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Jalur Nama Penghubu Jalur Pipa ng
Pkerja (KPa)
SPM Tanki Flushing oil flushing oil onshore
179.172
60
90
268.758
Tanki loading oil onshore SPM
194.358
80
120
291.537
Ballast water
SPM – Tanki ballast water
980.665
40
60
1470.997
Nama Jalur Pipa
Mp (KG/m)
Black oil
Flushing oil Black oil Ballast water
Pw
Pf
Tdesain (0C)
Tkerja (oC)
Pdesain (KPa)
Diameter dalam Diamter Mc (Kg/m) (m) luar (m)
145.69 167.58
1025 1025
1040 1040
0.321 0.371
84.23 112.62
0.356 0.406
167.58
1025
1040
0.371
112.62
0.406
E (Kpa)
207000000
207000000
207000000
Ma (Kg/m)
Diameter dalam (mm)
321.2
371.42
371.42
Total berat pipa
diameter (mm)
tegangan yang tebal pipa diijinkan
tebal nominal
Tebal nominal desain
355.6 322560
0.15
16.15
17.48
322560
0.18
16.18
17.48
322560
0.93
16.93
17.48
406.4
406.4
K
Vk
Kecepatan arus
RE
101.75 132.89
331.66 413.10
0.227 0.000001 0.248 0.000001
0.27 0.27
91440 104503
132.89
413.10
0.248 0.000001
0.27
104503
D/t
Longiudin hoop stress thin Schedule al stress wall thin wall
strain hoop
Longitudinal strain
min temperata ru installation
60 20.34
2733.71
1366.85 1.32063E-005 6.60315E-006
-30
3389.03
1694.52 1.63721E-005 8.18607E-006
-30
17099.92
8549.96 8.26083E-005 4.13042E-005
-30
60 23.25
60 23.25
alfa
poison ratio
longitduin al stress combine
hoop strain
Tegangan Tegangan kombinasi kombinasi tekanan tekanan internal internal
0.000014
0.3
260000 0.000896
467071.62
1366.85
0.000014
0.3
317763 0.001096
717847.06
1694.52
0.000014
0.3
197730 0.000776
18275452.63
8549.96
Tegangan kombinasi tekanan dan temparatur
Tegangan kombinasi tekanan dan temparatur
Tegangan kompresi akibat temperatur dan tekanan
16546472207.0651
257266.18
259999.89
24707793129.7553
314374.26
317763.29
8156808692.9908
180630.10
197730.02
