4150-02-B-E4

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MATAKULIAH : TERMODINAMIKA II MODEL TUGAS/QUIZ : QUIZ- ETS-04 MATERI : SIKLUS RANKINE DG REHEAT AWAL TUGAS : 12 MEI 2015 AKHIR TUGAS : 13 MEI 2015, ,JAM 10.00 PAGI Melalui email : [email protected] NAMA : Much. Shochib Chabibi NBI/KLAS : 421204150-B-Q-ETS-04 email : Perhatikan gambar dibawah ini : Diketahui : P1 = 344 + 50 = 394 Psia P3 = 7000 + 50 = 7050 Psia T3 = 1570 P5 = 2600 + 50 = 2650 Psia T = 1700 P=7000 psia + 2 NBI dan T=1570 F P=2600 psia + 2 NBI dan T=1700 F P=344 psia + 2 NBI Tentukan : Effisiensi siklus tsb

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Transcript of 4150-02-B-E4

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MATAKULIAH : TERMODINAMIKA IIMODEL TUGAS/QUIZ : QUIZ- ETS-04MATERI : SIKLUS RANKINE DG REHEATAWAL TUGAS : 12 MEI 2015AKHIR TUGAS : 13 MEI 2015, ,JAM 10.00 PAGI

Melalui email : [email protected]

NAMA : Much. Shochib ChabibiNBI/KLAS : 421204150-B-Q-ETS-04email :

Perhatikan gambar dibawah ini :

Diketahui :

P1 = 344 + 50 = 394 Psia

P3 = 7000 + 50 = 7050 Psia

T3 = 1570 ℉

P5 = 2600 + 50 = 2650 Psia

T = 1700 ℉

P=7000 psia + 2 NBI dan T=1570 F

P=2600 psia + 2 NBI dan T=1700 F

P=344 psia + 2 NBI

Tentukan : Effisiensi siklus tsb

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Untuk mencari h3 dan s3, dengan menggunakan tabel b2, dengan menginterpelasi 1570 F

dengan P = 7050 psia

P(psia)Temperatur

1500 1570 1600

7000h (Btu/lbm) 1714,4 1783,5

s (Btu/lbm 0R) 1,5751 1,6096

7050h (Btu/lbm) 1713,765 1762,174 1782,97

s (Btu/lbm 0R) 1,57397 1,598246 1,60865

8000h (Btu/lbm) 1701,7 1772,9

s (Btu/lbm 0R) 1,5552 1,5906

h3= 1762,174 s3=1,598246

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P(psia)Entalpi Volume

hf Vf

300 394,1 0,01890394 422,394 0,01931400 424.2 0,01934

hfp1=422,394Btu/lbmVfp1=0,01931ft3/lbm

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P(psia)Entropi

Sf Sfg

2600 0,9237 0,29712650 0,9348 0,2725

3203.8 1,0582 0,0000

Sfp4 = 0,9348 Btu/lbm0R

Sfgp4 = 0,2725 Btu/lbm0R

X4 = S3−S fp4

S fgp 4 =

1,598246−0,93480,2725 = 2,43

Untuk mencari h4, dengan uji coba interpelasi pada P = psia 2650

P(psia)Temperatur1100 1200

2000h (Btu/lbm) 1537,2 1598,6

s (Btu/lbm 0R) 1,6019 1,6400

2650h (Btu/lbm) 1519,52 1584,3

s (Btu/lbm 0R) 1,5640 1,60425

3000h (Btu/lbm) 1510,0 1576,6

s (Btu/lbm 0R) 1.5436 1.5850

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S3 = S4

P = 2650 psia 1200 F 1300 Fh (Btu/lbm) 1519,52 h4 = 1574,64 1584,3s (Btu/lbm 0R) 1,5640 s4 = 1,598246 1,60425

P(psia)Temperatur

1700

2000h (Btu/lbm) 1898.1

s (Btu/lbm 0R) 1.7978

2650h (Btu/lbm) 1891,8

s (Btu/lbm 0R) 1,7663

3000h (Btu/lbm) 1888.4

s (Btu/lbm 0R) 1.7494

h5 =1891.8 Btu/lbm 0R.

S5 =1.7663 Btu/lbm 0R.

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P(psia)Entropi

Sf Sfg

300 0,5885 0,9232394 0,6199 0,8674400 0,6219 0,8639

Sfp6 = 0,6199 Btu/lbm0R

Sfgp6 =0,8674 Btu/lbm0R

X6 = S5−S fp6

S fgp 6 =

1.7663−0,61990,8674 = 1,32

Untuk mencari h6, dengan uji coba interpelasi pada P = 394 psia.

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P(psia)Temperatur1000 1100

300h (Btu/lbm) 1526,4 1579,8

s (Btu/lbm 0R) 1,7966 1,8319

394h (Btu/lbm) 1523,8 1577,5

s (Btu/lbm 0R) 1,7654 1,7823

400h (Btu/lbm) 1523.6 1577.4

s (Btu/lbm 0R) 1.7634 1.7991

S5 = S6

P = 435 psia 1000 F 1100 Fh (Btu/lbm) 1523,8 h6 = 1526,66 1577,5s (Btu/lbm 0R) 1,7654 S6 = 1.7663 1,7823

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h2= h1+V1(P3–P1)

h2= 422,394 + 0,01931 ft3/lbm (7050 – 394) lbf/in2 x 144 in2/ft2 x Btu/778lbf.ft

= 422,394 + 23,79 = 446,184 Btu/lbm

η = W t1+W t 2−W p

QB+QR=

(h3−h4 )+(h5−h6 )−(h2−h1)

(h3−h2 )+(h5−h4)

=(1762,174 –1574,64 )+(1891,8– 1526,66 )−(446,184−422,394)

(1762,174−446,184 )+(1891,8−1574,64 )

η = 187,534+365,14−23,79

1315,99−3 17,16=

528,884998,83

= 0,5295 = 52,95 %