Q2/ Air flows isentropically in a converging-diverging nozzle with initial Ma = 0.2, pressure = 1 MPa and temperature 27 C. Find the exit temperature, pressure and velocity at Ma = 1.8

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Q2/ Air flows isentropically in a converging-diverging nozzle with initial Ma = 0.2, pressure = 1 MPa and temperature 27 C. Find the exit temperature, pressure and velocity at Ma = 1.8
LUA
TABLE A-32
One-dimensional isentropic compressible-flow functions for an ideal
100 gas with k = 1.4
to Ma
Ma*
A/A*
PIPO
pl po
TITO
0
0
00
1.0000
1.0000
1.0000
0.1
0.1094
5.8218
0.9930
0.9950
0.9980
0.2
0.2182
2.9635
0.9725
0.9803
0.9921
0.3 0.3257
2.0351
0.9395
0.9564
0.9823
0.4
0.4313
1.5901
0.8956
0.9243
0.9690
0.5
0.5345
1.3398
0.8430
0.8852
0.9524
0.6 0.6348
1.1882 0.7840
0.8405
0.9328
0.7
0.7318
1.0944 0.7209
0.7916
0.9107
1.0382 0.6560 0.7400
0.8865
0.8 0.8251
0.9 0.9146
1.0089 0.5913 0.6870
0.8606
1.0
1.0000
1.0000
0.5283
0.6339
0.8333S 3
1.2
1.1583
1.0304
0.4124
0.5311
0.7764
1.4
1.2999
1.1149
0.3142
0.4374
0.7184
1.6 1.4254
1.2502
0.2353 0.3557
0.6614
1.8
1.5360
1.4390
0.1740
0.2868
0.6068
2.0
1.6330
1.6875
0.1278
0.2300
0.5556
2.2
1.7179
2.0050 0.0935 0.1841
0.5081
2.4
1.7922
2.4031
0.0684 0.1472
0.4647
TABLE A-1
Molar mass, gas constant, and ideal-gas specfic heats of some substances
VOL NAN
Gas Constant
Molar Mass
M, kg/kmol
Substance
R, kJ/kg. K*
Air
28.97
0.2870
17.03
0.4882
39.95
0.2081
Ammonia, NH3
Argon, Ar
Bromine, Br₂
Isobutane, C4H10
159.31
0.05202
58.12
0.1430
n-Butane, C4H10
58.12
0.1430
Carbon dioxide, CO₂
44.01
0.1889
Carbon monoxide, CO
28.01
0.2968
Chlorine, Cl₂
70.905
0.1173
86.47
0.09615
Chlorodifluoromethane (R-22), CHCIF2
Ethane, C₂H6
30.070
0.2765
lewoll A \Sp
S siune cumst one c4M
olsy
Specific Heat Data at 25°C
CkJ/kg. K
0.7180
1.605
0.3122
0.1732
1.520
1.551
0.6550
0.7417
0.3608
0.5535
1.468
Cp. kJ/kg. K
1.005
2.093
0.5203
0.2253
1.663
1.694
0.8439
1.039
0.4781
0.6496
1.744
K= C₂/Cv
1.400
1.304
1.667
1.300
1.094
1.092
1.288
1.400
1.325
1.174
1.188
Transcribed Image Text:LUA TABLE A-32 One-dimensional isentropic compressible-flow functions for an ideal 100 gas with k = 1.4 to Ma Ma* A/A* PIPO pl po TITO 0 0 00 1.0000 1.0000 1.0000 0.1 0.1094 5.8218 0.9930 0.9950 0.9980 0.2 0.2182 2.9635 0.9725 0.9803 0.9921 0.3 0.3257 2.0351 0.9395 0.9564 0.9823 0.4 0.4313 1.5901 0.8956 0.9243 0.9690 0.5 0.5345 1.3398 0.8430 0.8852 0.9524 0.6 0.6348 1.1882 0.7840 0.8405 0.9328 0.7 0.7318 1.0944 0.7209 0.7916 0.9107 1.0382 0.6560 0.7400 0.8865 0.8 0.8251 0.9 0.9146 1.0089 0.5913 0.6870 0.8606 1.0 1.0000 1.0000 0.5283 0.6339 0.8333S 3 1.2 1.1583 1.0304 0.4124 0.5311 0.7764 1.4 1.2999 1.1149 0.3142 0.4374 0.7184 1.6 1.4254 1.2502 0.2353 0.3557 0.6614 1.8 1.5360 1.4390 0.1740 0.2868 0.6068 2.0 1.6330 1.6875 0.1278 0.2300 0.5556 2.2 1.7179 2.0050 0.0935 0.1841 0.5081 2.4 1.7922 2.4031 0.0684 0.1472 0.4647 TABLE A-1 Molar mass, gas constant, and ideal-gas specfic heats of some substances VOL NAN Gas Constant Molar Mass M, kg/kmol Substance R, kJ/kg. K* Air 28.97 0.2870 17.03 0.4882 39.95 0.2081 Ammonia, NH3 Argon, Ar Bromine, Br₂ Isobutane, C4H10 159.31 0.05202 58.12 0.1430 n-Butane, C4H10 58.12 0.1430 Carbon dioxide, CO₂ 44.01 0.1889 Carbon monoxide, CO 28.01 0.2968 Chlorine, Cl₂ 70.905 0.1173 86.47 0.09615 Chlorodifluoromethane (R-22), CHCIF2 Ethane, C₂H6 30.070 0.2765 lewoll A \Sp S siune cumst one c4M olsy Specific Heat Data at 25°C CkJ/kg. K 0.7180 1.605 0.3122 0.1732 1.520 1.551 0.6550 0.7417 0.3608 0.5535 1.468 Cp. kJ/kg. K 1.005 2.093 0.5203 0.2253 1.663 1.694 0.8439 1.039 0.4781 0.6496 1.744 K= C₂/Cv 1.400 1.304 1.667 1.300 1.094 1.092 1.288 1.400 1.325 1.174 1.188
pressure = 1
(25 Marks)
Q2/ Air flows isentropically in a converging-diverging nozzle with initial Ma = 0.2,
MPa and temperature 27 C. Find the exit temperature, pressure and velocity
at
Ma = 1.8.
11
Transcribed Image Text:pressure = 1 (25 Marks) Q2/ Air flows isentropically in a converging-diverging nozzle with initial Ma = 0.2, MPa and temperature 27 C. Find the exit temperature, pressure and velocity at Ma = 1.8. 11
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