ข้อสอบสามัญเครื่องกล power plant 1/2547

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    2 (Power Plant / Gas Turbine) 1/2547

    6 5 20 1. 5 MW

    compressor 97 k Pa, 30 0C compressor 2 k Pa compressor 5.5 : 1 isentropic compressor 84 % (transmission efficiency) 98 % turbine 900 0C (C12 H26) 43,100 kJ/kg

    97 % 3 % isentropic turbine 88 % turbine 100 k Pa

    specific fuel consumption thermal efficiency

    (CPa) = 1.005 kJ/kg K , (CPg) = 1.147 kJ/kg K , isentropic index (a) = 1.4 , (g) = 1.33 gas constant ( R ) = 0.287 kJ/kg K

    (20 )

    1

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    c = 84 %

    m = 98 %T03 = 900

    oC = 1,173 KHV = 43,100 kJ/kg

    b = 97 %

    compressor

    adiabatic process stagnationh0a = h01 T0a = T01

    T0a ~ Ta = T01 = 30 + 273 = 303 K

    P1 ~ P 01 P01 = 97 2 = 95 k Pa

    P02 = 5.5 P01 = 5.5 x 95 = 522.5 kPa P03 = P02 0.03 P02 = 0.97 x 522.5

    = 506.8 k Pa

    2

    Wnet = 5 MW

    Pa = 97 kPaTa = 30

    oC

    Pi = P0a - P01 = 2 k Pa

    01

    02

    = 5.5

    Pb = P03 - P02 = 3 % of P02t = 88 %

    P04

    = 100 k Pa

    a = 1.4

    g = 1.33R = 0.287 kJ/kg K Cpa = 1.005 kJ/kg KCpg = 1.147 kJ/kg K

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    compressor

    01

    20

    T

    T

    = a1a

    01

    02

    P

    P

    = 4.1

    14.1

    )5.5(

    = (5.5)0.2857 = 1.6275

    =20T 1.6275 x 303 = 493.1 K

    c = 0.84 =0102

    0120

    TT

    TT

    T02 - T01 = 0.84303493.1

    = 226.4 K

    T02 = 529.4 K

    Turbine

    40

    03

    T

    T

    = g

    g

    1

    )(04

    03

    = 1.33

    11.33

    )100

    506.8(

    = (5.068)0.248

    = 1.4955

    '04T =1.49551,173

    = 784.3 K

    t

    = 0.88 =

    4003

    0403

    TT

    TT

    T03- T04 = 342 K

    T04 = 1,173 342 = 830.97 K

    W = 5 MW = m a )(m

    cW

    tW

    =

    )T(T

    0.98

    1.005-)T1.147(Tm

    01020403a

    =

    (226.4)

    0.98

    1.005-1.147(342)m a

    3

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    = 160.1 am

    am = 31.2 kg / s

    bfHVm = m a Cpg ( T03 T02)

    m f = 0.97x43,100)529.41,173(1.147x31.2

    = 0.763 kg / s

    f = af

    m

    m

    = 31.20.763

    = 0.024 kgf / kg

    Specific fuel consumption (sfc) =Wf

    = 600,3X160.1

    0.024

    = 0.55 kgf / kWh

    Thermal efficieney () =HVfW

    =43,100x0.024

    160.1

    = 15.5 %

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    2. Single stage gas turbine nozzle rotor (designed conditions) ( ) nozzle 700 stagnation pressure temperature 311 k Pa 850 0C static pressure 100 kPa total (stagnation) to static efficiency 87 % mean blade speed =500 m/s

    stage 1. specific work done 2. Mach Number nozzle3. 4. total to total efficiency5. degree of reaction stage

    (CP) isentropic ( ) 1.148 kJ/kgK 1.33

    (20 )

    Ca = 900 km/h = 250 m/s

    F = A)P(P]CCf)[(1m aeaja ++am = = 100 kg/s

    f = = 0.018 kgf /kgCj =

    Ca = = 250 m/sPe = (nozzle)Pa = = 69 kPaA =

    5

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    T04 = 970 K

    T04 = T05 = T5 +gp

    25

    2C

    C1

    Check choking

    2.49

    69

    172

    P

    P

    a

    04 ==

    +

    =

    1g

    g

    )1

    1

    (1-1

    1

    cP

    P

    g

    g

    j

    04

    = 4

    )]2.330.33(

    0.951[1

    1

    Pc j

    c

    04

    P

    P= 1.914

    choked

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    T5 = Tc =

    +12

    g

    T04 = x 970 = 832.6 K

    P5 = Pc = 1.914P04

    = 1.914172 = 89.86 k Pa 1

    25C = (970 832.6) x 2 x 1.147 = 315.2 x 10 3

    C5 = Cj = 561.4 m/s

    5 =5

    5

    TR

    P=

    832.6x0.287

    89.86 = 0.375 kg/m3

    5m = 5 A5 C5 = 0.375 A5 x 561.4 = am ( 1 + f )

    = 100 x 1.018 = 101.8 kg/s A5 = 0.4836 m

    2

    F = 100 [ (1.018) 561.4 250 ] + (89.86 69) 0.4836

    . = 42.24 kN

    . (propulsive efficiency) , p

    p =aC

    C1

    2

    j+ =250

    561.41

    2

    + = 61.62 %

    . (energy conversion efficiency) , e

    e =(HV)m

    /2)C(Cam

    f

    2a

    2j

    = 322

    10x43,930x1.8

    /2](250)[(561.4)100

    . (overall efficiency) , o

    o = 0.6162 x 0.1597 = 9.84 %

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    7

    22.33

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    6. ( Combined Cycle Power Plant ) (Gass Turbine ) ( Steam Turbine) Heat Recovery Steam Generator, HRSG q q q Percentage

    (20 )

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