ข้อสอบสามัญเครื่องกล Power Plant 3/2547

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    6 4

    POWER PLANT 1 - 3 2

    GAS TURBINE 4 - 6 2

    POWER PLANT

    1. Ideal Saturated Rankine Cycle Power Plant

    40 bar (Saturated Temperature 250.3o

    C) Condenser 0.10 bar (Saturated Temperature 45.8

    oC) -

    (25 ) 40 bar hf= 1,087 kJ/kg , h g = 2,801 kJ/kg ,

    sf= 2.797 kJ/kg-K , s g = 6.070 kJ/kg-K

    0.10 bar hf= 191.83 kJ/kg , h g = 2,584.7 kJ/kg ,s

    f= 0.6493 kJ/kg-K , s

    g= 8.1502 kJ/kg-K

    1.1 Rankine Cycle (Qin)1.2 Rankine Cycle (Qout)1.3 Rankine Cycle (Win)1.4 Rankine Cycle (Wnet)1.5 Rankine Cycle

    40 bar hf= 1,087 kJ/kg , h g = 2,801 kJ/kg ,

    sf= 2.797 kJ/kg-K , s g = 6.070 kJ/kg-K

    0.10 bar hf= 191.83 kJ/kg , h g = 2,584.7 kJ/kg ,s

    f= 0.6493 kJ/kg-K , s

    g= 8.1502 kJ/kg-K

    h1 = 191.83 kJ/kg

    h3 = 2,801 kJ/kg

    s3 = 6.070 kJ/kg-K

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    1W2 = -v*(P2 P1) = h1 h2

    = - 0.00101 * (4000 10)

    = - 4.03 kJ/kg

    h2 = h1 + Wp

    = 191.83 + 4.03 kJ/kg

    = 195.86 kJ/kg

    s4 = s3 = 6.070 kJ/kg-K

    x4 = (s4 - 0.6493) / (8.1502 - 0.6493)

    = 0.7227

    h4 = hf + x4 * (hg hf)

    = 191.83 + 0.7227 *(2,584.7 - 191.83)

    = 1921.09 kJ/kg

    Wt = h3 h4

    = 2,801 - 1921.09

    = 879.91 kJ/kg

    1.1 Qin = h3 h2

    = 2,801.4 - 195.86

    = 2605.14 kJ/kg

    1.2 Qout = h4 h1

    = 192109 - 191.83

    = 1729.26 kJ/kg

    1.3 Wp = 1W2 = - 4.03 kJ/kg

    1.4 W = Wt + Wp

    = 879.91 4.03

    = 875.88 kJ/kg

    1.5 Eff = W/Qin

    = 875.88 / 2605.14

    = 33.62 %

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    2. Superheated Rankine Cycle Power Plant (SuperheatedSteam) 30 bar Steam Temperature 300 oC Condenser 0.10 bar (Saturated Temperature 45.8 oC) - (25 )

    30 bar hf= 1,008.42 kJ/kg , h g = 2,804.2 kJ/kg ,

    sf= 2.6457 kJ/kg-K , s g = 6.1869 kJ/kg-K

    300oC h = 2,995 kJ/kg , s = 6.5410 kJ/kg-K

    0.10 bar hf= 191.83 kJ/kg , h g = 2,584.7 kJ/kg ,sf= 0.6493 kJ/kg-K , s g = 8.1502 kJ/kg-K

    2.1 Rankine Cycle (Qin)2.2 Rankine Cycle (Qout)2.3 Rankine Cycle (Win)2.4 Rankine Cycle (Wnet)2.5 Rankine Cycle

    30 bar hf= 1,008.42 kJ/kg , h g = 2,804.2 kJ/kg ,

    sf= 2.6457 kJ/kg-K , s g = 6.1869 kJ/kg-K

    300oC h = 2,995 kJ/kg , s = 6.541 kJ/kg-K

    0.10 bar hf= 191.83 kJ/kg , h g = 2,584.7 kJ/kg ,sf= 0.6493 kJ/kg-K , s g = 8.1502 kJ/kg-K

    h1 = 191.83 kJ/kg

    h3 = 2,995 kJ/kg

    s3 = 6.541 kJ/kg-K

    1W2 = -v*(P2 P1) = h1 h2

    = - 0.00101 * (3,000 10)

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    = - 3.02 kJ/kg

    h2 = h1 + Wp

    = 191.83 + 3.02 kJ/kg

    = 194.85 kJ/kg

    s4 = s3 = 6.541 kJ/kg-K

    x4 = (s4 - 0.6493) / (8.1502 - 0.6493)

    = 0.7855

    h4 = hf + x4 * (hg hf)

    = 191.83 + 0.7855*(2,584.7 - 191.83)

    = 2071.35 kJ/kg

    Wt = h3 h4

    = 2,995 - 2071.35

    = 923.65 kJ/kg

    2.1 Qin = h3 h2

    = 2800.15 kJ/kg

    2.2 Qout = h4 h1

    = 1879.52 kJ/kg

    2.3 Wp = 1W2 = 3.02 kJ/kg

    2.4 W = Wt + Wp

    = 923.65 3.02

    = 920.63 kJ/kg

    2.5 Eff = W/Qin

    = 32.88 %

    3. Carnot Ideal Cycle 2 ReversibleIsothermal Processes Reversible Adiabatic Processes(Isentropic) Ideal Saturated Rankine Cycle

    (25 )

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    CARNOT CYCLE SATURATED RANKINE CYCLE

    1. Condenser() Condenser

    (x1) Entropy Saturated Entropy, sf (P2- BoilerPressure)

    1. Condenser () Condenser

    (Saturated Liquid) Condenser

    2. Pump (x1) Condenser Pump Power

    2. Condenser (Boiler) Pump Power Pump

    GAS TURBINE

    4. (30 ) (25 )1) ......2) 1 specific work................3)

    ............................. ..................... ..................................4) Regenerator .....................................

    5) Reheater ...........................

    6) ...............

    ................................... (//)7) ...............

    ......................................................................................................................................................................

    8) Stagnation temperature ..........................................................................................................

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    9) twin spool ...................................................................10) 1. .................... 2. ..

    3. .. 4.

    11) propelling nozzle ........................................ 12) Propelling nozzle subsonic convergent nozzle

    supersonic ......................................................................................................................................... 13) ................................................................................................ 14) ................................................................15) Power plant Cogeneration ...........................................

    .......................................................................................................................................................................

    T 3 16) 2-5 .

    17) ...............................................................

    18) ...............................................................

    19) Ram compression ...........................................................................................................................................................................................................................................................................

    20) exhaust diffuser.......................................................................................

    2

    45

    2

    S

    1

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    1)

    2) 3) , , 4) 5) 6) , 7) 8)

    9) 2 10) , , 11) 12) Convergent divergent nozzle

    13)

    14) Ft = (Mc.Cjc + Mh.Cjh) - MaCa

    15) Industrial Gas Turbine

    16) Regenerator

    17)

    18)

    19)

    20)

    5. combined cycle gas turbine 4 waste heat boiler gas turbine boiler 4 steam turbine 1 gas turbine 1 60 MW steam turbine 120 MW

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    gas turbine compressor, combustion chamber, turbine generator

    60 MW 300 K, 1.01325 barisentropic efficiency compressor 80 %combustion efficiency 97 %

    isentropic efficiency turbine 86 %transmission efficiency 99 %

    pressure drop combustion chamber 0.04 bar gases turbine 930 0C turbine 1.2 bar, 505 0C 33.5 MJ/m3

    specific fuel consumption gas turbine

    (CPa) = 1.005 kJ/kgK gases (CPg) = 1.147 kJ/kgK isentropic (a) = 1.4 isentropic gases (g) = 1.333

    ( R ) = 0.287 kJ/kgK(25 )

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    6. gas turbine 2 stages high pressure stage gas turbine low-pressure stage gas turbine high pressure stage compressor low-pressure stage (propeller) = 4 : 1 60 kg/s turbine 6500 C compressor = 1.01 bar, 250C isentropic efficiencies compressor, high-pressure low-pressure stage turbines 80%,83% 85% mechanical efficiency 98% combustion chamber

    . turbine 2 stages . Cycle efficiency.

    (CPa CPg) 1.005 1.15kJ/kgK (a g ) 1.4 1.333

    (25 )

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