field applications• 1981 First beam type compressor• 1985 First steam turbine• 1985 First Mag brg / Dry seal• 1991 Bi-directional seal• 1992 XP seal - 123 to 200 bar• 1994 Type 82 barrier seal introduced• 1997 Worlds Largest 330mm Gas Seal • 1997 Cranite 2000• 1997 500 bar test rig• 1998 100,000,000 operating hours exceeded• 2000 First 5000 psig balance piston seal

Gas seal history

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Features Features

and and

operationoperation

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• Reduces Capital Cost of New Installations

• Cartridge design simplifies installation and protects critical seal components

• Proven and reliable technology

– Over…

• 180 Million Operation Hours

• 15,000 Cartridge Seals Installed

Dry gas seal features

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• Extremely low process gas leakage

• Withstands rapid speed and pressure changes

• Theoretically, due to the non-contacting design feature, seal life can be considered unlimited

Dry gas seal features

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• Allowance for axial shaft shifts is normally + 0.125"

• Allowance for radial shaft shiftsis normally +.025"

• Capable of handling starts and stops at full pressure

Dry gas seal features

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• Eliminates Seal Oil Support System

• Reduces Maintenance Costs

• Saves Energy

• Prevents Oil Contamination

Dry gas seal features

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• Seal Reverse Rotation– Short periods of reverse rotation can be

tolerated without damage but should be avoided• Bi-directional seal designs are available

• Seal Reverse Pressurization– Not recommended

• Seal Liquid Contamination– Can tolerate small amounts of liquid

contamination, but should be avoided

Dry gas seal features / operation

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• Slow Roll/Turning Gear– Does not adversely affect seal performance

• Vibration– Seal will withstand vibration allowances of

API 617• Compressor Wash

– Compressor cleaning can be performed provided seals are isolated by a buffer gas

Dry gas seal features / operation

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• Mating Ring – Tungsten/Silicon Carbide

• Primary Ring– Carbon/Cranite 2000

• Hardware– 410SS/316SS/Hasteloy/other

• Springs– Hastelloy C

Dry gas seal materials

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Operating Operating

principals principals

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UNIDIRECTIONAL SPIRAL GROOVE

BIDIRECTIONAL SPIRAL GROOVE

Operating principals

Spiral Groove Comparison

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OUTER LAND

SPIRAL GROOVE

DIAMETER

GROOVE DIAMETER

INNER DIAMETER

ROTATION RELATIVE TO PRIMARY RING

Operating principals

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Direction of RotationGas is induced towards the center.

Gas is Compressed &Pressure increases toset Gap.

Sealing Dam

Operating principals

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Direction of Rotation Gas is induced towards the center.

Gas is Compressed &Pressure increases toset Gap.Sealing Dam

Operating principals

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Normal Gap

Compression

Expansion

Gas FilmPressureDistribution

Spring Load+ Hydrostatic

S P

CLOSING FORCE

FC

OPENING FORCE

FO

FC = FO

Operating principals

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Gas FilmPressureDistribution

Spring Load+ Hydrostatic

S P

CLOSING FORCE

FC

OPENING FORCE

FOFC >FO

Increased Gap

Operating principals

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Gas Film PressureDistribution

Spring Load+ Hydrostatic

S P

CLOSING FORCE

FC

OPENING FORCE

FOFC < FO

Reduced Gap

Operating principals

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Operating Principals

30

20

10

0 1 2 3 4 5 gap (m)

Combined Stiffness (Hydrostatic & Hydrodynamic)

Hydrostatic Stiffness Only

Sti

ffn

es

s (

GN

/m)

Non-Contacting Seal Hydrostaticand Hydrodynamic Stiffness

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Dry Gas Seal in Operation

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C-STEADY Analysis

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Seal Seal

arrangementsarrangements

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PR

OC

ES

S G

AS

S

IDE

Polymer Rings Carrier

Dry gas seals: AT vs XP

28 XP SEAL

PR

OC

ES

S G

AS

SID

E

28 AT SEAL

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Primary Vent Filtered Process Gas

Bearings Process Gas

SERVICE: PLANT AIR AND NITROGEN SERVICE

Dry gas seal arrangements

Pressure: Up To 1800 PSIG Temperature: -4 To +400°F Speed: Up To 660 Ft/Sec. Gases: All

SINGLE SEAL

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DGS Arrangements - XP Single Seal

SEALINGSEALINGGASGAS

BARRIERBARRIERGASGAS

PRIMARYPRIMARYLEAKAGELEAKAGE

PR

OC

ES

S

PR

OC

ES

S

CA

VIT

YC

AV

ITY

SERVICE: PLANT AIR AND NITROGEN SERVICE

BE

AR

ING

B

EA

RIN

G

CA

VIT

YC

AV

ITY

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N2 Purge Secondary Vent Primary Vent Filtered Process Gas

Bearings Process Gas

SERVICE: Natural Gas Pipeline Compressors and Process Gas Compressors

Pressure: Up To 1800 PSIG Temperature: -4 To +400°F Speed: Up To 660 Ft/Sec. Gases: All

Dry gas seal arrangementsTANDEM SEAL

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XP Tandem Seal

SEALINGSEALINGGASGAS

SECONDARYSECONDARYLEAKAGELEAKAGE

PRIMARYPRIMARYLEAKAGELEAKAGE

BARRIERBARRIERGASGAS

PR

OC

ES

S

PR

OC

ES

S

CA

VIT

YC

AV

ITY

BE

AR

ING

B

EA

RIN

G

CA

VIT

YC

AV

ITY

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N2 Purge Secondary Vent N2 Purge Primary Vent Filtered Process Gas

Bearings Process Gas

Pressure: Up To 1800 PSIG Temperature: -4 To +400°F Speed: Up To 660 Ft/Sec. Gases: All

SERVICE: Applications Where Zero Process Leakage Is Required

Dry gas seal arrangementsTANDEM SEAL WITH INTERMEDIATE LABYRINTH

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XP Tandem Seal w/ Int. Labyrinth

SEALINGSEALINGGASGAS

SEPARATIONSEPARATIONGAS (N2)GAS (N2)

BARRIERBARRIERGAS (N2)GAS (N2)

SECONDARYSECONDARYLEAKAGE (N2)LEAKAGE (N2)

PRIMARYPRIMARYLEAKAGELEAKAGE

PR

OC

ES

S

PR

OC

ES

S

CA

VIT

YC

AV

ITY

BE

AR

ING

B

EA

RIN

G

CA

VIT

YC

AV

ITY

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DGS Arrangements - Double Seal

BUFFER GASBUFFER GAS(PROCESS)(PROCESS)

SEALING GAS (N2)SEALING GAS (N2)SEPARATION (N2)SEPARATION (N2)

PR

OC

ES

S C

AV

ITY

PR

OC

ES

S C

AV

ITY

LEAKAGE LEAKAGE (N2)(N2)

BE

AR

ING

B

EA

RIN

G

CA

VIT

YC

AV

ITY

Pressure: Up To 400 PSIG Temperature: -4 To +400°F Speed: Up To 660 Ft/Sec. Gases: HCL, Styrene,CO,…Etc.

SERVICE: Toxic and Corrosive Environments

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• Resists seal hang-up due to O-Ring friction

• No explosive decompression problems associated with O-Rings

• Provides long shelf life

• Applications are not compromised by chemical compatibility of the O-Ring

Dry gas seals: AT vs. XP

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• Pressure:– AT: Up to 1800 PSIG– XP: Up to 2900 PSIG– EXP: Up to 6500 PSIG

• Temperature:– AT: -70 to +400°F– XP, EXP: -100 to +600°F

• Speed:– Up to 660 Ft./Sec.

Dry gas seal arrangements

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Barrier Barrier

sealsseals

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• Seal selection

• Associated controls

• Operation

Barrier seals

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• Carbon ring seal

• Split labyrinth

• Other

Barrier seals - Selection

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BE

AR

ING

SID

E

GA

S S

EA

L S

IDE

BUFFER GAS2ND STAGELEAKAGE

BEARINGVENT

Barrier seals - Carbon ring

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BUFFER GASBEARING

VENT2ND STAGELEAKAGE

Barrier seals - Split labyrinth

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• Barrier Seal

– N2 consumption < 1 scfm per side

– Seal life up to 5 years

– Floating seal prevents installation damage

• Split Labyrinth

– N2 consumption > 5 scfm per side

– Seal life indefinite (theoretically)

– Teeth can be damaged during installation

Barrier seals - comparison