34377 dphe she
DESCRIPTION
hhhTRANSCRIPT
SHE DPHEF dingin F panas Tc in tc out th in th out F dingin F panas
1.5 4.5 22 26 44 24 360/5 20ml/10 detik1.5 5 22 26 45 261.5 2.5 23 27 42 281.5 2 22 28 42 301.5 5.5 22 29 39 311.5 5 23 30 36 321.5 4 23 32 35 321.5 4 23 32 38 321.5 3 23 32 37 32
F dingin F panasF dingin F panas Tc in tc out th in th out 1214/5
23 32 39 321 1.5 24 32 48 321 1.5 24 32 52 321 2 24 32 53 322 2 24 32 57 322 2 24 32 54 322 2 24 32 54 32 F dingin F panas2 2 24 32 53 32 1440/52 2 24 32 52 32
F dingin F panas Tc in tc out th in th out2.5 2 24 33.5 52 322.5 1.5 24 34 52 322.5 1.5 24 34 50 322.5 1.5 24 34.5 49 332.5 1.5 24 34.5 48 342.5 1.5 24 35 47 342.5 1.5 24 35 46 342.5 1.5 24 35 46 34
F dingin F panas Tc in tc out th in th out3 1.5 24 34.5 46 343 1.5 24 34 46 343 1.5 24 34 47 343 1.5 24 34 46 343 1.5 24 34 46 34
F dingin F panas Tc in tc out th in th out4 1.5 24 33.8 46 33.5
4.5 1.5 24 33 45 334.5 1.5 24 33 45 334.5 1.5 24 33 45 324.5 1.5 24 32.5 46 324.5 1.5 24 32.5 46 32
F dingin F panas Tc in tc out th in th out3 2.5 24 32 42 313 2.5 24 32 41.5 313 2.5 24 32 41.5 31.53 2.5 24 32 41.5 323 2.5 24 32.5 42 32
F dingin F panas Tc in tc out th in th out3.5 3 24 32.5 44 32
3 3 24 32.5 45 323 3 24 32.5 46 323 3 24 33 48 324 3 24 33 46.5 32.5
F dingin F panas Tc in tc out th in th out7.5 8 24 34 44 348.5 9 24 33.5 38 358.5 9 24 32 37 34
9 9 24 31 38 339 9 24 30 38 32
Tc in tc out th in th out24 28 28 2324 31 54 4924 30 48 36.524 30 46.5 36.524 30 46 3524 30.5 46 3424 30.5 47 3424 30.5 49 34
Tc in tc out th in th out24 29 50.5 30.524 29 52 3024 30 51.5 3024 30 53.5 3024 30 55 2924 29.5 48 29
Tc in tc out th in th out25 30 46 34.525 30 41.5 3125 30 40.5 3025 30 40 29.525 30 39 29.5
F dingin F panas Tc in tc out th in th out F dingin F panas Tc in1.5 2 22 28 42 30 1 1.5 241.5 3 23 32 37 32 2.5 1.5 241.5 4 23 32 38 32 3 1.5 241.5 5 22 26 45 26 4 1.5 241.5 5.5 22 29 39 31 4.5 1.5 24
F dingin F panas Tc in tc out th in th out F dingin F panas Tc in3 1.5 24 34 47 34 1 2 243 2.5 24 32.5 42 32 1.5 2 223 3 24 33 48 32 2 2 243 4 24 33 46.5 32.5 2.5 2 243 4.5 24 32 45 31.5 3 2 24
tc out th in th out32 52 3235 47 3434 46 34
33.8 46 33.532.5 46 32
tc out th in th out32 53 3230 47 3132 52 32
33.5 52 3232 42 31
Laju alir Air panas = 3 LPM
Tcold DensitasThi Tho Tci Tco (Tci+Tco)/(liat literat
3 44 34 22 33 0.0001 27.5 996.505 0.0996514 42 33 22 33 0.0001 27.5 996.505 0.0996516 42 33 22 33 0.0001 27.5 996.505 0.0996517 42 32 22 31 0.0001 26.5 996.735 0.0996748 42 31 22 30 0.0001 26 996.85 0.099685
10 42 30 22 28 0.0001 25 997.08 0.099708
Laju Alir Air dingin = 5 LPM
Tcold DensitasThi Tho Tci Tco (Tci+Tco)/(liat literat
3 36 31 22 30 0.00015 26 996.85 0.1495274 34 31 22 30 0.00015 26 996.85 0.1495276 36 30 24 30 0.00015 27 996.62 0.1494937 36 30 24 30 0.00015 27 996.62 0.1494938 36 30 24 29 0.00015 26.5 996.735 0.14951
10 36 29 24 28 0.00015 26 996.85 0.149527
Laju Alir Air Dingin
Suhu (oC)Laju Alir
Air Dingin (m3/s)
Laju Alir Air Dingin
(kg/s)
Laju Alir Air Dingin
Suhu (oC)Laju Alir
Air Dingin (m3/s)
Laju Alir Air Dingin
(kg/s)
Cp delta T Q1 Thot Densitas Cp delta T(liat literat (Tco-Tci) M*Cp*delta T (Thi+Tho)/(liat literat (liat literat (Thi-Tho)
4.1805 11 4.582478 0.00005 39 992.593 0.04963 4.181 104.1805 11 4.582478 6.667E-05 37.5 993.1075 0.066207 4.181 94.1805 11 4.582478 0.0001 37.5 993.1075 0.099311 4.181 94.1811 9 3.750704 0.000117 37 993.72 0.115934 4.1796 104.1814 8 3.334583 0.000133 36.5 993.86 0.132515 4.1797 11
4.182 6 2.501873 0.000167 36 994 0.165667 4.1798 12
Cp delta T Q1 Thot Densitas Cp delta T(liat literat (Tco-Tci) M*Cp*delta T (Thi+Tho)/(liat literat (liat literat (Thi-Tho)
4.1814 8 5.001874 0.00005 33.5 994.4795 0.049724 4.181 54.1814 8 5.001874 6.667E-05 32.5 994.8225 0.066322 4.181 34.1808 6 3.750002 0.0001 33 994.84 0.099484 4.1804 64.1808 6 3.750002 0.000117 33 994.84 0.116065 4.1804 64.1811 5 3.125587 0.000133 33 994.84 0.132645 4.1804 64.1814 4 2.500937 0.000167 32.5 994.98 0.16583 4.1805 7
Laju Alir Air Panas
(m3/s)
Laju Alir Air Panas
(kg/s)
Laju Alir Air Panas
(m3/s)
Laju Alir Air Panas
(kg/s)
Q2 EfisiensiM*Cp*delta T Q1/Q22.075016 2.2084062.491309 1.8393853.736964 1.2262574.845577 0.7740476.092587 0.5473188.309442 0.301088
Q2 EfisiensiM*Cp*delta T Q1/Q2
1.03948 4.8119020.831871 6.0128042.495297 1.502828
2.91118 1.2881383.327063 0.9394434.852766 0.515363
DINGIN TETAP
1. DINGIN 4 LPM
Thi (C) Tho © Tci © Tco © laju dingin
PANAS (LPM) DINGIN (LPM) L/s
2 1.5 42 30 22 28 0.025
3 1.5 37 32 23 32 0.025
4 1.5 38 32 23 32 0.025
5 1.5 45 26 22 26 0.025
5.5 1.5 39 31 22 29 0.025
1.5 3 47 34 24 34 0.05
2.5 3 42 32 24 32.5 0.05
3 3 48 32 24 33 0.05
4 3 46.5 32.5 24 33 0.05
4.5 3 45 31.5 24 32 0.05
2. DINGIN 8 LPM
laju panas (L/s)dingin (LPM) panas (LPM) Thi (C) Tho © Tci © Tco ©
1 1.5 52 32 24 32 0.025
2.5 1.5 47 34 24 35 0.025
3 1.5 46 34 24 34 0.025
4 1.5 46 33.5 24 33.8 0.025
4.5 1.5 46 32 24 32.5 0.025
1 2 53 32 24 32 0.03333333333333
1.5 2 47 31 22 30 0.03333333333333
2 2 52 32 24 32 0.03333333333333
2.5 2 52 32 24 33.5 0.03333333333333
3 2 42 31 24 32 0.03333333333333
F dingin F panas Tc in tc out th in th out1.5 2 22 28 42 30
1.5 3 23 32 37 32
1.5 4 23 32 38 321.5 5 22 26 45 261.5 5.5 22 29 39 31
F dingin F panas Tc in tc out th in th out3 1.5 24 34 47 343 2.5 24 32.5 42 323 3 24 33 48 323 4 24 33 46.5 32.53 4.5 24 32 45 31.5
dimensi Shell Jumlah Diameter Panjang
No
L/m L/s Thi Tho Tci Tco1 2 0.0333333333 42 30 22 282 3 0.05 37 32 23 323 4 0.0666666667 38 32 23 324 5 0.0833333333 45 26 22 265 5.5 0.0916666667 39 31 22 29
1 1.5 0.025 47 30 24 342 2.5 0.0416666667 42 32 24 32.53 3 0.05 48 32 24 334 4 0.0666666667 46.5 32.5 24 335 4.5 0.075 45 31.5 24 32
NoLaju air dingin
L/m L/s Thi Tho Tci Tco1 1 0.0166666667 52 32 24 322 2.5 0.0416666667 47 34 24 353 3 0.05 46 34 24 344 4 0.0666666667 46 33.5 24 33.85 4.5 0.075 46 32 24 32.5
1 1 0.0166666667 53 32 24 322 1.5 0.025 47 31 22 303 2 0.0333333333 52 32 24 324 2.5 0.0416666667 52 32 24 33.55 3 0.05 42 31 24 32
Laju air panas Suhu (oC)
Suhu (oC)
F dingin F panas Tc in tc out th in th out1 1.5 24 32 52 32
2.5 1.5 24 35 47 34
3 1.5 24 34 46 344 1.5 24 33.8 46 33.5
4.5 1.5 24 32.5 46 32
F dingin F panas Tc in tc out th in th out1 2 24 32 53 32
1.5 2 22 30 47 312 2 24 32 52 32
2.5 2 24 33.5 52 323 2 24 32 42 31
Dimensi tube Jumlah Diameter pipa luar Panjang A24 0.032 1.2 2.893824
ΔT1 ΔT2 ΔTlm Y Z14 8 10.722 0.300 2.0005 9 6.805 0.643 0.5566 9 7.399 0.600 0.667
19 4 9.627 0.174 4.75010 9 9.491 0.412 1.143
13 6 9.053 0.435 1.7009.5 8 8.729 0.472 1.17615 8 11.136 0.375 1.778
13.5 8.5 10.808 0.400 1.55613 7.5 9.999 0.381 1.688
ΔT1 ΔT2 ΔTlm Y Z20 8 13.096 0.286 2.50012 10 10.970 0.478 1.18212 10 10.970 0.455 1.20012.2 9.5 10.794 0.445 1.27613.5 8 10.511 0.386 1.647
21 8 13.470 0.276 2.62517 9 12.579 0.320 2.00020 8 13.096 0.286 2.50018.5 8 12.525 0.339 2.10510 7 8.411 0.444 1.375
Cp air 4184 J/kg.Kρ panas 0.998 kg/L
ρ dingin 0.9968 kg/L
42 0.9914 47 0.9894 22
37 0.9933 42 0.9914 23
38 0.9929 48 0.9889 24
45 0.9902 0.9896
39 0.9926 45 0.9902
panas
Ft ΔTm Mh (kg/s) Qi (J/s) U Mc (kg/s)
0.880 9.435 0.033 1659.207 22.935 0.025
0.880 5.989 0.050 1038.992 54.187 0.025
0.780 5.771 0.066 1661.717 56.228 0.025
0.700 6.739 0.083 6559.745 21.408 0.025
0.890 8.447 0.091 3045.561 29.887 0.025
0.620 5.613 0.025 1759.351 128.443 0.050
0.790 6.896 0.041 1728.341 88.872 0.050
0.790 8.797 0.049 3310.046 73.759 0.050
0.800 8.646 0.066 3864.454 75.046 0.050
0.820 8.199 0.074 4194.784 70.344 0.050
Ft ΔTm Mc (kg/s) Qi (J/s) U Mh (kg/s)
0.860 11.263 0.017 1390.901 25.343 0.025
0.800 8.776 0.042 2260.214 44.827 0.025
0.810 8.885 0.050 2503.622 40.265 0.025
0.830 8.959 0.066 3477.253 39.136 0.025
0.710 7.463 0.075 4381.338 40.749 0.025
0.810 10.911 0.017 1460.446 34.863 0.033
0.810 10.189 0.025 1669.081 37.440 0.033
0.810 10.608 0.033 2781.802 35.877 0.033
0.720 9.018 0.042 3477.253 50.116 0.033
0.840 7.065 0.050 2294.987 54.101 0.033
0.99777
0.9975 52 0.9871
0.9973 46 0.9898
53 0.9866
Qo (J/s) ɳ (%)
626.200 37.741
939.047 90.381
939.047 56.511
417.467 6.364
730.567 23.988
2086.352 118.586
1773.399 102.607
1877.716 56.728
1877.716 48.589
1669.081 39.789
Qo (J/s) ɳ (%)
826.005 59.386
1138.404 50.367
1035.331 41.353
1014.624 29.179
880.031 20.086
1100.783 75.373
1103.907 66.139
1101.340 39.591
1307.842 37.611
1106.138 48.198
0 2 4 6 8 10 12 14 160
100
200
300
400
Kurva U vs Laju Alir Air(Laju Alir Air Dingin Tetap)
4 L/menit 8 L/menit
Laju alir air panas (L/menit)
U (W
/m2.
K)
0 2 4 6 8 10 12 14 160
1000
2000
3000
4000
5000
6000
7000
Kurva Qi dan Qo vs Laju Alir Air(Laju Alir Air Dingin Tetap 4 L/menit)
Qlepas (W) Qterima (W)
Laju alir (L/menit)
Q (J
/s)
0 2 4 6 8 10 12 14 160
100
200
300
400
Kurva U vs Laju Alir Air(Laju Alir Air Dingin Tetap)
4 L/menit 8 L/menit
Laju alir air panas (L/menit)
U (W
/m2.
K)
0 2 4 6 8 10 12 14 160
1000
2000
3000
4000
5000
6000
7000
Kurva Qi dan Qo vs Laju Alir Air(Laju Alir Air Dingin Tetap 4 L/menit)
Qlepas (W) Qterima (W)
Laju alir (L/menit)
Q (J
/s)
0 2 4 6 8 10 12 14 160
1000
2000
3000
4000
5000
Kurva Qi dan Qo vs Laju Alir Air(Laju Alir Air Dingin Tetap 8 L/menit)
Qlepas (W) Qterima (W)
Laju alir (L/menit)
Q (J
/s)
3 4 5 6 7 8 9 10 11 120
50
100
150
200
250
300
350
Kurva Efisiensi vs Laju Alir Air(Laju Alir Air Dingin Tetap)
Laju Alir ari panas (L/m)
ɳ (%
0 2 4 6 8 10 12 14 160
1000
2000
3000
4000
5000
Kurva Qi dan Qo vs Laju Alir Air(Laju Alir Air Dingin Tetap 8 L/menit)
Qlepas (W) Qterima (W)
Laju alir (L/menit)
Q (J
/s)
3 4 5 6 7 8 9 10 11 120
50
100
150
200
250
300
350
Kurva Efisiensi vs Laju Alir Air(Laju Alir Air Dingin Tetap)
Laju Alir ari panas (L/m)
ɳ (%
Laju alir air dingin 6 l 4 lpm geankLaju alir air panas K air µ (kg/m.s)lpm lps m3/s v(m/s) Thi Nre
2.000 0.033 0.000 0.000 42.000 0.612 0.635 0.001 6.9073.000 0.050 0.000 0.000 37.000 0.673 0.629 0.001 10.4834.000 0.067 0.000 0.000 38.000 0.660 0.630 0.001 13.9425.000 0.083 0.000 0.000 45.000 0.580 0.638 0.001 17.1525.500 0.092 0.000 0.000 39.000 0.648 0.631 0.001 19.1281.500 0.025 0.000 0.000 47 0.560 0.641 0.001 5.1232.500 0.042 0.000 0.000 42 0.612 0.635 0.001 8.6343.000 0.050 0.000 0.000 48 0.550 0.642 0.001 10.2234.000 0.067 0.000 0.000 47 0.565 0.640 0.001 13.6774.500 0.075 0.000 0.000 45 0.580 0.638 0.001 15.437
Cp air 4184 J/kg.Kρ panas 0.998 kg/L 998 kg/m3ρ dingin 0.9968 kg/L 996.8 kg/m3Atube 2.7313478 m2 Din 0.02788 m Dout 0.032 mAshell 2.826 m2 Dshell 0.375 mL 1.2 m2
k(stainless) 13.8 W/m.K rin 0.01394 m
c 0.386 rout 0.016 m
m 0.592
Laju alir air dingin 6 l 8 lpm geank
Laju alir air panas K air µ (kg/m.s)
lpm lps m3/s v(m/s) Thi Nre
2.000 0.033 0.000 0.000 53.000 0.506 0.647 0.001 6.7432.000 0.033 0.000 0.000 47.000 0.560 0.641 0.001 6.8312.000 0.033 0.000 0.000 52.000 0.515 0.646 0.001 6.7582.000 0.033 0.000 0.000 52.000 0.515 0.646 0.001 6.7582.000 0.033 0.000 0.000 42.000 0.612 0.635 0.001 6.9071.500 0.025 0.000 0.000 52.000 0.515 0.646 0.001 5.0681.500 0.025 0.000 0.000 47.000 0.560 0.641 0.001 5.1231.500 0.025 0.000 0.000 46.000 0.570 0.640 0.001 5.1341.500 0.025 0.000 0.000 46.000 0.570 0.640 0.001 5.1341.500 0.025 0.000 0.000 46.000 0.570 0.640 0.001 5.134
Cp air 4184 J/kg.Kρ panas 0.998 kg/L 998 kg/m3ρ dingin 0.9968 kg/L 996.8 kg/m3
Atube 2.7313478 m2 Din 0.02788 m Dout 0.032 mAshell 2.826 m2 Dshell 0.375 mL 1.2 m2k(stainless) 13.8 W/m.K rin 0.01394 mc 0.386 rout 0.016 mm 0.592
laju air dingin tetap µ (kg/m.s)Npr Nnu lpm lps m3/s v (m/s) Tco Kair
4.340 1.967 1.500 0.025 0.000 0.000 28.000 0.812 0.6173.907 2.432 1.500 0.025 0.000 0.000 32.000 0.745 0.6223.993 2.900 1.500 0.025 0.000 0.000 32.000 0.745 0.6224.607 3.437 1.500 0.025 0.000 0.000 26.000 0.849 0.6144.078 3.522 1.500 0.025 0.000 0.000 29.000 0.794 0.6184.789 1.703 3.000 0.050 0.000 0.000 34.000 0.715 0.6254.340 2.245 3.000 0.050 0.000 0.000 32.500 0.737 0.6234.881 2.579 3.000 0.050 0.000 0.000 33.000 0.730 0.6244.743 3.035 3.000 0.050 0.000 0.000 33.000 0.730 0.6244.607 3.229 3.000 0.050 0.000 0.000 32.000 0.745 0.622
K air viskositas air F dingin F panas Tc inT(oC) k T(oC) Vis 1.5 2 22
0 0.5694 52 0.5132 1.5 3 2315.6 0.5884 54 0.5146 1.5 4 2326.7 0.6109 56 0.4985 1.5 5 2237.8 0.6283 58 0.4832 1.5 5.5 22
65.6 0.6629 35 0.7228
93.3 0.6802 32 0.7679 42 0.9914 47
37 0.9933 4238 0.9929 48
45 0.990239 0.9926 45
laju air dingin tetap µ (kg/m.s)
Npr Nnu lpm lps m3/s v (m/s) Tco Kair
5.349 2.078 1.000 0.017 0.000 0.000 32.000 0.745 0.6224.789 2.019 1.500 0.025 0.000 0.000 30.000 0.777 0.6195.254 2.068 2.000 0.033 0.000 0.000 32.000 0.745 0.6225.254 2.068 2.500 0.042 0.000 0.000 33.500 0.722 0.6244.340 1.967 3.000 0.050 0.000 0.000 32.000 0.745 0.6225.254 1.744 1.000 0.017 0.000 0.000 32.000 0.745 0.6224.789 1.703 2.500 0.042 0.000 0.000 35.000 0.701 0.6264.698 1.694 3.000 0.050 0.000 0.000 34.000 0.715 0.6254.698 1.694 4.000 0.067 0.000 0.000 33.800 0.718 0.6254.698 1.694 4.500 0.075 0.000 0.000 32.500 0.737 0.623
F dingin F panas Tc in tc out1 2 24 32
1.5 2 22 30K air viskositas air 2 2 24 32T(oC) k T(oC) Vis 2.5 2 24 33.5
0 0.5694 52 0.5132 3 2 24 32
15.6 0.5884 54 0.514626.7 0.6109 56 0.498537.8 0.6283 58 0.483265.6 0.6629 35 0.722893.3 0.6802 32 0.7679
µ (kg/m.s)Nre Npr Nnu hi ho 1/hi.2pi.ri. ln(ro/ri)/k.2
0.001 5.543 3.178 0.253 125.070 848.277 0.076 0.0010.001 5.489 3.494 0.276 136.551 1048.902 0.070 0.0010.001 5.489 3.494 0.276 136.512 1250.766 0.070 0.0010.001 5.575 3.025 0.242 119.572 1482.350 0.080 0.0010.001 5.531 3.255 0.259 128.003 1518.864 0.074 0.0010.001 10.926 3.657 0.573 283.853 734.210 0.034 0.0010.001 10.966 3.534 0.557 275.595 968.074 0.035 0.0010.001 10.952 3.575 0.562 278.032 1112.203 0.034 0.0010.001 10.952 3.575 0.562 278.135 1308.891 0.034 0.0010.001 10.979 3.494 0.551 272.518 1392.715 0.035 0.001
tc out th in th out F dingin F panas Tc in tc out28 42 30 3 1.5 24 3432 37 32 3 2.5 24 32.532 38 32 3 3 24 3326 45 26 3 4 24 3329 39 31 3 4.5 24 32
0.9894 22 0.99777 47 0.9894 29 0.9959 34
0.9914 23 0.9975 52 0.9871 32 0.9951 32.5
0.9889 24 0.9973 46 0.9898 32 0.9951 33
0.9896 53 0.9866 26 0.9968 33
0.9902 29 0.9959 32
µ (kg/m.s)
Nre Npr Nnu hi ho 1/hi.2pi.ri. ln(ro/ri)/k.2
0.001 11.711 3.494 0.586 290.129 896.049 0.033 0.0010.001 17.647 3.334 0.844 417.525 870.531 0.023 0.0010.001 23.422 3.494 1.173 580.396 891.917 0.016 0.0010.001 29.154 3.616 1.511 747.973 891.917 0.013 0.0010.001 35.133 3.494 1.763 872.728 848.277 0.011 0.0010.001 11.711 3.494 0.586 290.198 752.248 0.033 0.0010.001 29.051 3.739 1.560 771.987 734.210 0.012 0.0010.001 34.962 3.657 1.836 908.548 730.521 0.010 0.0010.001 46.607 3.641 2.436 1205.842 730.521 0.008 0.0010.001 52.638 3.534 2.670 1321.489 730.521 0.007 0.001
th in th out F dingin F panas Tc in tc out th in 53 32 1 1.5 24 32 52
47 31 2.5 1.5 24 35 4752 32 3 1.5 24 34 4652 32 4 1.5 24 33.8 4642 31 4.5 1.5 24 32.5 46
53 0.986647 0.989452 0.987152 0.9871
42 0.9914
Interpolasi
1/ho.2pi.ro U Thi k miu Tco k
0.010 11.466 53 0.5062 0.6472 32 0.74510.008 12.667 47 0.5598 0.6407 30 0.77730.007 12.872 52 0.5145 0.6461 32 0.74510.006 11.557 52 0.5145 0.6461 33.5 0.72230.005 12.323 42 0.6121 0.6349 32 0.74510.011 21.665 38 0.6285 0.6814 32 0.619208110.009 22.506 34 0.6223 0.7371 32 0.619208110.007 23.245 34 0.6223 0.7371 32 0.619208110.006 23.8740.006 23.691 K air
th in th out T(oC) k T(oC) Vis47 34 0 0.5694 26 8.49E-01 0.613742 32 15.6 0.5884 27 8.30E-01 0.615248 32 26.7 0.6109 28 8.12E-01 0.6166
46.5 32.5 37.8 0.6283 29 7.94E-01 0.61845 31.5 65.6 0.6629 30 7.77E-01 0.6194
93.3 0.6802 32 7.45E-01 0.62220.9944 33 7.30E-01 0.6235
0.9949 34 7.15E-01 0.62480.9947 35 0.7006 0.62610.9947 36 6.87E-01 0.62740.9951 38 6.60E-01 0.63
40 6.35E-01 0.6325
42 6.12E-01 0.63491/ho.2pi.ro U 44 5.90E-01 0.6373
0.009 23.046 46 5.70E-01 0.63960.010 29.717 47 5.60E-01 0.64070.009 37.003 48 5.50E-01 0.64180.009 42.826 49 5.41E-01 0.64290.010 45.435 50 5.32E-01 0.6440.011 22.147 51 5.23E-01 0.64510.011 40.077 52 5.15E-01 0.64610.011 43.186 53 5.06E-01 0.64720.011 48.609 54 4.98E-01 0.64820.011 50.298 56 4.83E-01 0.6502
58 0.483233.5 7.22E-01 0.6242
37 6.73E-01 0.6287th out 45 5.80E-01 0.6384
32 39 6.48E-01 0.6312
34 32.5 7.37E-01 0.622834 46.5 5.65E-01 0.6401
33.5 33.8 7.18E-01 0.624632
miu
0.6222 420.6194 370.6222 380.6242 450.6222 39
den22 0.9977723 0.997524 0.997326 0.996829 0.9959
32 0.9951 42 0.9914 47 0.9894
32.5 0.9949 42 0.9914
33 0.9947 48 0.9889
33.8 0.9939 45 0.9902 0.9896
34 0.9944 45 0.990237 0.993338 0.992939 0.992642 0.991445 0.990246 0.9898
46.5 0.989647 0.989448 0.988952 0.987153 0.9866
28 9.96E-0130 9.95E-01
33.5 9.94E-0135 9.94E-01
3 4 5 6 7 8 9 10 11 120
20
40
60
80
100
120
140
Laju Alir vs U
4 L/m8 L/m
Laju Alir Air Panas (L/m)
U
3 4 5 6 7 8 9 10 11 120
20
40
60
80
100
120
140
Laju Alir vs U
4 L/m8 L/m
Laju Alir Air Panas (L/m)
U
3 4 5 6 7 8 9 10 11 120
20
40
60
80
100
120
140
Laju Alir vs U
4 L/m8 L/m
Laju Alir Air Panas (L/m)
U
3 4 5 6 7 8 9 10 11 120
20
40
60
80
100
120
140
Laju Alir vs U
4 L/m8 L/m
Laju Alir Air Panas (L/m)
U