2a compressor fundamentals

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Compressor Fundamentals

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  • 1 2007 Dresser-Rand

    Centrifugal Centrifugal CompressorsCompressors

  • 2 2007 Dresser-Rand

    TopicsTopics

    Centrifugal Compressor Model

    How a Centrifugal works / Energy Conversion

    Basic Construction

    Centrifugal Flow Paths

  • 3 2007 Dresser-Rand

    Basic PrinciplesBasic Principles

    Centrifugal Action

    A Centrifugal Stage

    Energy Conversion

  • 4 2007 Dresser-Rand

    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

  • 5 2007 Dresser-Rand

    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

  • 6 2007 Dresser-Rand

    Centrifugal ActionCentrifugal Action

    EYE OF THEIMPELLERLow Velocity, Low Pressure Gas Inlet

    TIP OF THE IMPELLERHigh Velocity, Higher Pressure Gas Outlet

    Cover Blades Disk

  • 7 2007 Dresser-Rand

    Centrifugal Action Diffusion PassageCentrifugal Action Diffusion Passage

    P1 P1

    P2P2

    Diffusion Passage

    Impeller Impeller

    Diffusion Passage

    Shaft

  • 8 2007 Dresser-Rand

    V1 V1

    V2V2 V1

    V1Diffusion Passage

    Impeller Impeller

    Diffusion Passage

    Shaft

    Diffusion Passage Velocity ChangesDiffusion Passage Velocity Changes

  • 9 2007 Dresser-Rand

    Pressure, Volume and TemperaturePressure, Volume and Temperature

    1 ft.

    1 ft.1 ft.

    Gas = 1 ft.3

  • 10

    2007 Dresser-Rand

    Temperature and Molecule Energy Temperature and Molecule Energy LevelLevel

    Greater Temperature = Greater Energy = Higher Pressure

  • 11

    2007 Dresser-Rand

    Add Heat

    1 ft.

    1 ft.1 ft.

    Gas = 1 ft.3

    Pressure, Volume and TemperaturePressure, Volume and Temperature

  • 12

    2007 Dresser-Rand

    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

  • 13

    2007 Dresser-Rand

    Centrifugal Compressor StageCentrifugal Compressor Stage

  • 14

    2007 Dresser-Rand

    Energy ConversionEnergy Conversion

    P4,V4,T4

    P2,V4,T2

    P3,V1,T3

    P3,V1,T3

    P5,V1,T5

    P1,V1,T1

    P5,V1,T5

  • 15

    2007 Dresser-Rand

    Basic ConstructionBasic Construction

    Compressor Types

    Basic Principles - Fundamentals

  • 16

    2007 Dresser-Rand

    1. Pipeline Radial InletMulti-stage

    4. Pipeline BoosterAxial InletSingle-stage

    2. Radially Split Multi-stage

    3. Axially SplitFabricated Case

    Types of CentrifugalsTypes of Centrifugals

  • 17

    2007 Dresser-Rand

    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

  • 18

    2007 Dresser-Rand

    Sizes of CentrifugalsSizes of Centrifugals

    Large VolumeLower PressureLower RPM

    Smaller VolumeHigher PressureHigher RPM

  • 19

    2007 Dresser-Rand 2000 by Dresser-Rand

    Designation of centrifugal Designation of centrifugal compressorscompressors

  • 20

    2007 Dresser-Rand 2000 by Dresser-Rand

    Designation of centrifugal Designation of centrifugal compressorscompressors

  • 21

    2007 Dresser-Rand 2000 by Dresser-Rand

    Designation of centrifugal Designation of centrifugal compressorscompressors

  • 22

    2007 Dresser-Rand 2000 by Dresser-Rand

    Designation of centrifugal Designation of centrifugal compressorscompressors

  • 23

    2007 Dresser-Rand 2000 by Dresser-Rand

    Application ParametersApplication Parameters

  • 24

    2007 Dresser-Rand

    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

  • 25

    2007 Dresser-Rand

    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

  • 26

    2007 Dresser-Rand

    Sizes of CentrifugalsSizes of Centrifugals

  • 27

    2007 Dresser-Rand

    D26

    D4

    Sizes of CentrifugalsSizes of Centrifugals

  • 28

    2007 Dresser-Rand

    Application ParametersApplication Parameters

  • 29

    2007 Dresser-Rand

    Axial Split CasingAxial Split Casing

    Axially Split Fabricated

    Casing

    ForgedEnd Covers,

    Cartridges, orHeads

    2000 by Dresser-Rand

    Operate at relatively low pressures < 850 psig

  • 30

    2007 Dresser-Rand

    Axially Split Compressor on Test

    Axial Split CasingAxial Split Casing

  • 31

    2007 Dresser-Rand

    Radial Split CasingRadial Split Casing

    Radially Split Forged/Fabricated

    Casing

    2000 by Dresser-Rand

    Rotor Assembly

  • 32

    2007 Dresser-Rand

    Radially Split Compressor in Service

    Radial Split CasingRadial Split Casing

  • 33

    2007 Dresser-Rand

    Pipeline Booster CasingPipeline Booster Casing

    DischargeNozzle

    Inlet Nozzle

    Head

    Volute

  • 34

    2007 Dresser-Rand 2000 by Dresser-Rand

    Casing before machiningCasing before machining

  • 35

    2007 Dresser-Rand 2000 by Dresser-Rand

    Nozzles before machiningNozzles before machining

  • 36

    2007 Dresser-Rand 2000 by Dresser-Rand

    Casing with feet and nozzlesCasing with feet and nozzles

  • 37

    2007 Dresser-Rand 2000 by Dresser-Rand

    Casing fixationCasing fixation

  • 38

    2007 Dresser-Rand 2000 by Dresser-Rand

    Compressor head with lifting Compressor head with lifting toolstools

  • 39

    2007 Dresser-Rand

    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

  • 40

    2007 Dresser-Rand

    Shear Rings & OShear Rings & O--RingsRings

  • 41

    2007 Dresser-Rand 2000 by Dresser-Rand

    Head fixationHead fixation

  • 42

    2007 Dresser-Rand 2000 by Dresser-Rand

    Head fixationHead fixation

  • 43

    2007 Dresser-Rand

    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

  • 44

    2007 Dresser-Rand

    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

  • 45

    2007 Dresser-Rand

    Modular Bundle Technology

  • 46

    2007 Dresser-Rand

    Bundle Assembly RollerBundle Assembly Roller

  • 47

    2007 Dresser-Rand

    Bundle Components

    ROTOR

    BEARINGS & SEALS

    HEADS

    RETURN BEND

    DIAPHRAGMS

    VOLUTE

  • 48

    2007 Dresser-Rand

    Modular Bundle Technology

  • 49

    2007 Dresser-Rand

    [email protected]