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Introduction
General description and main features
GE Oil & Gas
Oil & Gas Industry Applications
Customer Training
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Centrifugal Compressor Training Course
22/11/2012
What is a Compressor?
A machine used to increase the
pressure of a GAS
Introduction Customer Training
Customer Training
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Centrifugal Compressor Training Course
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What is a Gas?
Gas is one of the three classical states of
matter characterized by molecular weight
(MW), pressure (p) and temperature (T)
Introduction Customer Training
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Centrifugal Compressor Training Course
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Customer Training
Gas compression
Gas
ps
Gas
pd
Mechanical
power
Introduction
Customer Training
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Centrifugal Compressor Training Course
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What we need to compress a gas?
For many reasons: to transport it,
to enhance an oil field production, etc…
Introduction
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Centrifugal Compressor Training Course
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Customer Training
Compression Services
Pipeline inspection device
Offshore production platform
Subsea equipment
Oil/Gas field
Re-injection plant
Oil / gas processing plant
LNG receiving plant
LNG liquefaction plant
Gas boosting station
Oil boosting station
Power generation plant
Natural Gas storage plant
Refinery / Petrochemical /
fertilizer plant
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Centrifugal Compressor Training Course
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Customer Training
Compression Services
Distribution
Midstream Downstream
Upstream
• Exploration &
Production
 Re-injection
 Gas Lift
 Gas Gathering
 Export Gas
•Gas Plants
 Feed Gas
 Gas Treatment
• LNG
 Mixed Refrigerant
 Propane
• Pipelines
 Gas Boosting
 HP Transport
 Gas Storage (Injection +
withdrawal)
• Refinery
 HCU, HDT, HDS
 Recycle
 Air Feed
 FCC
• Petrochemical/
Fertilizers
 Syngas
(Ammonia, Methanol)
 Refrigeration
 CO2 Compression
(Urea)
 Feed Gas
 Charge Gas
 Ethylene & derivatives
• NGV Re-fuelling
 Cubogas
Nuovo Pignone Compressors
GE Oil & Gas
Oil & Gas Industry Applications
9
Centrifugal Compressor Training Course
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Customer Training
Vertically split
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
Horizontally split
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
Single Volute
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
Nuovo Pignone TAGs
BCL 406
2
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
Nuovo Pignone TAGs
BCL 406
Casing
B=barrel
P=pipeline
M=Middle Split
S=single volute
Impeller design
C=closed
R=open
Diffuser
L=free vortex (not vaned)
2
Literal Part
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
2 BCL 406
BCL 406 /A
Casing design pressure rating
 N p<150 bar
 A p<200 bar
 B p<300 bar
 C p<400 bar
 D p<550 bar
 E p up to 1000 bar
Barrel Type
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
 Pipeline compressors are designed to maximize compression efficiency over the broad range of
operating conditions required by gas pumping stations;
 Suction and discharge nozzles for gas transportation are generally located opposite each other to
meet station layout requirements.
pmax 150 bar
PCL 406
Pipeline Type
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
Low pressure applications
2 MCL 406
Middle Split Type
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
SRL
Integrally geared
Single stage
 Impeller overhung mounted on the shaft;
 Each impeller has the discharge volute.
Single Volute Type
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
IMPELLERS design
R= open type
C= closed type
2 BCL 406
Compressors overview
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Customer Training
Free vortex DIFFUSER
Diffuser
No fixed blades
2 BCL 406
Compressors overview
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Centrifugal Compressor Training Course
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Customer Training
Nuovo Pignone TAGs
BCL 406
n. of
impellers
Nominal diameter of the
impeller
Section arrangment
2
Numerical Part
Compressors overview
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Customer Training
Nominal size (mm)
400 mm
BCL 406
2
Compressors overview
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Customer Training
BCL...MCL...
Section arrangment
suction discharge
 One compression section;
 In line configuration.
Compressors overview
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Customer Training
2 BCL... 2 MCL...
Section arrangment
1 st
suction
1 st
discharge
2 nd
suction
2 nd
discharge
 Two compression sections in a single
casing;
 Back to back configuration;
 Cooling of the gas;
 Tmax 250°C.
Compressors overview
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Customer Training
3 BCL... 3 MCL...
Section arrangment
 More than two compression sections
in a single casing;
 Sidestreams.
suction discharge
sidestreams
Compressors overview
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Customer Training
D BCL... D MCL...
Section arrangment
suction
discharge
 Two compression sections in parallel in the
same casing;
Compressors overview
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Customer Training
Technology Selection Map
Compressors overview
Compressor rotating parts
GE Oil & Gas
Oil & Gas Industry Applications
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Customer Training
Rotating parts
Shaft
Thrust Collar
Impellers
Spacers
Balance drum
Coupling hub
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Customer Training
Thrust Collar
 Transmits the rotor thrust to the thrust bearing;
 Fixes the axial position of the rotor;
 Hydraulically shrink-fitted to the shaft;
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Customer Training
Impeller
The function of the
impeller is to add
energy to the gas.
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Customer Training
Impeller
In order to minimize erosion and corrosion effects on impeller due to pitting or fouling phenomenon
related to gas composition, it is possible to use special stainless steel alloy with Ni-Cr-Mo or apply a
specific protective coating.
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Customer Training
The blades are bended
Impeller
The blades are bended and twisted
Impellers are fully customized
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Customer Training
Balancing Drum
 Balances part of the axial thrust;
 Interference fitted and keyed;
 Positioned after the last impeller;
 Holes for rotor balancing.
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Customer Training
Coupling
FLEXIBLE DRY type design is mostly used by NP
HUB
No lubrication is needed
Connects elements between compressor and the remaining equipment of a compressor
train.
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Customer Training
Coupling
Basically a flexible coupling has the following functions:
2. Accommodate Parallel Offset and/or Angular misalignment
1. Physically connect two rotating shafts
3. Compensate for axial movement of coupled shafts
Compressor stator parts
GE Oil & Gas
Oil & Gas Industry Applications
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Customer Training
Stator parts
Diaphragms
Bearings
Seal
End cover
Flanges and Nozzles
Bearings
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Customer Training
Stator parts
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Centrifugal Compressor Training Course
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Customer Training
BCL: Casing-Diaphragms
LOWER HALF
UPPER HALF
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Customer Training
Casing-Diaphragms: bundle
Diaphragms
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Centrifugal Compressor Training Course
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Customer Training
Casing-Diaphragms: bundle
Labyrinth
seals
Diffuser
Return channel
Blades
Impeller
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Centrifugal Compressor Training Course
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Customer Training
Casing-Diaphragms: bundle
Suction volute Discharge volute
In new barrel compressors the inlet and disharge volutes are separated from the inermediate
diaphragms.
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Customer Training
Casing-Diaphragms: bundle
The upper half of the bundle is lowered on the lower
half.
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Customer Training
Horizontally split
The diaphragms are installed in the casing without a countercasing
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Centrifugal Compressor Training Course
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Customer Training
Flanges and nozzles
Discharge Sideflow Suction
Discharge
Suction
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Centrifugal Compressor Training Course
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Customer Training
Flanges and nozzles
In the barrel type for high or very high pressure, piping is directly connected to the casing
without nozzles;
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Centrifugal Compressor Training Course
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Customer Training
Shear and Shim rings
Shear ring
Shim ring
Locking system using
shear and shim rings
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Customer Training
Head cover
The functions of the head cover are:
 Close the bundle inside the casing;
 Guide the flow;
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Centrifugal Compressor Training Course
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Customer Training
Bearings
Thrust bearing
 Direct Lubricated: lube oil is provided for each pad
through a groove manufactured on the pads
 Flooded: Oil fills the bearing assembly and drains
from the top through a flow control orifice
Tilting pads type are adopted. The function of the thrust
bearing is to compensate part of the axial thrust.
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Customer Training
Thrust Bearings Components
Thrust bearing are self equalizing: the bearing distributes the load equally between all pads.
Thrust shoes
Base ring
Leveling plates
Thrust collar
Pivot
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Customer Training
Journal Bearing
Jourbal bearing
Tilting pads type are adopted.
The functions of the journal bearing are:
 Support the rotor weight
 Create a lifting effect
 Damping effect
Two types of possible lubrication:
 Direct lubrication: Lube oil is provided for each pad through a
groove manufactured on the pads
 Flooded lubrication: The oil enter from an orifice in the upper
part of the bearing and exits in the lower part after the
lubriction of pads.
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Customer Training
Journal Bearing
Bearings pad
Bearings casing
Pivot
Centrifugal Compressor Gas Path
GE Oil & Gas
Oil & Gas Industry Applications
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Centrifugal Compressor Training Course
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Customer Training
SUCTION DISCHARGE
Gas Path
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Centrifugal Compressor Training Course
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Customer Training
Shaft
Inlet Volute
Fin
Casing
Blade
Impeller
Suction Nozzle
Suction Pipe
Suction
The gas flow is directed towards the
eye of the first impeller.
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Customer Training
Suction
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Centrifugal Compressor Training Course
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Customer Training
Labyrinth
Seal
Suction
diaphragm
Labyrinth
Seal
Shaft
Key
Disk
Suction
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Customer Training
Intermediate stages
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Centrifugal Compressor Training Course
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Customer Training
Single stage
Labirinth
seals
Diffuser
Return channel
Blades
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Customer Training
C3=C1
optimal condition
Gas Inlet
Increased
velocity
P4,C4
P1,C1
P2,C2
P3,C3
+ +
+
++ +
Single stage
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Customer Training
Single stage
Impeller
Inlet
Blade
Inlet
Diffuser
Inlet
Diffuser
Outlet
Velocity
Pressure
Energy
1 2 3 4
1
2
3
4
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Customer Training
Last impeller
Discharge volute
Discharge
Centrifugal Compressor Axial Thrust
GE Oil & Gas
Oil & Gas Industry Applications
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Customer Training
Axial Thrust
Axial thrust
P2 > P1
P2
P2
P1
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Centrifugal Compressor Training Course
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Customer Training
Axial Thrust
Balancing Drum
The BALANCE DRUM is a disk installed after the last impeller in order to balance part of the axial
thrust (80÷85%).
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Customer Training
Axial Thrust
P2
P1
P2
Ps
R1 R2 Rd
Axial Force Drum Force
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Centrifugal Compressor Training Course
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Customer Training
Axial Thrust
Balancing
Line
Ps Pd Ps+ΔP
Ps= Suction Pressure
Ps = Discharge Pressure
ΔP= Pressure Drop on balancing line
Axial Force Drum Force
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Customer Training
Balancing line
Centrifugal Compressor
Performance Curves
GE Oil & Gas
Oil & Gas Industry Applications
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Customer Training
Performance Curves
 Polytropic Head
 Polytropic Efficiency
 Pressure Ratio
 Power
 Discharge Temperature
 Discharge Pressure
Performance curves describe the relation of the centrifugal compressor operating
parameter and the inlet capacity.
The performance curves are valid ONLY for the condition specified in the performance diaghram...
Qinlet
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Customer Training
Operating Range Maximum
continuous speed
(MCS)
Minimum
operating speed
(MOS)
Discharge
pressure
(bar
a)
Normal operating
point
Qinlet
Choking Area
Surge Limit
Line
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Customer Training
Operating point Plant
resistance curve
Operating
point
 The plot represents the
envelope of all the possible
operating conditions relevant
to the given suction parameter.
 The actual operating point is
unique and it is always the
intersection between the
compressor curve at the given
speed and the plant
resistance curve.
Qinlet
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Customer Training
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Customer Training
Off-design conditions
Discharge
pressure
MW
MW
Qinlet
Ts
Ts
Ps
Ps
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Customer Training
Other map variation cause:
Normal working
graph
Internal recycles
effect
Discharge
pressure
Qinlet
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Customer Training
According to API 617 the following regulating methods are defined:
 Speed Variation
 Suction throttling
 Variable inlet guide vanes (VIGV)
 Discharge blowoff
 Cooled bypass
Regulation
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Customer Training
Discharge
pressure
Regulation
Qinlet
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Customer Training
Discharge
pressure
Regulation
Qinlet
Choke, Stall, Surge and
Anti-surge Control System
GE Oil & Gas
Oil & Gas Industry Applications
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Customer Training
Choking
Choking Area
Choke rapresents the right limit of performance
curve.
Rapid decrease in performances and
efficiency.
Discharge
pressure
Qinlet
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Customer Training
Surge
 Surge is the left limit of performance curve, on the left of this line the compressor operates in
unstable condition;
 Represents the maximum polytropic head of the curve;
 All surge points, defined for different speeds represent the Surge Limit Line;
Surge Limit
Line
Discharge
pressure
Qinlet
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Customer Training
Surge
P2
P1
P2 > P1
Flow inside the impeller
Axial thrust
Normal operating
conditions
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Customer Training
Surge
P2
P1
Flow inside the impeller
Axial thrust
P1 > P2
Surge condition
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Customer Training
Factors leading to surge
During NORMAL OPERATION:
 High discharge pressure (Increase of plant resistance);
 Reduction of suction pressure;
 Increase of suction temperature.
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The Antisurge System is composed by:
 Antisurge Valve
 Instrumentation:
 Flow indicator trasmitter
 Pressure indicator trasmitter
 Electronic controller
Antisurge system
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Customer Training
Antisurge system
PRESSURE
TRANSMITTER
ANTISURGE VALVE
COMPRESSOR
FT PT PT
ANTISURGE
CONTROL
FLOW
TRANSMITTER
PRESSURE
TRANSMITTER
The opening of the Antisurge Valve increases the suction flow moving the operating point along the
speed.
The purpose of the Antisurge Control System is to avoid that the operating point reaches the SLL.
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…just a clarification:
The systems work together but are separately.
Antisurge system
The anti-surge controller is a special electronic device that interacts with the
main control panel but is not depending from it.
Lube Oil System
GE Oil & Gas
Oil & Gas Industry Applications
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Customer Training
Lube Oil System
The function of the lube oil system is to provide the
right amount of lube oil to bearings with the desired
viscosity by regulating pressure and temperature.
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Customer Training
Lube Oil System P&ID
Tank
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Customer Training
Lube Oil System P&ID
Main
pump
Auxiliary pump Emergency pump
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Customer Training
Lube Oil System P&ID
PCV
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Customer Training
Lube Oil System P&ID
TCV
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Customer Training
Lube Oil System P&ID
Filters
Dry Gas Seals System
GE Oil & Gas
Oil & Gas Industry Applications
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Customer Training
Sealing systems
The function of the sealing system is to avoid gas leakages
Statoric part
Rotating part
Gap
 Gas property is to occupy all the available volume
 Gas moves from high pressure sections to low pressure ones
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Sealing systems
The function of the sealing system is to avoid two types of leakage
Process gas leakages between the
compression stages
Process gas leakages towards the
atmosphere
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Customer Training
Types of seals:
 Fluid dynamic seals
 Labyrinth seals
 O-Ring gaskets
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Customer Training
Labyrinth Seals
Plain Stepped Abradable
A labyrinth seal is a type of mechanical seal that minimize the gas leakages. Labyrinth seals on
rotating shafts provide non-contact sealing action by controlling the passage of fluid through a
series of teeth.
Efficiency
Main purpose is to minimize internal leakages
close to the impellers due to different
pressure value at inlet and discharge.
 Eye of the impeller
 Foot of the impeller
 Balance drum
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Customer Training
Balancing Line
Shaft End Seal Shaft End Seal
Balancing Drum
Shaft end sealing
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Customer Training
Dry gas seal system
Mechanical dry gas seal are
supplied as cartridges.
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Customer Training
DGS: main components
Stationary ring
Rotating ring
Spring
Seal gas
SHAFT
Process
side
Athmosphere
side
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Customer Training
Operating conditions
Static Pressure +
Spring Thrust
Dynamic
Pressurization
Process Side
Stationary ring Rotating ring
Seal
gas
Seal
gas
The pressure profile at the
interface is self adjuxting to
restore to a position of equilibrium
 Gas enters the groove moving towards the center;
 Gas is compressed and pressure increases setting the gap between the rings.
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Customer Training
Shaft rotation Shaft rotation
Dry gas seal
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Customer Training
Gas source
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Customer Training
Intermediate Labyrinth
Product side
Outboard seal
Inboard seal
Seal gas STREAM 1
Primary vent (leakage from inbord seal
+ intermediate buffer gas - to flare) STREAM 2
Intermediate buffer
gas (N2)
STREAM 3
Secondary vent (leakage from Outbord seal
+ separation gas - atmospheric) STREAM 4
Separation gas (N2)
STREAM 5
Atmosphere
(Bearing chamber)
Separation seal
Inner seals
Carbon rings
Face
Seat
Seat
Face
Nomenclature TANDEM type:
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Customer Training
Process gas
side
Bearings
side
Buffer-Process gas
supply
Seal
gas supply
N2
Seal gas
leakage Separation gas
N2
Inner seal Inboard seal Outboard seal Separation seal
Dry gas seal: DOUBLE type
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Tertiary seal
The function of the tertiary seal is to avoid the oil vapours entering into the dry gas seal.
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Customer Training
Dry Gas Seal System P&ID
Seal Gas Filters
Buffer Gas Filters
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Customer Training
Dry Gas Seal System P&ID
Buffer Gas
PCV
Seal Gas
PCV
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Customer Training
Dry Gas Seal System P&ID
Primary Vent
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Customer Training
Dry Gas Seal System P&ID
Secondary Vent
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Customer Training
Dry Gas Seal System P&ID
Seal Gas
Heater
Vibrations Overview
GE Oil & Gas
Oil & Gas Industry Applications
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Customer Training
The measure of the mechanical behavior of a compressor is given by the amplitude
and frequency of the rotor vibrations.
The rotor vibration amplitude must not cause:
 Contact between rotating and stator parts;
 Dry gas seals overloading;
 Fatigue in the bearings.
Mechanical behavior
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The typical vibrations of the centrifugal compressors can be classified with reference to
the frequency and the nature of the force causing vibrations.
According to the first classification (frequency) the vibration may be:
 Synchronous
The vibration frequency corresponds to the machine rotation speed (ωR)
 Asynchronous
The vibration frequency is different from the machine rotation speed (ω R)
Vibrations classification
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Syncronous vibrations
𝜔 = 𝜔𝑅
The most common causes are:
 Unbalance in the rotor system;
 Rotor and stator parts contact;
 Fouling deposit.
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Asyncronous vibrations
It is necessary to do another distinction between frequency of the vibration and
machine rotational speed
 Frequency of the vibration multiple of ωR
 Frequency of the vibration lower or higher than ωR
𝜔 = 𝐾𝜔𝑅
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Asyncronous vibrations
Frequency of the vibration multiple of ωR
𝜔 = 𝐾𝜔𝑅
The most common causes are:
 Coupling misalignment;
 Loose of interference in some rotor components.
𝜔 = 2𝜔𝑅
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Customer Training
Asyncronous Vibrations
Frequency of the vibration lower or higher than ωR
The most common causes are:
 High clearance in journal bearings
 Oil whip;
 Aerodynamic effects
(rotating stall in diffusers)
 Cross - coupling
𝜔 = 0.5 𝜔𝑅
𝜔 = ( 0.4 − 0.5 ) 𝜔𝑅
𝜔 = ( 0.1 − 0.2 ) 𝜔𝑅
𝜔 = 0.2 𝜔𝑅
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What are the problems?
The main problem that we have to consider when a rotor-bearing system is
subjected to a periodic force is the phenomenon of RESONANCE.
 A system is in resonance when vibration amplitude becomes maximum;
 This occurs when the frequency of a periodic force (excitation frequency), applied to a rotor-
bearing system, corresponds to a natural frequency of that system.
A centrifugal compressor has many natural frequencies that are colled Critical
Speeds;The most important are the first and the second; It is necessary to determine the
field operation speeds that avoid the resonance.
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NC1 = Rotor first critical, center frequency, cycles per minute
Ncn = Critical speed, n th
Nmc = Maximum continuous speed, 105 percent
N1 = Initial (lower) speed at 0,707 x peak amplitude (critical)
N2 = Final (higher) speed at 0,707 x peak amplitude (critical)
SM = Separation margin
API 617
𝑁1 𝑁2
𝑁𝑐1
0.707 𝑝𝑒𝑎𝑘
𝑆𝑀
𝑜𝑝𝑒𝑟𝑎𝑡𝑖𝑛𝑔
𝑠𝑝𝑒𝑒𝑑𝑠
𝑁𝑐𝑛
𝑁𝑚𝑐
𝑉𝑖𝑏𝑟𝑎𝑡𝑖𝑜𝑛
𝑙𝑒𝑣𝑒𝑙
𝐴𝐹 =
𝑁𝑐𝑖
𝑁2 − 𝑁1
𝑆𝑀
123
Centrifugal Compressor Training Course
22/11/2012
Customer Training

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GE centrifugal compressors.pdf

  • 1. Introduction General description and main features GE Oil & Gas Oil & Gas Industry Applications
  • 2. Customer Training 2 Centrifugal Compressor Training Course 22/11/2012 What is a Compressor? A machine used to increase the pressure of a GAS Introduction Customer Training
  • 3. Customer Training 3 Centrifugal Compressor Training Course 22/11/2012 What is a Gas? Gas is one of the three classical states of matter characterized by molecular weight (MW), pressure (p) and temperature (T) Introduction Customer Training
  • 4. 4 Centrifugal Compressor Training Course 22/11/2012 Customer Training Gas compression Gas ps Gas pd Mechanical power Introduction
  • 5. Customer Training 5 Centrifugal Compressor Training Course 22/11/2012 What we need to compress a gas? For many reasons: to transport it, to enhance an oil field production, etc… Introduction
  • 6. 6 Centrifugal Compressor Training Course 22/11/2012 Customer Training Compression Services Pipeline inspection device Offshore production platform Subsea equipment Oil/Gas field Re-injection plant Oil / gas processing plant LNG receiving plant LNG liquefaction plant Gas boosting station Oil boosting station Power generation plant Natural Gas storage plant Refinery / Petrochemical / fertilizer plant
  • 7. 7 Centrifugal Compressor Training Course 22/11/2012 Customer Training Compression Services Distribution Midstream Downstream Upstream • Exploration & Production  Re-injection  Gas Lift  Gas Gathering  Export Gas •Gas Plants  Feed Gas  Gas Treatment • LNG  Mixed Refrigerant  Propane • Pipelines  Gas Boosting  HP Transport  Gas Storage (Injection + withdrawal) • Refinery  HCU, HDT, HDS  Recycle  Air Feed  FCC • Petrochemical/ Fertilizers  Syngas (Ammonia, Methanol)  Refrigeration  CO2 Compression (Urea)  Feed Gas  Charge Gas  Ethylene & derivatives • NGV Re-fuelling  Cubogas
  • 8. Nuovo Pignone Compressors GE Oil & Gas Oil & Gas Industry Applications
  • 9. 9 Centrifugal Compressor Training Course 22/11/2012 Customer Training Vertically split Compressors overview
  • 10. 10 Centrifugal Compressor Training Course 22/11/2012 Customer Training Horizontally split Compressors overview
  • 11. 11 Centrifugal Compressor Training Course 22/11/2012 Customer Training Single Volute Compressors overview
  • 12. 12 Centrifugal Compressor Training Course 22/11/2012 Customer Training Nuovo Pignone TAGs BCL 406 2 Compressors overview
  • 13. 13 Centrifugal Compressor Training Course 22/11/2012 Customer Training Nuovo Pignone TAGs BCL 406 Casing B=barrel P=pipeline M=Middle Split S=single volute Impeller design C=closed R=open Diffuser L=free vortex (not vaned) 2 Literal Part Compressors overview
  • 14. 14 Centrifugal Compressor Training Course 22/11/2012 Customer Training 2 BCL 406 BCL 406 /A Casing design pressure rating  N p<150 bar  A p<200 bar  B p<300 bar  C p<400 bar  D p<550 bar  E p up to 1000 bar Barrel Type Compressors overview
  • 15. 15 Centrifugal Compressor Training Course 22/11/2012 Customer Training  Pipeline compressors are designed to maximize compression efficiency over the broad range of operating conditions required by gas pumping stations;  Suction and discharge nozzles for gas transportation are generally located opposite each other to meet station layout requirements. pmax 150 bar PCL 406 Pipeline Type Compressors overview
  • 16. 16 Centrifugal Compressor Training Course 22/11/2012 Customer Training Low pressure applications 2 MCL 406 Middle Split Type Compressors overview
  • 17. 17 Centrifugal Compressor Training Course 22/11/2012 Customer Training SRL Integrally geared Single stage  Impeller overhung mounted on the shaft;  Each impeller has the discharge volute. Single Volute Type Compressors overview
  • 18. 18 Centrifugal Compressor Training Course 22/11/2012 Customer Training IMPELLERS design R= open type C= closed type 2 BCL 406 Compressors overview
  • 19. 19 Centrifugal Compressor Training Course 22/11/2012 Customer Training Free vortex DIFFUSER Diffuser No fixed blades 2 BCL 406 Compressors overview
  • 20. 20 Centrifugal Compressor Training Course 22/11/2012 Customer Training Nuovo Pignone TAGs BCL 406 n. of impellers Nominal diameter of the impeller Section arrangment 2 Numerical Part Compressors overview
  • 21. 21 Centrifugal Compressor Training Course 22/11/2012 Customer Training Nominal size (mm) 400 mm BCL 406 2 Compressors overview
  • 22. 22 Centrifugal Compressor Training Course 22/11/2012 Customer Training BCL...MCL... Section arrangment suction discharge  One compression section;  In line configuration. Compressors overview
  • 23. 23 Centrifugal Compressor Training Course 22/11/2012 Customer Training 2 BCL... 2 MCL... Section arrangment 1 st suction 1 st discharge 2 nd suction 2 nd discharge  Two compression sections in a single casing;  Back to back configuration;  Cooling of the gas;  Tmax 250°C. Compressors overview
  • 24. 24 Centrifugal Compressor Training Course 22/11/2012 Customer Training 3 BCL... 3 MCL... Section arrangment  More than two compression sections in a single casing;  Sidestreams. suction discharge sidestreams Compressors overview
  • 25. 25 Centrifugal Compressor Training Course 22/11/2012 Customer Training D BCL... D MCL... Section arrangment suction discharge  Two compression sections in parallel in the same casing; Compressors overview
  • 26. 26 Centrifugal Compressor Training Course 22/11/2012 Customer Training Technology Selection Map Compressors overview
  • 27. Compressor rotating parts GE Oil & Gas Oil & Gas Industry Applications
  • 28. 28 Centrifugal Compressor Training Course 22/11/2012 Customer Training Rotating parts Shaft Thrust Collar Impellers Spacers Balance drum Coupling hub
  • 29. 29 Centrifugal Compressor Training Course 22/11/2012 Customer Training Thrust Collar  Transmits the rotor thrust to the thrust bearing;  Fixes the axial position of the rotor;  Hydraulically shrink-fitted to the shaft;
  • 30. 30 Centrifugal Compressor Training Course 22/11/2012 Customer Training Impeller The function of the impeller is to add energy to the gas.
  • 31. 31 Centrifugal Compressor Training Course 22/11/2012 Customer Training Impeller In order to minimize erosion and corrosion effects on impeller due to pitting or fouling phenomenon related to gas composition, it is possible to use special stainless steel alloy with Ni-Cr-Mo or apply a specific protective coating.
  • 32. 32 Centrifugal Compressor Training Course 22/11/2012 Customer Training The blades are bended Impeller The blades are bended and twisted Impellers are fully customized
  • 33. 33 Centrifugal Compressor Training Course 22/11/2012 Customer Training Balancing Drum  Balances part of the axial thrust;  Interference fitted and keyed;  Positioned after the last impeller;  Holes for rotor balancing.
  • 34. 34 Centrifugal Compressor Training Course 22/11/2012 Customer Training Coupling FLEXIBLE DRY type design is mostly used by NP HUB No lubrication is needed Connects elements between compressor and the remaining equipment of a compressor train.
  • 35. 35 Centrifugal Compressor Training Course 22/11/2012 Customer Training Coupling Basically a flexible coupling has the following functions: 2. Accommodate Parallel Offset and/or Angular misalignment 1. Physically connect two rotating shafts 3. Compensate for axial movement of coupled shafts
  • 36. Compressor stator parts GE Oil & Gas Oil & Gas Industry Applications
  • 37. 37 Centrifugal Compressor Training Course 22/11/2012 Customer Training Stator parts Diaphragms Bearings Seal End cover Flanges and Nozzles Bearings
  • 38. 38 Centrifugal Compressor Training Course 22/11/2012 Customer Training Stator parts
  • 39. 39 Centrifugal Compressor Training Course 22/11/2012 Customer Training BCL: Casing-Diaphragms LOWER HALF UPPER HALF
  • 40. 40 Centrifugal Compressor Training Course 22/11/2012 Customer Training Casing-Diaphragms: bundle Diaphragms
  • 41. 41 Centrifugal Compressor Training Course 22/11/2012 Customer Training Casing-Diaphragms: bundle Labyrinth seals Diffuser Return channel Blades Impeller
  • 42. 42 Centrifugal Compressor Training Course 22/11/2012 Customer Training Casing-Diaphragms: bundle Suction volute Discharge volute In new barrel compressors the inlet and disharge volutes are separated from the inermediate diaphragms.
  • 43. 43 Centrifugal Compressor Training Course 22/11/2012 Customer Training Casing-Diaphragms: bundle The upper half of the bundle is lowered on the lower half.
  • 44. 44 Centrifugal Compressor Training Course 22/11/2012 Customer Training Horizontally split The diaphragms are installed in the casing without a countercasing
  • 45. 45 Centrifugal Compressor Training Course 22/11/2012 Customer Training Flanges and nozzles Discharge Sideflow Suction Discharge Suction
  • 46. 46 Centrifugal Compressor Training Course 22/11/2012 Customer Training Flanges and nozzles In the barrel type for high or very high pressure, piping is directly connected to the casing without nozzles;
  • 47. 47 Centrifugal Compressor Training Course 22/11/2012 Customer Training Shear and Shim rings Shear ring Shim ring Locking system using shear and shim rings
  • 48. 48 Centrifugal Compressor Training Course 22/11/2012 Customer Training Head cover The functions of the head cover are:  Close the bundle inside the casing;  Guide the flow;
  • 49. 49 Centrifugal Compressor Training Course 22/11/2012 Customer Training Bearings Thrust bearing  Direct Lubricated: lube oil is provided for each pad through a groove manufactured on the pads  Flooded: Oil fills the bearing assembly and drains from the top through a flow control orifice Tilting pads type are adopted. The function of the thrust bearing is to compensate part of the axial thrust.
  • 50. 50 Centrifugal Compressor Training Course 22/11/2012 Customer Training Thrust Bearings Components Thrust bearing are self equalizing: the bearing distributes the load equally between all pads. Thrust shoes Base ring Leveling plates Thrust collar Pivot
  • 51. 51 Centrifugal Compressor Training Course 22/11/2012 Customer Training Journal Bearing Jourbal bearing Tilting pads type are adopted. The functions of the journal bearing are:  Support the rotor weight  Create a lifting effect  Damping effect Two types of possible lubrication:  Direct lubrication: Lube oil is provided for each pad through a groove manufactured on the pads  Flooded lubrication: The oil enter from an orifice in the upper part of the bearing and exits in the lower part after the lubriction of pads.
  • 52. 52 Centrifugal Compressor Training Course 22/11/2012 Customer Training Journal Bearing Bearings pad Bearings casing Pivot
  • 53. Centrifugal Compressor Gas Path GE Oil & Gas Oil & Gas Industry Applications
  • 54. 54 Centrifugal Compressor Training Course 22/11/2012 Customer Training SUCTION DISCHARGE Gas Path
  • 55. 55 Centrifugal Compressor Training Course 22/11/2012 Customer Training Shaft Inlet Volute Fin Casing Blade Impeller Suction Nozzle Suction Pipe Suction The gas flow is directed towards the eye of the first impeller.
  • 56. 56 Centrifugal Compressor Training Course 22/11/2012 Customer Training Suction
  • 57. 57 Centrifugal Compressor Training Course 22/11/2012 Customer Training Labyrinth Seal Suction diaphragm Labyrinth Seal Shaft Key Disk Suction
  • 58. 58 Centrifugal Compressor Training Course 22/11/2012 Customer Training Intermediate stages
  • 59. 59 Centrifugal Compressor Training Course 22/11/2012 Customer Training Single stage Labirinth seals Diffuser Return channel Blades
  • 60. 60 Centrifugal Compressor Training Course 22/11/2012 Customer Training C3=C1 optimal condition Gas Inlet Increased velocity P4,C4 P1,C1 P2,C2 P3,C3 + + + ++ + Single stage
  • 61. 61 Centrifugal Compressor Training Course 22/11/2012 Customer Training Single stage Impeller Inlet Blade Inlet Diffuser Inlet Diffuser Outlet Velocity Pressure Energy 1 2 3 4 1 2 3 4
  • 62. 62 Centrifugal Compressor Training Course 22/11/2012 Customer Training Last impeller Discharge volute Discharge
  • 63. Centrifugal Compressor Axial Thrust GE Oil & Gas Oil & Gas Industry Applications
  • 64. 64 Centrifugal Compressor Training Course 22/11/2012 Customer Training Axial Thrust Axial thrust P2 > P1 P2 P2 P1
  • 65. 65 Centrifugal Compressor Training Course 22/11/2012 Customer Training Axial Thrust Balancing Drum The BALANCE DRUM is a disk installed after the last impeller in order to balance part of the axial thrust (80÷85%).
  • 66. 66 Centrifugal Compressor Training Course 22/11/2012 Customer Training Axial Thrust P2 P1 P2 Ps R1 R2 Rd Axial Force Drum Force
  • 67. 67 Centrifugal Compressor Training Course 22/11/2012 Customer Training Axial Thrust Balancing Line Ps Pd Ps+ΔP Ps= Suction Pressure Ps = Discharge Pressure ΔP= Pressure Drop on balancing line Axial Force Drum Force
  • 68. 68 Centrifugal Compressor Training Course 22/11/2012 Customer Training Balancing line
  • 69. Centrifugal Compressor Performance Curves GE Oil & Gas Oil & Gas Industry Applications
  • 70. 70 Centrifugal Compressor Training Course 22/11/2012 Customer Training Performance Curves  Polytropic Head  Polytropic Efficiency  Pressure Ratio  Power  Discharge Temperature  Discharge Pressure Performance curves describe the relation of the centrifugal compressor operating parameter and the inlet capacity. The performance curves are valid ONLY for the condition specified in the performance diaghram... Qinlet
  • 71. 71 Centrifugal Compressor Training Course 22/11/2012 Customer Training Operating Range Maximum continuous speed (MCS) Minimum operating speed (MOS) Discharge pressure (bar a) Normal operating point Qinlet Choking Area Surge Limit Line
  • 72. 72 Centrifugal Compressor Training Course 22/11/2012 Customer Training Operating point Plant resistance curve Operating point  The plot represents the envelope of all the possible operating conditions relevant to the given suction parameter.  The actual operating point is unique and it is always the intersection between the compressor curve at the given speed and the plant resistance curve. Qinlet
  • 73. 73 Centrifugal Compressor Training Course 22/11/2012 Customer Training
  • 74. 74 Centrifugal Compressor Training Course 22/11/2012 Customer Training Off-design conditions Discharge pressure MW MW Qinlet Ts Ts Ps Ps
  • 75. 75 Centrifugal Compressor Training Course 22/11/2012 Customer Training Other map variation cause: Normal working graph Internal recycles effect Discharge pressure Qinlet
  • 76. 76 Centrifugal Compressor Training Course 22/11/2012 Customer Training According to API 617 the following regulating methods are defined:  Speed Variation  Suction throttling  Variable inlet guide vanes (VIGV)  Discharge blowoff  Cooled bypass Regulation
  • 77. 77 Centrifugal Compressor Training Course 22/11/2012 Customer Training Discharge pressure Regulation Qinlet
  • 78. 78 Centrifugal Compressor Training Course 22/11/2012 Customer Training Discharge pressure Regulation Qinlet
  • 79. Choke, Stall, Surge and Anti-surge Control System GE Oil & Gas Oil & Gas Industry Applications
  • 80. 80 Centrifugal Compressor Training Course 22/11/2012 Customer Training Choking Choking Area Choke rapresents the right limit of performance curve. Rapid decrease in performances and efficiency. Discharge pressure Qinlet
  • 81. 81 Centrifugal Compressor Training Course 22/11/2012 Customer Training Surge  Surge is the left limit of performance curve, on the left of this line the compressor operates in unstable condition;  Represents the maximum polytropic head of the curve;  All surge points, defined for different speeds represent the Surge Limit Line; Surge Limit Line Discharge pressure Qinlet
  • 82. 82 Centrifugal Compressor Training Course 22/11/2012 Customer Training Surge P2 P1 P2 > P1 Flow inside the impeller Axial thrust Normal operating conditions
  • 83. 83 Centrifugal Compressor Training Course 22/11/2012 Customer Training Surge P2 P1 Flow inside the impeller Axial thrust P1 > P2 Surge condition
  • 84. 84 Centrifugal Compressor Training Course 22/11/2012 Customer Training Factors leading to surge During NORMAL OPERATION:  High discharge pressure (Increase of plant resistance);  Reduction of suction pressure;  Increase of suction temperature.
  • 85. 85 Centrifugal Compressor Training Course 22/11/2012 Customer Training The Antisurge System is composed by:  Antisurge Valve  Instrumentation:  Flow indicator trasmitter  Pressure indicator trasmitter  Electronic controller Antisurge system
  • 86. 86 Centrifugal Compressor Training Course 22/11/2012 Customer Training Antisurge system PRESSURE TRANSMITTER ANTISURGE VALVE COMPRESSOR FT PT PT ANTISURGE CONTROL FLOW TRANSMITTER PRESSURE TRANSMITTER The opening of the Antisurge Valve increases the suction flow moving the operating point along the speed. The purpose of the Antisurge Control System is to avoid that the operating point reaches the SLL.
  • 87. 87 Centrifugal Compressor Training Course 22/11/2012 Customer Training …just a clarification: The systems work together but are separately. Antisurge system The anti-surge controller is a special electronic device that interacts with the main control panel but is not depending from it.
  • 88. Lube Oil System GE Oil & Gas Oil & Gas Industry Applications
  • 89. 89 Centrifugal Compressor Training Course 22/11/2012 Customer Training Lube Oil System The function of the lube oil system is to provide the right amount of lube oil to bearings with the desired viscosity by regulating pressure and temperature.
  • 90. 90 Centrifugal Compressor Training Course 22/11/2012 Customer Training Lube Oil System P&ID Tank
  • 91. 91 Centrifugal Compressor Training Course 22/11/2012 Customer Training Lube Oil System P&ID Main pump Auxiliary pump Emergency pump
  • 92. 92 Centrifugal Compressor Training Course 22/11/2012 Customer Training Lube Oil System P&ID PCV
  • 93. 93 Centrifugal Compressor Training Course 22/11/2012 Customer Training Lube Oil System P&ID TCV
  • 94. 94 Centrifugal Compressor Training Course 22/11/2012 Customer Training Lube Oil System P&ID Filters
  • 95. Dry Gas Seals System GE Oil & Gas Oil & Gas Industry Applications
  • 96. 96 Centrifugal Compressor Training Course 22/11/2012 Customer Training Sealing systems The function of the sealing system is to avoid gas leakages Statoric part Rotating part Gap  Gas property is to occupy all the available volume  Gas moves from high pressure sections to low pressure ones
  • 97. 97 Centrifugal Compressor Training Course 22/11/2012 Customer Training Sealing systems The function of the sealing system is to avoid two types of leakage Process gas leakages between the compression stages Process gas leakages towards the atmosphere
  • 98. 98 Centrifugal Compressor Training Course 22/11/2012 Customer Training Types of seals:  Fluid dynamic seals  Labyrinth seals  O-Ring gaskets
  • 99. 99 Centrifugal Compressor Training Course 22/11/2012 Customer Training Labyrinth Seals Plain Stepped Abradable A labyrinth seal is a type of mechanical seal that minimize the gas leakages. Labyrinth seals on rotating shafts provide non-contact sealing action by controlling the passage of fluid through a series of teeth. Efficiency Main purpose is to minimize internal leakages close to the impellers due to different pressure value at inlet and discharge.  Eye of the impeller  Foot of the impeller  Balance drum
  • 100. 100 Centrifugal Compressor Training Course 22/11/2012 Customer Training Balancing Line Shaft End Seal Shaft End Seal Balancing Drum Shaft end sealing
  • 101. 101 Centrifugal Compressor Training Course 22/11/2012 Customer Training Dry gas seal system Mechanical dry gas seal are supplied as cartridges.
  • 102. 102 Centrifugal Compressor Training Course 22/11/2012 Customer Training DGS: main components Stationary ring Rotating ring Spring Seal gas SHAFT Process side Athmosphere side
  • 103. 103 Centrifugal Compressor Training Course 22/11/2012 Customer Training Operating conditions Static Pressure + Spring Thrust Dynamic Pressurization Process Side Stationary ring Rotating ring Seal gas Seal gas The pressure profile at the interface is self adjuxting to restore to a position of equilibrium  Gas enters the groove moving towards the center;  Gas is compressed and pressure increases setting the gap between the rings.
  • 104. 104 Centrifugal Compressor Training Course 22/11/2012 Customer Training Shaft rotation Shaft rotation Dry gas seal
  • 105. 105 Centrifugal Compressor Training Course 22/11/2012 Customer Training Gas source
  • 106. 106 Centrifugal Compressor Training Course 22/11/2012 Customer Training Intermediate Labyrinth Product side Outboard seal Inboard seal Seal gas STREAM 1 Primary vent (leakage from inbord seal + intermediate buffer gas - to flare) STREAM 2 Intermediate buffer gas (N2) STREAM 3 Secondary vent (leakage from Outbord seal + separation gas - atmospheric) STREAM 4 Separation gas (N2) STREAM 5 Atmosphere (Bearing chamber) Separation seal Inner seals Carbon rings Face Seat Seat Face Nomenclature TANDEM type:
  • 107. 107 Centrifugal Compressor Training Course 22/11/2012 Customer Training Process gas side Bearings side Buffer-Process gas supply Seal gas supply N2 Seal gas leakage Separation gas N2 Inner seal Inboard seal Outboard seal Separation seal Dry gas seal: DOUBLE type
  • 108. 108 Centrifugal Compressor Training Course 22/11/2012 Customer Training Tertiary seal The function of the tertiary seal is to avoid the oil vapours entering into the dry gas seal.
  • 109. 109 Centrifugal Compressor Training Course 22/11/2012 Customer Training Dry Gas Seal System P&ID Seal Gas Filters Buffer Gas Filters
  • 110. 110 Centrifugal Compressor Training Course 22/11/2012 Customer Training Dry Gas Seal System P&ID Buffer Gas PCV Seal Gas PCV
  • 111. 111 Centrifugal Compressor Training Course 22/11/2012 Customer Training Dry Gas Seal System P&ID Primary Vent
  • 112. 112 Centrifugal Compressor Training Course 22/11/2012 Customer Training Dry Gas Seal System P&ID Secondary Vent
  • 113. 113 Centrifugal Compressor Training Course 22/11/2012 Customer Training Dry Gas Seal System P&ID Seal Gas Heater
  • 114. Vibrations Overview GE Oil & Gas Oil & Gas Industry Applications
  • 115. 115 Centrifugal Compressor Training Course 22/11/2012 Customer Training The measure of the mechanical behavior of a compressor is given by the amplitude and frequency of the rotor vibrations. The rotor vibration amplitude must not cause:  Contact between rotating and stator parts;  Dry gas seals overloading;  Fatigue in the bearings. Mechanical behavior
  • 116. 116 Centrifugal Compressor Training Course 22/11/2012 Customer Training The typical vibrations of the centrifugal compressors can be classified with reference to the frequency and the nature of the force causing vibrations. According to the first classification (frequency) the vibration may be:  Synchronous The vibration frequency corresponds to the machine rotation speed (ωR)  Asynchronous The vibration frequency is different from the machine rotation speed (ω R) Vibrations classification
  • 117. 117 Centrifugal Compressor Training Course 22/11/2012 Customer Training Syncronous vibrations 𝜔 = 𝜔𝑅 The most common causes are:  Unbalance in the rotor system;  Rotor and stator parts contact;  Fouling deposit.
  • 118. 118 Centrifugal Compressor Training Course 22/11/2012 Customer Training Asyncronous vibrations It is necessary to do another distinction between frequency of the vibration and machine rotational speed  Frequency of the vibration multiple of ωR  Frequency of the vibration lower or higher than ωR 𝜔 = 𝐾𝜔𝑅
  • 119. 119 Centrifugal Compressor Training Course 22/11/2012 Customer Training Asyncronous vibrations Frequency of the vibration multiple of ωR 𝜔 = 𝐾𝜔𝑅 The most common causes are:  Coupling misalignment;  Loose of interference in some rotor components. 𝜔 = 2𝜔𝑅
  • 120. 120 Centrifugal Compressor Training Course 22/11/2012 Customer Training Asyncronous Vibrations Frequency of the vibration lower or higher than ωR The most common causes are:  High clearance in journal bearings  Oil whip;  Aerodynamic effects (rotating stall in diffusers)  Cross - coupling 𝜔 = 0.5 𝜔𝑅 𝜔 = ( 0.4 − 0.5 ) 𝜔𝑅 𝜔 = ( 0.1 − 0.2 ) 𝜔𝑅 𝜔 = 0.2 𝜔𝑅
  • 121. 121 Centrifugal Compressor Training Course 22/11/2012 Customer Training What are the problems? The main problem that we have to consider when a rotor-bearing system is subjected to a periodic force is the phenomenon of RESONANCE.  A system is in resonance when vibration amplitude becomes maximum;  This occurs when the frequency of a periodic force (excitation frequency), applied to a rotor- bearing system, corresponds to a natural frequency of that system. A centrifugal compressor has many natural frequencies that are colled Critical Speeds;The most important are the first and the second; It is necessary to determine the field operation speeds that avoid the resonance.
  • 122. 122 Centrifugal Compressor Training Course 22/11/2012 Customer Training NC1 = Rotor first critical, center frequency, cycles per minute Ncn = Critical speed, n th Nmc = Maximum continuous speed, 105 percent N1 = Initial (lower) speed at 0,707 x peak amplitude (critical) N2 = Final (higher) speed at 0,707 x peak amplitude (critical) SM = Separation margin API 617 𝑁1 𝑁2 𝑁𝑐1 0.707 𝑝𝑒𝑎𝑘 𝑆𝑀 𝑜𝑝𝑒𝑟𝑎𝑡𝑖𝑛𝑔 𝑠𝑝𝑒𝑒𝑑𝑠 𝑁𝑐𝑛 𝑁𝑚𝑐 𝑉𝑖𝑏𝑟𝑎𝑡𝑖𝑜𝑛 𝑙𝑒𝑣𝑒𝑙 𝐴𝐹 = 𝑁𝑐𝑖 𝑁2 − 𝑁1 𝑆𝑀
  • 123. 123 Centrifugal Compressor Training Course 22/11/2012 Customer Training