2a compressor fundamentals
DESCRIPTION
Compressor FundamentalsTRANSCRIPT
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Centrifugal Centrifugal CompressorsCompressors
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TopicsTopics
Centrifugal Compressor Model
How a Centrifugal works / Energy Conversion
Basic Construction
Centrifugal Flow Paths
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Basic PrinciplesBasic Principles
Centrifugal Action
A Centrifugal Stage
Energy Conversion
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The Centrifugal EffectThe Centrifugal Effect
MomentumVelocity & Direction
Centripetal Force
Centrifugal Reaction
Any object traveling in a circle is kept in that path by the centripetal force
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Gas Velocity IncreaseGas Velocity Increase
V1
V2
V3
When the impeller rotates, the rotation forces the gas molecules outward the center / impeller eye because the lack of centripetal force
As the gas molecules move outward, they gain velocity
The gas tends to oppose the push of the blades, so the pressure of the gas increases
The impeller adds both velocity and pressure to the gas
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Centrifugal ActionCentrifugal Action
EYE OF THEIMPELLERLow Velocity, Low Pressure Gas Inlet
TIP OF THE IMPELLERHigh Velocity, Higher Pressure Gas Outlet
Cover Blades Disk
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Centrifugal Action Diffusion PassageCentrifugal Action Diffusion Passage
P1 P1
P2P2
Diffusion Passage
Impeller Impeller
Diffusion Passage
Shaft
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V1 V1
V2V2 V1
V1Diffusion Passage
Impeller Impeller
Diffusion Passage
Shaft
Diffusion Passage Velocity ChangesDiffusion Passage Velocity Changes
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Pressure, Volume and TemperaturePressure, Volume and Temperature
1 ft.
1 ft.1 ft.
Gas = 1 ft.3
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Temperature and Molecule Energy Temperature and Molecule Energy LevelLevel
Greater Temperature = Greater Energy = Higher Pressure
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Add Heat
1 ft.
1 ft.1 ft.
Gas = 1 ft.3
Pressure, Volume and TemperaturePressure, Volume and Temperature
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What is a Stage of Compression?What is a Stage of Compression?Centrifugal Stage
Return Bend
Guide Vanes
Return Channel
Return Bend
ImpellerIncreases VelocityIncreases Static Pressure
DiffuserReduces VelocityIncreases Static Pressure
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Centrifugal Compressor StageCentrifugal Compressor Stage
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Energy ConversionEnergy Conversion
P4,V4,T4
P2,V4,T2
P3,V1,T3
P3,V1,T3
P5,V1,T5
P1,V1,T1
P5,V1,T5
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Basic ConstructionBasic Construction
Compressor Types
Basic Principles - Fundamentals
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1. Pipeline Radial InletMulti-stage
4. Pipeline BoosterAxial InletSingle-stage
2. Radially Split Multi-stage
3. Axially SplitFabricated Case
Types of CentrifugalsTypes of Centrifugals
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Gases - All types of gases Speed - 3,500 to 26,500 RPM Pressure - Vacuum to 10,500 PSI Flow range - 800 to 520,000 ACFM Number of stages - 1 to 10 impellers Head - 3,000 to 15,000 ft/lb/lb per stage
2000 by Dresser-Rand
Application parametersApplication parameters
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Sizes of CentrifugalsSizes of Centrifugals
Large VolumeLower PressureLower RPM
Smaller VolumeHigher PressureHigher RPM
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Designation of centrifugal Designation of centrifugal compressorscompressors
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Designation of centrifugal Designation of centrifugal compressorscompressors
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Designation of centrifugal Designation of centrifugal compressorscompressors
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Designation of centrifugal Designation of centrifugal compressorscompressors
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Application ParametersApplication Parameters
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Model ExplanationModel Explanation
D12R5SD DATUM Centrifugal Compressor
12 Frame Size Based on case insidediameter (from 2 to 28)
R Radial or Vertical Split Casing
5 Actual Number of Impellers
B/C/S Back to Back Configuration
Compound
Straight Through
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Model ExplanationModel Explanation
D14R8-6CD DATUM Centrifugal Compressor
8 Frame Size Based on case insidediameter (from 2 to 28)
R Radial or Vertical Split Casing
10 Actual Number of Impellers
B/C/S Back to Back Configuration
Compound
Straight Through
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Sizes of CentrifugalsSizes of Centrifugals
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D26
D4
Sizes of CentrifugalsSizes of Centrifugals
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Application ParametersApplication Parameters
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Axial Split CasingAxial Split Casing
Axially Split Fabricated
Casing
ForgedEnd Covers,
Cartridges, orHeads
2000 by Dresser-Rand
Operate at relatively low pressures < 850 psig
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Axially Split Compressor on Test
Axial Split CasingAxial Split Casing
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Radial Split CasingRadial Split Casing
Radially Split Forged/Fabricated
Casing
2000 by Dresser-Rand
Rotor Assembly
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Radially Split Compressor in Service
Radial Split CasingRadial Split Casing
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Pipeline Booster CasingPipeline Booster Casing
DischargeNozzle
Inlet Nozzle
Head
Volute
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Casing before machiningCasing before machining
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Nozzles before machiningNozzles before machining
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Casing with feet and nozzlesCasing with feet and nozzles
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Casing fixationCasing fixation
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Compressor head with lifting Compressor head with lifting toolstools
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Radially Split with Shear Ring HeadsRadially Split with Shear Ring Heads
Shear Ring
O-Rings
Retaining Ring
It offers the benefits of greater strength and faster disassembly than bolted design
Proper assembly is assured by elimination of the precise torque requirements of bolted head requirements
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Shear Rings & OShear Rings & O--RingsRings
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Head fixationHead fixation
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Head fixationHead fixation
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Nameplate DataNameplate DataModel: D14R8-6C
Serial No: DF5115
Max Allowable Working Pressure: 175 barg
Min / Max Temp: 0C / 150C
Min / MCOS: 5715/ 8980 RPM
Trip Speed: 9429 RPM
NC1: 3800 - 4250
NC2: 15800 - 16050
Max Sealing / Settleout Pressure: 70.5 / 138 barg
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Nameplate DataNameplate DataModel: D8R10B
Serial No: CT32293A01/B01
Max Allowable Working Pressure: 175 barg
Min / Max Temp: -29C / 193C
Min / MCOS: 5903 / 8855 RPM
Trip Speed: 9298 RPM
NC1: 3500
NC2: 14500 - 16000
Max Sealing / Settleout Pressure: 89 barg
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Modular Bundle Technology
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Bundle Assembly RollerBundle Assembly Roller
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Bundle Components
ROTOR
BEARINGS & SEALS
HEADS
RETURN BEND
DIAPHRAGMS
VOLUTE
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Modular Bundle Technology
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