labtk-perhitungan aliran fluida
DESCRIPTION
laporanTRANSCRIPT
Data Pengamatan Aliran Fluida
Venturi
TurbulenNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 625 356 601 395 5 102 722 455 515 324 5 5.27 5.503 790 527 454 260 5 4.22 4.504 802 537 444 250 5 4.08 3.49
Orifice P0= 607 350 609 425
TurbulenNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 579 310 725 540 5 6.802 614 347 750 540 5 12.883 660 392 715 523 5 24.524 667 395 718 524 5 25.47
TransisiNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 691 423 705 510 0.620 10
LaminerNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 670 398 710 515 0.320 102 670 400 710 515 0.280 10
Pipa LurusP0= 677 407 699 505TurbulenNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 635 365 750 560 5 7.41 8.392 645 375 740 545 5 8.18 8.913 675 405 730 530 5 16.01 15.264 677 406 727 533 5 15.60 17.37
Transisi
No ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)A B C D
1 680 410 720 525 0.6 10680 410 720 525 0.67 10
LaminerNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 679 410 719 523 0.31 10
679 410 719 523 0.31 102 680 410 719 524 0.21 10
680 410 719 524 0.22 10
Elbow P0 = 250TurbulenNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 650 380 740 547 5 7.50
660 390 740 555 5 8.372 651 381 715 520 5 4.74
651 381 715 520 5 3.953 644 371 719 525 5 5.95
644 371 719 525 5 6.864 635 365 720 530 5 12.94
635 365 720 530 5 13.66
TransisiNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 636 365 745 554 0.55 10
0.54 10
LaminerNo ∆P Volume (Liter) t1 (s) t2 (s) t rata-rata (s)
A B C D1 635 365 745 555 0.32 10
635 365 745 555 0.34 102 635 365 745 555 0.22 10
635 365 745 555 0.23 10
Jenis Aliran No ∆H (mmHg) Volume (L) Waktu (s) Debit (L/s)a b c d (d-c)-(b-a) (c-a)
∆Pturbulen 1 380 650 547 740 -77 167 5.00 7.50 0.67
390 660 555 740 -85 165 5.00 8.37 0.605.00 7.94 0.63
2 381 651 520 715 -75 139 5.00 4.74 1.05381 651 520 715 -75 139 5.00 3.95 1.27
5.00 4.35 1.153 371 644 525 719 -79 154 5.00 5.95 0.84
371 644 525 719 -79 154 5.00 6.86 0.735.00 6.41 0.78
4 365 635 530 720 -80 165 5.00 12.94 0.39365 635 530 720 -80 165 5.00 13.66 0.37
5.00 13.30 0.38transisi 1 365 636 554 745 -80 189 0.55 10.00 0.06
365 636 554 745 -80 189 0.54 10.00 0.050.55 10.00 0.05
laminer 1 365 635 555 745 -80 190 0.32 10.00 0.03365 635 555 745 -80 190 0.34 10.00 0.03
0.33 10.00 0.032 365 635 555 745 -80 190 0.22 10.00 0.02
365 635 555 745 -80 190 0.23 10.00 0.020.23 10.00 0.02
ρ minyak ρ air g (d-c)-(b-a) m (c-a) m ∆P Debit (m3/s) V0 (m/s) Ke
805.55 998.8 9.8 -0.08 0.167 1026.77 0.00067 0.56 6.60805.55 998.8 9.8 -0.09 0.165 944.04 0.00060 0.50 7.55805.55 998.8 9.8 0.00 0 0.00 0.00063 0.53 0.00805.55 998.8 9.8 -0.08 0.139 768.49 0.00105 0.88 1.97805.55 998.8 9.8 -0.08 0.139 768.49 0.00127 1.06 1.37805.55 998.8 9.8 0.00 0 0.00 0.00115 0.96 0.00805.55 998.8 9.8 -0.08 0.154 883.73 0.00084 0.70 3.57805.55 998.8 9.8 -0.08 0.154 883.73 0.00073 0.61 4.75805.55 998.8 9.8 0.00 0 0.00 0.00078 0.65 0.00805.55 998.8 9.8 -0.08 0.165 983.51 0.00039 0.32 18.80805.55 998.8 9.8 -0.08 0.165 983.51 0.00037 0.31 20.96805.55 998.8 9.8 0.00 0 0.00 0.00038 0.31 0.00805.55 998.8 9.8 -0.08 0.189 1218.43 0.00006 0.05 1149.83805.55 998.8 9.8 -0.08 0.189 1218.43 0.00005 0.05 1192.81805.55 998.8 9.8 0.00 0 0.00 0.00005 0.05 0.00805.55 998.8 9.8 -0.08 0.19 1228.21 0.00003 0.03 3424.00805.55 998.8 9.8 -0.08 0.19 1228.21 0.00003 0.03 3033.03805.55 998.8 9.8 0.00 0 0.00 0.00003 0.03 0.00805.55 998.8 9.8 -0.08 0.19 1228.21 0.00002 0.02 7244.18805.55 998.8 9.8 -0.08 0.19 1228.21 0.00002 0.02 6627.94805.55 998.8 9.8 0.00 0 0.00 0.00002 0.02 0.00
P Q944.04 0.00063768.49 0.00115883.73 0.00078983.51 0.00038
1218.43 0.000051228.21 0.000031228.21 0.00002
Nre
Ke Nre24166.02 3033.03 815.603
21654.14 6627.94 1196.218
22841.22 1192.81 1975.572
38237.37 20.96 13627.45
45884.84 7.55 22841.22
41713.49 4.75 28297.44
30461.36 1.37 41713.4926420.5728297.4414006.5813268.3113627.451993.6961957.4471975.5721159.9691232.4671196.218797.4785833.7275
815.603
P Q1228.21 0.000021228.21 0.000031218.43 0.00005
983.51 0.00038944.04 0.00063883.73 0.00078768.49 0.00115
600 800 1000 1200 1400 1600 1800 2000 22000
1000
2000
3000
4000
5000
6000
7000
TransisiLaminer
Bilangan Reynold (Nre)Ko
nsta
nta
Elbo
w (K
e)
10000 15000 20000 25000 30000 35000 40000 450000
5
10
15
20
25
Turbulen
Bilangan Reynold (Ke)
Kons
tant
a El
bow
(Ke)
000,000 000,000 000,0000.00
200.00
400.00
600.00
800.00
1000.00
1200.00
Turbulen
Laju Alir
Teka
nan
000,000 000,000 000,0001212.00
1214.00
1216.00
1218.00
1220.00
1222.00
1224.00
1226.00
1228.00
1230.00
TransisiLaminer
Laju Alir
Teka
nan
000,000 000,000 000,0000.00
200.00
400.00
600.00
800.00
1000.00
1200.00
Turbulen
Laju AlirTe
kana
n000,000 000,000 000,000
1212.00
1214.00
1216.00
1218.00
1220.00
1222.00
1224.00
1226.00
1228.00
1230.00
TransisiLaminer
Laju Alir
Teka
nan
600 800 1000 1200 1400 1600 1800 2000 22000
1000
2000
3000
4000
5000
6000
7000
TransisiLaminer
Bilangan Reynold (Nre)
Kons
tant
a El
bow
(Ke)
10000 15000 20000 25000 30000 35000 40000 450000
5
10
15
20
25
Turbulen
Bilangan Reynold (Ke)
Kons
tant
a El
bow
(Ke)
000,000 000,000 000,0001212.00
1214.00
1216.00
1218.00
1220.00
1222.00
1224.00
1226.00
1228.00
1230.00
TransisiLaminer
Laju Alir
Teka
nan
000,000 000,000 000,0001212.00
1214.00
1216.00
1218.00
1220.00
1222.00
1224.00
1226.00
1228.00
1230.00
TransisiLaminer
Laju Alir
Teka
nan
Jenis Aliran No ∆H (mmHg) Volume (L) Waktu (s)a b c d (d-c)-(b-a) (c-a)
∆Pturbulen 1 380 650 547 740 -77 167 5.00 7.50
390 660 555 740 -85 165 5.00 8.375.00 7.94
2 381 651 520 715 -75 139 5.00 4.74381 651 520 715 -75 139 5.00 3.95
5.00 4.353 371 644 525 719 -79 154 5.00 5.95
371 644 525 719 -79 154 5.00 6.865.00 6.41
4 365 635 530 720 -80 165 5.00 12.94365 635 530 720 -80 165 5.00 13.66
5.00 13.30transisi 1 365 636 554 745 -80 189 0.55 10.00
365 636 554 745 -80 189 0.54 10.000.55 10.00
laminer 1 365 635 555 745 -80 190 0.32 10.00365 635 555 745 -80 190 0.34 10.00
0.33 10.002 365 635 555 745 -80 190 0.22 10.00
365 635 555 745 -80 190 0.23 10.000.23 10.00
Debit (L/s) ρ minyak ρ air g (d-c)-(b-a) m (c-a) m ∆P Debit (m3/s)
0.67 805.55 998.8 9.8 -0.08 0.167 1026.77 0.000670.60 805.55 998.8 9.8 -0.09 0.165 944.04 0.000600.63 805.55 998.8 9.8 0.00 0 0.00 0.000631.05 805.55 998.8 9.8 -0.08 0.139 768.49 0.001051.27 805.55 998.8 9.8 -0.08 0.139 768.49 0.001271.15 805.55 998.8 9.8 0.00 0 0.00 0.001150.84 805.55 998.8 9.8 -0.08 0.154 883.73 0.000840.73 805.55 998.8 9.8 -0.08 0.154 883.73 0.000730.78 805.55 998.8 9.8 0.00 0 0.00 0.000780.39 805.55 998.8 9.8 -0.08 0.165 983.51 0.000390.37 805.55 998.8 9.8 -0.08 0.165 983.51 0.000370.38 805.55 998.8 9.8 0.00 0 0.00 0.000380.06 805.55 998.8 9.8 -0.08 0.189 1218.43 0.000060.05 805.55 998.8 9.8 -0.08 0.189 1218.43 0.000050.05 805.55 998.8 9.8 0.00 0 0.00 0.000050.03 805.55 998.8 9.8 -0.08 0.19 1228.21 0.000030.03 805.55 998.8 9.8 -0.08 0.19 1228.21 0.000030.03 805.55 998.8 9.8 0.00 0 0.00 0.000030.02 805.55 998.8 9.8 -0.08 0.19 1228.21 0.000020.02 805.55 998.8 9.8 -0.08 0.19 1228.21 0.000020.02 805.55 998.8 9.8 0.00 0 0.00 0.00002
A V0
0.00037994 1.7546630.00037994 1.5722790.00037994 1.6584720.00037994 2.7763660.00037994 3.3316390.00037994 3.0287620.00037994 2.211760.00037994 1.9183630.00037994 2.0546410.00037994 1.0169990.00037994 0.9633950.00037994 0.9894720.00037994 0.144760.00037994 0.1421280.00037994 0.1434440.00037994 0.0842240.00037994 0.0894880.00037994 0.0868560.00037994 0.0579040.00037994 0.0605360.00037994 0.05922
Vo (m/s)
(Nre)
Laminer0.000031 5,297,807 0.02596 170,529,816 11,235,834
0.0000215 5,237,801 0.01801 35,029,596 7,794,968
Transisi 0.0000635 5,335,684 0.05318 40,175,926 23,017,013
Turbulen
0.000634 12,771,556 0.53098 0.0982655 229,815,224
0.000585 10,719,215 0.48995 0.0968663 212,056,893
0.00031 6,709,227 0.25963 0.2159117 112,371,326
0.000304 6,352,385 0.25461 0.2125668 110,198,603
Jenis aliran
Debit (m3/s)Fanning friction
factor (F)
BilanganReynold
0
100,000,000
200,000,000
300,000,0000
20,000,00040,000,00060,000,00080,000,000
100,000,000120,000,000140,000,000160,000,000180,000,000
fanning friction terhadap NRe
fanning friction terhadap NRe
0
100,000,000
200,000,000
300,000,0000
20,000,00040,000,00060,000,00080,000,000
100,000,000120,000,000140,000,000160,000,000180,000,000
fanning friction terhadap NRe
fanning friction terhadap NRe