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Mech. Calc
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RO CalculationsCalculation of the Wetted surface Area
Vessel informationOD 3.75 ftL 36 ftT 64P 1160.3 psiz1 0.8325
Lower Portion - CondensateLAHH 3.3 ft
15.2
39.3
54.5
Upper Portion GlycolLAHH 2.5 ft
29.5
Total Surface Area VesselTotal 83.9Total + 20% 100.7
Calculation Of Heat inputQ 880328.06 BTU/hrλ 178 BTU/lbW 4946 lb/hrW 2243 kg/hr
Volume CalculationsCylinder 346.4Heads 11.220% pipe 71.5Total 429.1m1 1723.2 lb
-5.50.9695
100 psi assumes constant volume for Delta Mass166.53214 isolated system at RO open
del mass 1556.7 lb 706.0989 kgtime 15 minrate 103.8 lb/minrate 6226.7 lb/hr
Overall Rate Relief and Vessel Volumerate 11172 lb/hr
5067.7133 kg/hr
oF
Areahead ft2
Arealevel ft2
Arealower ft2
Arealevel ft2
ft2
ft3
ft3
ft3
ft3
T2
z2
P2
m2
RO sizing
Method: Use API 520 Gas critical flow eqn for PRV
Input data 01-380-0-VE-01 01-380-0-VE-01Case LAHH LALL
Fire Wetted Fire WettedW flow rate kg/h 5067.71 5067.71cp/cv 1.177 1.177C coeff based on cp/cv 336 336Kd eff coeff of discharge 0.975 0.975P1 upstream pressure kPaa 7978 7978Kb capacity correction factor due to back pressure 1 1Kc corection factor for rupture disk 1 1T relieving temp K 291 291Z compressibility factor 0.833 0.833M molecular weight 16.00 16.00
Calculated values
A mm2 99.29 99.29d equiv orifice dia mm 11.24 11.24
Selected orifice dia mm 20see "Numerical" for sizing
required effective discharge area= 13160.W/(C.Kd.P1.Kb.Kc).(TZ/M)0.5
Equation
constantsM 16R 8314.5C 0.72k 1.17Pa 200000
1.753234317 3.45 A 0.000314 m2 Orifice size 20
Target Mass to hit 1266.928 kginterval 1.67 min
P kPa Z T (K) degF t mass (kg). cumulativeQi (kg/s) 3.277506 8000000 0.8325 291 1.7 327.75
2.870869 7000000 0.8445 286.3 55.86 3.3 287.09 614.842.464943 6000000 0.855 281.8 47.8 5.0 246.49 861.332.055841 5000000 0.8685 276.9 39.08 6.7 205.58 1066.921.644514 4000000 0.8854 271.7 29.66 8.3 164.45 1231.371.231809 3000000 0.9065 266.1 19.5 10.0 123.18 1354.550.819227 2000000 0.9321 260.0 8.6 11.7 81.92 1436.470.408056 1000000 0.9631 253.6 -3 13.3 40.81 1477.280.281346 690000 0.97 252.1 -5.56 15.0 28.13 1505.410.203549 500000 0.9808 250.2 -9.125 16.666666667 20.35
1505.41
Hourly Rate 6022 kg/hr
PROJECT : OYO FPSO
JOB NO : 2008-07
LOCATION : Nigeria
CLIENT : BA / ENI
REFERENCES : 1. ISOTHERMAL FLOW - API 521, 4TH EDITION, MARCH 1997, SECTION 5.42. FITTINGS K FACTOR - FLOW OF FLUIDS THROUGH VALVES, FITTINGS AND PIPE, CRANE3. FRICTION FACTORS - HSI-JEN CHEN EQUATION "SOLVING FLUID FLOW PROBLEMS WITH SPREADSHEETS", HYDROCARBON PROCESSING, SEPTEMBER 1989.
GENERAL DATA
Line number
PFD stream number
Fluid HC gas
Case
PROCESS INPUT DATA
Mass flowrate (kg/hr) 6021.644
Temperature (deg C) 17.85
Pipe outlet pressure (bar abs) 2.01
Molecular weight 20
Compressibility factor Z 0.8325
Specific heat ratio 1.177
Fluid viscosity (cP) 0.013172
PIPE SIZE DATA
Pipe schedule 80
Pipe nominal diameter (in) 4"
Pipe OD (mm) 114.3
Pipe ID no. 10
Pipe thickness (mm) 8.56
Pipe internal diameter (mm) 97.18
Absolute roughness (mm) 0.045
PIPE & FITTINGS
Pipe straight length (m) 5.3
Fittings (K factors)
Globe valve Stem perpendicular to run
Y-pattern
Angle valve
Gate valve Wedge disc, double disc, plug
Check valve Conventional swing
ISOTHERMAL COMPRESSIBLE FLOW PRESSURE DROP CALCULATION SHEET
From d/s RO-4302(1)
ToHP Flare
Header (2)
Fire wetted
depresur.
Lift check valve
Footvalve Poppet disc w/ strainer
Ball valve Full bore 1 0.050
Reduced bore <= 1 1/2"
Reduced bore > 1 1/2"
Butterfly valve 2" to 8"
10" to 14"
16" to 24"
Plug valve Straight thru'
90° Elbow welded/flange, 1.5D
welded/flange, 3D 3 0.603
screwed, std
45° Elbow
Tee Flow thru run 3 1.005
Flow thru branch
Reducer Enlargement
Contraction
Pipe entrance 1 0.780
Pipe exit 1 1.000
Others
Total K factors for fittings 3.437558
Total equivalent length for fittings (m) 19.95232
Total equivalent length for pipe & fittings (m) 25.25232
OUTPUT
Pipe outlet fluid density (kg/m3) 1.9959
Pipe inlet fluid density (kg/m3) 2.418702
Average fluid density (kg/m3) 2.207301
Type of flow subsonic
Mach number at pipe outlet 0.328347
Reynold number 1675560
Friction factor 0.016743
(kg/m.s2) 25846.91
Flow regime Turbulent
(bar) Err:522
Pipe inlet pressure (bar abs) Err:522
Pipe outlet pressure (bar abs) 2.01
Pipe outlet volumetric flowrate (m3/hr) 3017.007
Pipe outlet average velocity (m/sec) 113.7981
Reynolds number 1675560
Friction factor constant A 0.000125
Friction factor constant B 3E-06
1/f^0.5 7.728286
Friction factor 0.016743
Mass flowrate (lb/hr) 13277.73
rv2
DP
Temperature (deg F) 64.13
(Rankine) 524.13
Pipe outlet pressure (psi a) 29.1497
Critical pressure (psi a) 9.571623
Corrected pipe outlet pressure (psi a) 29.1497
Molecular weight 20
Compressibility factor Z 0.8325
Specific heat ratio 1.177
Fluid viscosity (cP) 0.013172
Pipe internal diameter (inch) 3.825984
(feet) 0.318832
Flow type subsonic
Mach number at pipe outlet 0.328347
Corrected Mach number at pipe outlet 0.328347
Pipe equivalent length (feet) 82.8276
fL/D 4.349575
Per API 521
Pipe inlet pressure P1 (psi abs) 35.32944
P1' 29.1507
P1' ERR 1
P1' n+1 35.32944
y 4.349643
ISERROR(81) 1
Pipe inlet pressure (bar abs) 2.435789
REV 0DATE 11/25/2008BY LYLCHECKED KKP
1. ISOTHERMAL FLOW - API 521, 4TH EDITION, MARCH 1997, SECTION 5.42. FITTINGS K FACTOR - FLOW OF FLUIDS THROUGH VALVES, FITTINGS AND PIPE, CRANE3. FRICTION FACTORS - HSI-JEN CHEN EQUATION "SOLVING FLUID FLOW PROBLEMS WITH SPREADSHEETS",
VE-01 (3)
HC gas
6021.644
17.85
80.8
20
0.8325
1.177
0.013172
80
2"
60.3
10
5.54
49.22
0.045
1
ISOTHERMAL COMPRESSIBLE FLOW PRESSURE DROP CALCULATION SHEET VER. 1.03 (June 2004)
u/s RO-4302(4)
Fire wetted
depresur.
1 0.058
3 1.159
1 0.780
1 1.000
2.996872
7.636693
8.636693
80.2332
80.37054
80.30187
subsonic
0.031846
3308227
0.019315
9770.898
Turbulent
Err:522
Err:522
80.8
75.05178
11.03545
3308227
0.000247
1.52E-06
7.195281
0.019315
13277.73
64.13
524.13
1171.605
37.31266
1171.605
20 0 0 0
0.8325 0 0 0
1.177 0 0 0
0.013172 0 0 0
1.937795
0.161483
subsonic
0.031846
0.031846
28.32835
3.388435
1173.616
1171.606
1
1173.616
3.388437
1 0 0 0
80.93832
SummaryFlow rates
From vessel volume 2824 kg/hrFrom fire relief 2243 kg/hrtotal 5068 kg/hr
Mass needed to evacuate in 15 min1267 kg
Orrifice sized for RV fire case11.24 mm
Orrifice sized using Numerical methodSelected 20 mm
Flow rate in the 15 min duration 6022 kg/hr
Line SizingInlet
size 2"DP Err:522 barMach 0.032Velocity 11.04 m/s
Outletsize 4"DP Err:522 barMach 0.33Velocity 113.80 m/s