AHM SHISHIR ATHLE Blowers and Compressors.pdf

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    Sudnya Industrial Services Pvt.Ltd., Pune

    Energy Conservation in Fans,Blowers and Compressors

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    Vacuum Pump, Fan, Blower or

    Compressor?

    How can we distinguish between thesemachines?

    Vacuum Pump:Draws gases/ vapours from a system to make itspressure lower than its surroundings

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    Moves gases/ vapours such that the difference in totalpressure is a few hundred mm WG

    Blower:When the ∆∆∆∆P is > few hundred mm WG but < 2 kg f /cm 2

    Compressor:When the ∆∆∆∆P is > 2 kg f /cm 2

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    Types of Fans and BlowersCentrifugal

    Forward Curved BladesBackward Curved BladesRadial Blades

    Aerofoil Blades

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    Tube Axial

    Vane AxialPropeller

    Lobe Type (Roots Blowers)Single-StageMulti-Stage

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    Fan (& Pump) Equation

    Rotation

    u2

    Volute (Discharge)

    2 n H

    d Q nQ

    ∝∝∝∝

    ∝∝∝∝

    ∝∝∝∝

    u H uQ

    ∝∝∝∝

    ∝∝∝∝

    2

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    u1

    Eye (Inlet)

    3

    3

    2

    d P

    n P

    H Q P d H

    ∝∝∝∝

    ∝∝∝∝

    ××××∝∝∝∝

    ∝∝∝∝

    nu ∝∝∝∝

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    System Flow Rate

    35.00

    40.00

    45.00

    50.00

    1460 rpm 1095 rpm 730 rpm No Static Head 10 m Static Head 15 m Static Head

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    0.00

    5.00

    10.00

    15.00

    20.00

    25.00

    .

    0 20 40 60 80 100 120 140

    Flow Rate m3/h

    H e a d m

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    Friction LossesFanning equation forPressure drop inStraight PipesLoss in Fittings

    Values of K are

    c

    2

    p g2

    u

    D

    Lf 4P =∆

    2u⋅

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    tabulated inHandbooks

    Since ∆∆∆∆P ∝∝∝∝ u 2 , therelationship betweenthese quantities is aparabolic curve

    cf

    g2

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    Fan Efficiencies at different

    Speeds

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    Static Head vs Fan Efficiency in

    Variable Speed Control

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    Reading the Curves

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    Flow Control Methods

    Throttling by a valve

    By-passing by a valve

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    Parallel running of Pumps

    Variable speed control of the pump

    On-off control of the pump

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    Throttle Control

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    Throttling Increases Resistance

    in the System

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    By-Passing

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    On-Off Control

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    Variable Speed Control

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    Fans in Parallel

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    Pumps1 and 2

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    Fans in Series

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    Pumps1 and 2

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    Variable Speed Control of Fans

    Pays

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    Consider Variable Speed Control

    when...the fan is a part of the control system. the fan output varies.

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    Power Consumption of a Fan

    η ρ g H QP ***=

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    H Qk P **=when η is constant

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    Relative Power Consumption

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    Energy Consumption of a Fanis the Power multiplied by the Time

    P

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    t

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    Duty Cycle Curve

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    QQQ min50maxm 61

    32

    61

    FlowMedian Q ++=

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    Energy Use Calculated by the

    Median Flow Method

    Qmax = 300 l/sQ50 = 250 l/sQmin = 81 l/s

    (= Energy Consumption in Variable Speed Control)

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    l/s204l/s636m

    =++=

    and the equivalent power is 42 kW.

    The total energy isW = 42 kW*5000 h = 210 MWh

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    Reading the Power Consumed

    by a Fan

    Duty point of a fan:

    Nominalx Throttle controlx Variable speed control

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    Power consumption ofthe fan in variable speedcontrol

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    Segmented Duty Cycle

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    Comparison based on Energy

    ConsumptionTime Flow Throttle

    ControlVariable Speed

    Control

    1480 rpm

    % h % l/s kW MWh rpm kW MWh

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    40 2000 90 270 75 150 1400 64 128

    30 1500 62 186 71 107 1180 35 53

    30 1500 32 96 65 98 920 24 36

    Compared to throttle control variable speed controlsaves energy 355 - 217 MWh = 138 MWh

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    Variable Speed Control Saves

    Energy

    Cost saving =

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    saved energy*energy price137 MWh * Rs.3700/MWh = Rs. 5.07 lakhs/year

    For Variable Speed AC Drives

    the Payback Period would beless than Two Years

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    Types of CompressorsPositive Displacement

    ReciprocatingLobe typeScrewScroll

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    KinematicCentrifugal

    Axial Flow

    LubricatedNon-Lubricated

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    Screw Compressor

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    Volumetric Efficiency Volumetric Efficiency is the ratio of Volume of Gas delivered to the displacedvolume

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    Power Drawn dp

    p dW Power

    P

    P∫ ∫ ∆

    ==2

    1 ρ k pV n =

    −⋅⋅⋅⋅=

    11

    1

    1

    21

    0

    0

    γ

    γ

    γ

    η p p

    T q

    T p

    K Power A

    Adiabatic Compression

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    Isothermal Compression

    ⋅=

    1

    20

    0

    1 ln p p

    qT RT

    K Power Aη

    −<

    =

    11

    ln

    1

    1

    2

    2

    γ

    γ

    γ

    p p

    p p

    X For n > 1 and p 2 > p1

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    K A

    K A = 0.004363 0.001 98066.5

    p 0 , p 1 , p 2 lb f /in 2 Pa = N/m 2 kg f /cm 2

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    T1 , T 2 °R °K °K

    q 0 ft 3 / min m 3 /secm 3 /sec

    P h. p. kW kW

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    Factors affecting Energy UseTackle each of the factors in the equation

    Factor Units Change by Energy usechanged by

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    p 2 /p 1 kg f /cm 2 1 6 – 10%T1 °K 4 1%

    q 0 m 3 /sec 1% 1%

    X °K 5 2.1%

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    Measures: Compression RatioClean filters regularlyReduce Process Operating PressureConsider two sets of numbers

    1,2,4,8: AM = 3.75 GM = 2.821,3,9,27,81: AM = 24.2 GM = 9

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    s suggests t at a ser es o compressors av ngCompression ratios < p 2 /p 1 of one largecompressor will have a lower energy usageHence, multi-stage compression

    Implicit assumption: each stage startscompression at the same temperatureCompression Ratios for each stage are equal

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    MeasuresCool intake from outside compressor room

    Reduce leakagesMaintain compressor

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    ModulationBlow off

    By-passi.e. re-circulate from exhaust to suction “Unload” individual cylinders

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    Inlet Guide Vane Control for CentrifugalCompressorsBlade angle control for Axial flow

    Compressors Variable Speed Drives

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    Reduce VolumeReduce Leakages

    Reduce UsageFlow nozzles

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    TestingCapacity

    Time to pump up the pressure of a receiver of known

    volume to a given pressureUse of flow nozzles

    Leakages

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    Close all valves at the points of usePump up the receiver to a desired pressureNote the time/s taken for the pressure to drop to a lowerpressure/s

    U L

    L

    T T T LeakRate+

    =

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    Drying and FiltrationFilter air only if the application demands it

    DryersRefrigerant DryersLimitation on the Dew Point temperatures that can

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    Dessicant DryingPurge dryer using compressed air

    Highest operating costs though capital costs are lowWaste a lot of compressed air

    Heat of Compression DryersMost expensive, but most efficient

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    GeneralReceiver

    Volume: about 1 min. generation capacityLocate near large loads

    Install drains and traps at intervals

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    Avoid misuseUse only where necessaryCheck periodically for leakages

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    Contact Us

    Sudnya Industrial Services Pvt. Ltd.5 Raj Apartments,28 Pushpak, Park, Aundh,

    27-Feb-14 Sudnya Industrial Services Pvt. Ltd., Pune 43

    Pune – 411 007Tel: +91 20 3291 2316

    Mobile: +91 98224 07214E-mail: [email protected]