API 650 API 620 SEISMIC CALC Sherical Tank EN14620 ALLOWABLE STRESS
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[AAA1] [AAA2] 
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1. TANK DESIGN DATA
DescriptionInner TankOuter Tank
Tank ContainmentAPI 625 SINGLE Containment
Design CodeAPI 620 12th Edition Annex R (ADDENDUM 1, NOV. 2014)
Content NameLPG
Specific Gravity (Density)SG =0.581 (p = 581 kg/kg/cm³)
Nominal capacity Vnom =46633.0m©ø27094Ton@SG
Storage capacity VSto =44705.2m©ø25974Ton@SG
Net working capacityVnet =40633.5m©ø23608Ton@SG
Vapor Space capacityVapor =1927.8m©ø4.13% Vapor Space Ratio VSR = Vapor / Vnom * 100
Tank inside diameter D =46000mm150.919ft48000mm157.480ft
Tank Height HT =28060mm92.060ft31000mm101.706ft
High High Liquid LevelHHLL =26900mm88.255ft25168mm82.572ft
High Liquid Level HLL =26550mm87.106ft25168mm82.572ft
Low Liquid Level LLL =2450mm8.038ft25168mm82.572ft
Hydrostatic Test LevelHTL =26900mm88.255ft22826mm74.888ft
Design Temperature-45.0ºC7.0ºF65.0ºC68.1ºF
Operating Temperature-45.0ºC7.0ºF40.0ºC54.2ºF
Design pressure (Internal)0.153kg/cm²15.000kPa.g
Design pressure (External)0.002kg/cm²0.200kPa.g
Operating pressure 0.088kg/cm²8.600kPa.g
Pneumatic Test pressure0.191kg/cm²18.750kPa.g
Shell Joint Efficiency1.001.00
InsulationYes (Cold)
Max. Boil - off Rate0.05 wt% / Day
Design Wind Speed (3-sec.gust)34 m/sec
Seismic DesignASCE 7-10 Ss=0.00 g, S1=0.00 g, SOIL=D, Importance Factor I=1.25
MaterialInner TankOuter Tank
Shell PlateA553-TYPE1A553-TYPE1
Annular PlateA553-TYPE1A553-TYPE1
Bottom PlateA553-TYPE1A553-TYPE1
RoofTypeSuspended DeckDome Roof
PlateA36
StructureA36
Wind Stiffener-A36
Compression Ring-A36
Corrosion AllowanceInner TankOuter Tank
Shell Plate 0.00mm0.000in1.50mm0.059in
Annular Plate 0.00mm0.000in1.50mm0.059in
Bottom Plate 0.00mm0.000in1.50mm0.059in
Suspended Deck0.00mm0.000in
Roof Plate 0.00mm0.000in
Roof Structure0.75mm0.030in



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[AAA1] [AAA2] 
Doc. No. : [AAA3]Rev. No.[AAA4] 
2.TANK CAPACITY CALCULATION
   
2.1) SKETCH DRAWING
 
   
A. Design specification
  Design Specific Gravity & DensitySG =0.581¥ñ =581kg/m³
Tank inside diameterDi =46000mm150.919ft
Height from bottom to top Ht =28060mm92.060ft
Critical High liquid levelCHLL =26900mm88.255ft
High high liquid levelHHLL =26900mm88.255ft
High liquid levelHLL =26550mm87.106ft
Low liquid levelLLL =2450mm8.038ft
Net Working Height ( Hnet = HLL - LLL ) Hnet =24100mm79.068ft
 
B. Nominal Capacity
Vno = p * Di©÷/ 4 * HtVno =46633.0m©ø27093.8Ton
D. Storage Capacity
Vsto = p * Di©÷/ 4 * HLLVsto =44705.2m©ø25973.7Ton
C. Net working Capacity
Vnet = p * Di©÷/ 4 * HnetVnet =40633.5m©ø23608.1Ton
E. Vapor Space Volume (m©ø) and Vapor Space Ratio (%)
Vapor = Vnom - VstoVapor =1927.8m©ø4.1 %


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API Àû¿ëÄÚµå : cboAPI.ListIndex = [0] API 620 12 Edition

API Àû¿ëÄÚµå : API 620 Annex_Q_OR_R = [ R ]

¹øÈ£Inner TankOuter TankDescription
0API 620 12th Edition Annex RDesign Code
1LPGContent Name
20.581Content Specific Gravity
346633.056096.3Storage Capacity
40.2External Pressure(kPa)
5Suspended DeckDome RoofType of Roof
64600048000Tank Inside Diameter
72806031000Tank Height
82690025168Design Liquid Level
92655025168Max. Liquid Level
1024502450Min. Liquid Level
114140043200Roof Radius
12015.0Deaign Pressure(kPa)
1308.6Operating Pressure(kPa)
14-4565Design Temperature
15-4540Operating Temperature
162690022826Hydrostatic Test Level
1700Pneumatic Test Pressure
180.05Max. Boil-off Rate
1934Design Wind Speed
20ASCE 7-10Seismic Coefficient
211.41(Roof) Dead Load
221.20(Roof) Live Load
230(Roof) Snow Load
24Material
25A553-TYPE1A553-TYPE1Shell Plate
26A553-TYPE1A553-TYPE1Annular Plate
27A553-TYPE1A553-TYPE1Bottom Plate
28Suspended DeckDome RoofSD:Single Deme, DD:Double Deme
29A36Roof Plate
30A36Roof Structure
31-A36Shell Stiffener
32-A36Compression Ring
33BLANKBLANKJoint Efficiency
341.001.00Shell Plate
351.000.7Roof Plate
361.00Compression Ring
370.35Bottom Plate
381.01.0Annular Plate

k°¢ºÎ¸íĪ S(k)¹øÈ£Inner TankOuter Tank
k°¢ºÎ¸íĪ S(k)¹øÈ£thk imt(k)CA tt(i)Wt(kg) tt(i+1)thk omt(k)CA tt(i+2)Wt(kg) tt(i+3)
k=0Shelli= 0imt(0) = 22.000.00987.62omt(0) = 20.001.50853.93
k=1Annulari= 4imt(1) = 12.000.0011.27omt(1) = 12.001.5066.23
k=2Bottomi= 8imt(2) = 8.000.00160.31omt(2) = 8.001.50190.18
k=3Roof Decki= 12imt(3) = 0.000.00omt(3) = 6.000.000.00
k=4Roof Platei= 16imt(4) = 5.000.000.00omt(4) = 7.000.00108.59
k=5Roof Strui= 20imt(5) = 0.000.00omt(5) = 0.7555.98
k=6Shell Stiffi= 24imt(6) = 11.36omt(6) = 0.005.27
k=7Comp Ring.i= 28imt(7) = omt(7) = 44.001.5045.77



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[AAA1] [AAA2] 
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3.1) Shell plate thickness at design condition Material :[A553-TYPE1]
    Diameter of tank inside D =46000mm46.000m1811.024in
Height of tank Ht =28060mm28.060m1104.724in
Design liquid level for shell th'k. calc. DLL =26900mm26.900m88.255ft
High liquid level HLL =26550mm26.550m87.106ft
Corrosion allowanceC.A =0.000mm0.000in
Design specific gravityG =0.581¥ñ=581.0kg/m©ø36.271lb/ft©ø
Tank radius, Rc = D / 2Rc =23000.0mm23.000m905.512in
Joint efficiency of Shell WeldE =1.000
Minimum Tensile strengthFu =689.476MpaFu=100000psi
Minimum Yield strengthFy =399.896MpaFy=58000psi
Allowable Stress for Design ConditionSts =229.823MpaSts=33333psi
  Sts = Min( Fu * 0.3, Fy * 0.6)
Design internal pressurePg =0.000mbar0.000psi
Liquid head pressure, PL = G * HLPL =See Below 3.1.1 Table(a)
Total pressure, P = Pg + PLP =See Below 3.1.1 Table(a)
¡¡ ¡¡For cylindrical sidewalls of a vertical tank : as per API 620 5.10.2.5 c) Eqn. (10)(11),
T2 = P x RcT1 = Meridional (Longitudinal) unit force. (lb/in)
T2 : Latitudinal (Circumferential) unit force. (lb/in)
Required shell thickness calculation : as per API 620 5.10.3.2 Eqn. (16),
td =
T2
¡¡Sts ¡¿ E  
£« CA
td : Design thickness of shell. (mm)
tu : Used (Selected) thickness of shell. (mm)

3.1.1) Inner Tank Shell Plate Thickness Calculation (Design Condition)
Shell WidthHTPL (design)PT2t2UsedThkWeightWtrEN 14620-2
Thickness (mm)
No.mmmmmmWTRinWTRpsilb/ininchmmmmTonmmeettMin
83360280602840111.8112.3472125.240.0641.62612.045.8133601.2411.6848.0
73450247006200244.0945.1244639.840.1393.53112.047.03734502.8843.9128.0
63450212509650379.9217.9757221.460.2175.51212.047.03734504.576.28.0
534501780013100515.74810.8269803.070.2947.46812.047.03734506.2568.4888.0
434501435016550651.57513.67712384.690.3729.44914.054.87923477.94310.77611.0
334501090020000787.40216.52814966.30.44911.40516.062.72216819.62913.06313.0
23450745023450923.22819.37917547.920.52613.3618.070.565125211.31515.35115.0
140004000269001059.05522.2320129.530.60415.34221.095.45798713.00117.63918.0
0280600269001059.055000014.8470.54419977END


S-Tank Engineering
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[AAA1] [AAA2] 
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3.2) Shell plate thickness at Hydrostatic-Test condition Material :A553-TYPE1
    Diameter of tank inside D =46000mm46.000m1811.024in
Height of tank Ht =28060mm28.060m1104.724in
Design liquid levelDLL =26900mm26.900m88.255ft
Hydro test level, HTL = DLL*1.25*G HTL =26900mm26.900m88.255ft
Tank radius, Rc = D / 2Rc =23000.0mm23.000m905.512in
Joint efficiency of Shell WeldingE =1.000
Test Water Specific GravityG =1.000¥ñ=1000.0kg/m©ø62.428lb/ft©ø
Minimum Tensile strengthFu =689.476MpaFu=100000psi
Minimum Yield strengthFy =399.896MpaFy=58000psi
Allowable Stress for Test ConditionSts =339.912MpaSts=49300psi
  Sts = Min(0.55Fu, 0.75Fy), Annex Q.6.1.2
Pnematic test pressure, Pt=1.25 x PgPt =0.000mbar0.000psi
Liquid head pressure, PL = G * HLPL =See Below 3.1.1 Table(a)
Total pressure, P = Pt + PLP =See Below 3.1.1 Table(a)
¡¡ ¡¡For cylindrical sidewalls of a vertical tank : as per API 620 5.10.2.5 c) Eqn. (10)(11),
¡¡¡¡T2 = P x Rc T1 = Meridional (Longitudinal) unit force. (lb/in)
T2 : Latitudinal (Circumferential) unit force. (lb/in)
Required shell thickness calculation : as per API 620 5.10.3.2 Eqn. (16),
¡¡¡¡tt = T2 / (Sts x E)td : tt : Hydrostatic test thickness of shell. (mm)
tu : Used (Selected) thickness of shell. (mm)

3.2.1) Inner Tank Shell Plate Thickness Calculation (Hydrostatic Test Condition)
Shell WidthHTPL (hydro)PT2t2UsedThk
td
WeightWtr
No.mmmmmmWTRinWTRpsilb/ininchmmmmTonmm
83360280602840111.8114.0393657.360.0741.8812.045.813360
73450247006200244.0948.8187984.80.1624.11512.047.0373450
63450212509650379.92113.72612429.060.2526.40112.047.0373450
534501780013100515.74818.63316872.410.3428.68712.047.0373450
434501435016550651.57523.5421315.750.43210.97314.054.8792347
334501090020000787.40228.44725759.10.52213.25916.062.7221681
23450745023450923.22833.35430202.450.61315.5718.070.5651252
140004000269001059.05538.26134645.790.70317.85621.095.457987
0280600269001059.055000014.8470.54419977

3.1.1) Inner Tank : Pg = 0 psi
No.Shell HeightDesign ConditionHydrostatic ConditionDesignHydroMin.ThkUsed.ThkShell
WHTLiquid Head(PL)PWT1T2Stst1t2Water LevelPWT1T2Stst1t2t1t2t1t2tMinUsedThkWeightºÎÁ·µÎ²²Wtr
(mm)(mm)(mmWTR)(inWTR)(psi)(lb)(lb/in)(lb/in)(psi)(inch)(inch) (mm)(inch)(psi)(lb)(lb/in)(lb/in)(psi)(inch)(inch)(mm)(mm)(mm)(mm)(mm)(mm)(Ton)(mm)(mm)
012345678910111213141516171819202122232425262728
83360280602840111.8112.34760455270.0422125.243333300.0642840111.8114.0391040538203657.364930000.07401.62601.887.9381245.814.0623360
73450247006200244.0945.124131979810.2134639.843333300.1396200244.0948.8182271597507984.84930000.16203.53104.1157.9381247.0374.0623450
63450212509650379.9217.975205420190.2157221.463333300.2179650379.92113.726353563150.21912429.064930000.25205.51206.4017.9381247.0374.0623450
534501780013100515.74810.826278860570.2179803.073333300.29413100515.74818.633479966560.19616872.414930000.34207.46808.6877.9381247.0373.3133450
434501435016550651.57513.677352300950.21812384.693333300.37216550651.57523.54606369970.17321315.754930000.43209.449010.9737.9381454.8793.0272347
334501090020000787.40216.528425741330.2214966.33333300.44920000787.40228.447732773370.1525759.14930000.522011.405013.2597.9381662.7222.7411681
23450745023450923.22819.379499181710.22217547.923333300.52623450923.22833.354859176780.12730202.454930000.613013.36015.577.9381870.5652.431252
140004000269001059.05522.23572622090.22320129.533333300.604269001059.05538.261985580190.10534645.794930000.703015.342017.8567.9382195.4573.144987
0280600269001059.0550000000269001059.05500000000000014.782470.544019977

3.1.2) Outer Tank : Pg = 2.1756 psi
No.Shell HeightDesign ConditionHydrostatic ConditionDesignHydroMin.ThkUsed.ThkShell
WHTLiquid Head(PL)PWT1T2Stst1t2Water LevelPWT1T2Stst1t2t1t2t1t2tMinUsedThkWeightºÎÁ·µÎ²²Wtr
(mm)(mm)(mmWTR)(inWTR)(psi)(lb)(lb/in)(lb/in)(psi)(inch)(inch) (mm)(inch)(psi)(lb)(lb/in)(lb/in)(psi)(inch)(inch)(mm)(mm)(mm)(mm)(mm)(mm)(Ton)(mm)(mm)
012345678910111213141516171819202122232425262728
1090031000002.1760931.4162056.06333330.0870.121002.7201188.4242570.08493000.0240.0522.213.0730.611.3217.9383537.3627.06229
9300030100002.1760931.4162056.06333330.0870.121002.7201188.4242570.08493000.0240.0522.213.0730.611.3217.9381035.572.0623000
8330027100206881.4173.8854793284931.4413670.87333330.0870.169002.7201188.4242570.08493000.0240.0522.214.2930.611.3217.9381039.122.0623300
73300238005368211.3396.61212442141931.4226247.56333330.0870.2463026119.1347.023120718941187.9596635.91493000.0240.1352.216.2480.613.4297.9381039.122.0623300
63300205008668341.269.33920090999931.4028824.25333330.0870.3246326249.05511.717252368811188.111071.18493000.0240.2252.218.230.615.7157.9381039.121.773300
533001720011968471.18112.06627739856931.38311400.95333330.0870.4019626378.97616.411384018681188.2415506.46493000.0240.3152.2110.1850.618.0017.9381246.951.8151946
433001390015268601.10214.79335388714931.36313977.64333330.0870.47812926508.89821.105515668551188.3819941.73493000.0240.4042.2112.1410.6110.2627.9381558.692.8591038
333001060018568731.02417.5243037571931.34416554.33333330.0870.55616226638.81925.798647318421188.04824376.07493000.0240.4942.2114.1220.6112.5487.9381766.522.878735
23300730021868860.94520.24750686429931.32419131.03333330.0870.63319526768.7430.492778968291188.18928811.34493000.0240.5842.2116.0780.6114.8347.9381974.352.922543
14000400025168990.86622.97458335286931.30521707.72333330.0870.7122826898.66135.186910618161188.32933246.62493000.0240.6742.2118.0340.6117.127.9382094.861.966572
031000025168990.866000000022826898.66100000000000014.49531.66017763


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[AAA1] [AAA2] 
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5. [INNER TANK] Top Girder calculation

Refer to Guide to STORAGE TANK & EQUIPMENT
The David Taylor model basin Formula is used to decide upon the pitching of the stiffeners on the tank shell.
This is taken from the work of Windenburg and Trilling (Reference 18.4), some of which is based on test work
carried out on behalf of the US Navy as far back as 1929.

¡¡5-1) The number of stiffeners required to stabilise the shell is given by : (equ. 18. 11)

¡¡¡¡Ns = (He / Ls) - 1 = (19977 / 5664) - 1 = 2.53,¡¡Ns¡¡= 3 EA

¡¡5-2) Total height of equivalent tank shell ( He = ¥ÒWtr ) (equ. 18. 10) TABLE 5.1
   
No.(Unit : mm)
tnWtuniformtactualWtr
812.0336012.012.03360
712.0345012.012.03450
612.0345012.012.03450
512.0345012.012.03450
414.0345012.014.02347
316.0345012.016.01681
218.0345012.018.01252
121.0400012.021.0987
He = ¥ÒWtr = Wtr1 + .. + Wtr8 =19977
 
   
5-2) The maximum height of unstiffened side wall (Ls) (equ. 18. 10)
Ls =222.992in5664.0mm
Where,
p = External pressure or Insulation pressure from annular space p =0.3556psi250Mpa
¡¡¡¡¡¡¡¡¡¡(Min. value of STE's standard)p = 0.00245kg/m²
D = Inner tank diameter D =1811.024in46000mm
F = Factor of safety F = 2.0
E = Modulus of elasticity of (A553-TYPE1) E =28862502psi199000Mpa
tmin= Thickness of the thinnest (top) shell course m =0.4724in 12.000mm
¥ô = Poisson's ratio ¥ô = 0.3
C.A = Corrosion Allowance CA =0.0000in0.000mm
 
Shell
No.
Stiff
Loc. Level
(mm)
Between
Location
L (mm)
Stiff ºÎÂøÀ§Ä¡(U+B=W)
to WELD(mm)
Top Angle
(Stiff Size)
Section
Area
(cm²)
Unit Weight
(kg/m)
Length
(m)
Weight
(Ton)
Ireqd < Iact
(cm©ù)
Areqd < Aact
(cm²)
8¡å27860200200(U)+ 3160(B)= 3360BL12x190x10034.8027.32145.33970.07010.00 < 7915.180.00 < 80.88
7¡å2307047901630(U)+ 1820(B)= 3450FB12 x 18021.6016.96145.22463.02793.00 < 2852.5830.00 < 67.68
6¡å1807050003180(U)+ 270(B)= 3450FB12 x 18021.6016.96145.22463.02793.00 < 2852.5830.00 < 67.68
4¡å1248055901870(U)+ 1580(B)= 3450FB12 x 18021.6016.96145.22463.02793.00 < 2960.4330.00 < 84.32
Top Girder & Stiff Weight : 11359.0kg

5-3) The number of stiffeners required to stabilise the shell is given by : (equ. 18. 11)

¡¡¡¡Ns = ( He / Ls) - 1 = (19977 / 5664) - 1 = 2.53,¡¡Ns¡¡= 3 EA


Where,
   5-4) Required inertia moment (equ. 18. 13) & Minimum required area (equ. 18. 14)
N=Buckling waves number (min. N = 2, Max. N = 10) N =6.55
p=External pressure or Insulation pressure from annular spacep =0.3553psi0.00245Mpa
¡¡¡¡(Min. value of STE's technical standard)p =250kg/m²
D=Inner tank diameterD =1614.2in41000mm
H=Inner tank heightH =990.2 in25150mm
F=Factor of safety F =2.0
E=Modulus of elasticityE =2.799E+07psi193000Mpa
TavAverage thickness of inner shell platetavg =0.43in10.82mm
Fa=Allowable compressive stress (lb/in2)Fa =15000psi103.42Mpa
CA=Corrosion allowance (mm)CA =0.03in0.80mm

5-5) Inner stiffener size &required section moment
C1=Neutral axis of combined section.12345
Iact =Actual moment of inertia of section.12345
Ireqd =Required moment of inertia of section.12345
La=Actual height of the tank associated with the particular stiffener12345
(Acutal distance of stiffener & stiffener or stiffener & top shell)12345
a=Web plate length (mm) 12345
b=Web plate thickness - CA (mm)12345
t=Corroded shell thickness where stiffener is located12345


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11. Intermediate Wind Girder Calculation
11-1) [Outer TANK] Wind Girder (Stiffener) calculation
   
No.(Unit : mm)
tnWtactualtuniformWtr
1035.09008.533.529.0
910.030008.58.53000.0
810.033008.58.53300.0
710.033008.58.53300.0
610.033008.58.53300.0
512.033008.510.51946.0
415.033008.513.51038.0
317.033008.515.5735.0
219.033008.517.5543.0
120.040008.518.5572.0
HTR =¥ÒWtr = Wtr1 + .. + Wtr10 =17763.0
 
11-2) Maximum unstiffened shell height (H1, Hsafe)
¡¡

¡¡¡¡ Lmin = MYMIN(H1, Hsafe) = Min( 14924, 11515 ) = 11515 (mm)

11-3) The number of stiffeners required to stabilise the shell is given by : (equ. 18. 11)

¡¡¡¡Nstiff = ( HTR / Lmin ) - 1 = (17763 / 11515) - 1 = 0.54,¡¡Nstiff¡¡= 1 EA


 
Shell
No.
Stiff
Loc. Level
(mm)
Between
Location
L (mm)
Stiff ºÎÂøÀ§Ä¡(U+B=W)
to WELD(mm)
Top Angle
(Stiff Size)
Section
Area
(cm²)
Unit Weight
(kg/m)
Length
(m)
Weight
(Ton)
Ireq < Iact
(cm©ù)
Zreq< Zact
(cm©ø)
Areq < Aact
(cm©ù)
Arstiff < Aastiff
(cm²)
7¡å2124097602560(U)+ 890(B)= 3450[BL]280x160x104300.0034.54152.65271.0522.7 < 570.52265 < 91172507 < 66121254 < 4300
Wind Stiff. Weight : 5271.0kg



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4. [INNER TANK] Bottom plate and Annular plate of calculation
   
4.1) Bottom plate (API 620 SEC. 5.9.4.2)
 1) Material of bottom plateMATL :A553-TYPE1
¡¡Bottom plate corrosion allowanceCA =0.0000inch0.00mm
Min. thickness: (API 620 SEC. 5.9.4.2 [1/4 inch])tbm =0.1875inch4.76mm
 
2) Required bottom plate thickness tbm+CA =0.188inch4.76mm
Used thickness of bottom plate tb_used =0.315inch8.00mm
4.2) Annular plate
1) Design condition
Annular plate material MATL :A553-TYPE1
 Design specific gravity of liquid contentGp =0.581p = 581.0kg/m©ø
 Annular plate corrosion allowanceCA =0.000inch0.00mm
Diameter of tank inside D =150.919ft46.000m
Nominal thickness for 1st shell course t =0.827inch21.00mm
Design liquid level Hd =88.255ft26.900m
2) Annular plate thickness
Minimum annular plate thickness, tb_min= 0.312(in)+ CAtb_min =0.312inch8.00mm
Used thickness of annular plate tb =0.472inch12.00mm
3) Design Stress in First Shell Course, Sd (psi)
        Sd =24336psi167.79MPa
as per API 620 Table Q-4A Minimum Thickness for the Annular Bottom Plate: Steel Tanks, inch (mm)
Nominal Thickness of First Shell Course
t, inch (mm)
Design Stress in First Shell Course, Sd (psi)
¡Â 20,000 ¡Â 22,000 ¡Â 24,000 ¡Â 26,000
t ¡Â 0.75
( t ¡Â 19.05 )
1/4
(6.35)
1/4
(6.35)
1/4
(6.35)
1/4
(6.35)
t ¡Â 1.00
( t ¡Â 25.40 )
1/4
(6.35)
1/4
(6.35)
1/4
(6.35)
5/16
(7.94)
t ¡Â 1.25
( t ¡Â 31.75 )
1/4
(6.35)
1/4
(6.35)
5/16
(7.94)
3/18
(9.53)
t ¡Â 1.50
( t ¡Â 38,10 )
1/4
(6.35)
9/32
(7.14)
3/8
(9.53)
7/16
(11.11)


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4) Width of annular plate (API 620 R.3.5.1 and API 650 Annex E.6.2.1.1.2)
¡¡ ¡¡Used annular plate thicknesstb =8.0mm0.315inch
¡¡ ¡¡Design liquid level plus internal pressure headH = Hd =26900mm88.255ft
¡¡ ¡¡Design specific gravity of liquidG =0.5810¥ñ=581.0kg/m©ø
4-1) Min. annular plate width
¡¡ ¡¡w = 390 · tb / (H · Gp)0.5 (inch)
¡¡ ¡¡(w : width between the inside of the shell and any lap welded joint
¡¡ ¡¡ in the reminder of the bottom)
w =653.0mm25.707inch
4-2) Min. required annular plate width due to seismicwSei =[#wSei_mm]mm[#wSei_in]inch
¡¡ ¡¡Min. radial width due to seismic (API 650 Annex E.6.2.1.1.2-1a) (Refer to Calculation 8.2.7)
4-3) Annular plate width : wDes = Max. (w, wSei, 610) [mm] =[#wSei_mm]mm[#wSei_in]inch
4-4) Min. annular plate width Lmin = (Wo+t1+wDes+Ov)Lmin =806.0mm652.958inch
4-5) Used annular plate widthL =[#wSei_mm]mm[#wSei_in]inch
 
5) Dimensions for annular plate (unit: mm)
¡¡¡¡ ¡¡
L =AAAmm
Di =AAAmm
Wo =AAAmm
t =AAAmm
Aid =AAAmm
Aod =AAAmm
Qv =AAAmm
¡¡ ¡¡Weight of Bottom Platewt_bott =AAAkgBBBN
¡¡ ¡¡Weight of Annular Platewt_annu =AAAkgBBBN


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[AAA1] [AAA2] 
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4. [OUTER TANK] Bottom plate and Annular plate of calculation
   
4.1) Bottom plate (API 620 SEC. 5.9.4.2)
 1) Material of bottom plateMATL :A553-TYPE1
¡¡Bottom plate corrosion allowanceCA =0.0591inch1.50mm
Min. thickness: (API 620 SEC. 5.9.4.2 [1/4 inch])tbm =0.1875inch4.76mm
 
2) Required bottom plate thickness tbm+CA =0.247inch6.26mm
Used thickness of bottom plate tb_used =0.315inch8.00mm
4.2) Annular plate
1) Design condition
Annular plate material MATL :A553-TYPE1
 Design specific gravity of liquid contentGp =0.581p = 581.0kg/m©ø
 Annular plate corrosion allowanceCA =0.059inch1.50mm
Diameter of tank inside D =157.480ft48.000m
Nominal thickness for 1st shell course t =0.787inch20.00mm
Design liquid level Hd =82.572ft25.168m
2) Annular plate thickness
Minimum annular plate thickness, tb_min= 0.312(in)+ CAtb_min =0.371inch9.50mm
Used thickness of annular plate tb =0.472inch12.00mm
3) Design Stress in First Shell Course, Sd (psi)
        Sd =26969psi185.95MPa
as per API 620 Table Q-4A Minimum Thickness for the Annular Bottom Plate: Steel Tanks, inch (mm)
Nominal Thickness of First Shell Course
t, inch (mm)
Design Stress in First Shell Course, Sd (psi)
¡Â 20,000 ¡Â 22,000 ¡Â 24,000 ¡Â 26,000
t ¡Â 0.75
( t ¡Â 19.05 )
1/4
(6.35)
1/4
(6.35)
1/4
(6.35)
1/4
(6.35)
t ¡Â 1.00
( t ¡Â 25.40 )
1/4
(6.35)
1/4
(6.35)
1/4
(6.35)
5/16
(7.94)
t ¡Â 1.25
( t ¡Â 31.75 )
1/4
(6.35)
1/4
(6.35)
5/16
(7.94)
3/18
(9.53)
t ¡Â 1.50
( t ¡Â 38,10 )
1/4
(6.35)
9/32
(7.14)
3/8
(9.53)
7/16
(11.11)


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4) Width of annular plate (API 620 R.3.5.1 and API 650 Annex E.6.2.1.1.2)
¡¡ ¡¡Used annular plate thicknesstb =8.0mm0.315inch
¡¡ ¡¡Design liquid level plus internal pressure headH = Hd =26900mm88.255ft
¡¡ ¡¡Design specific gravity of liquidG =0.5810¥ñ=581.0kg/m©ø
4-1) Min. annular plate width
¡¡ ¡¡w = 390 · tb / (H · Gp)0.5 (inch)
¡¡ ¡¡(w : width between the inside of the shell and any lap welded joint
¡¡ ¡¡ in the reminder of the bottom)
w =675.1mm26.577inch
4-2) Min. required annular plate width due to seismicwSei =[#wSei_mm]mm[#wSei_in]inch
¡¡ ¡¡Min. radial width due to seismic (API 650 Annex E.6.2.1.1.2-1a) (Refer to Calculation 8.2.7)
4-3) Annular plate width : wDes = Max. (w, wSei, 610) [mm] =[#wSei_mm]mm[#wSei_in]inch
4-4) Min. annular plate width Lmin = (Wo+t1+wDes+Ov)Lmin =1861.0mm675.056inch
4-5) Used annular plate widthL =[#wSei_mm]mm[#wSei_in]inch
 
5) Dimensions for annular plate (unit: mm)
¡¡¡¡ ¡¡
L =AAAmm
Di =AAAmm
Wo =AAAmm
t =AAAmm
Aid =AAAmm
Aod =AAAmm
Qv =AAAmm
¡¡ ¡¡Weight of Bottom Platewt_bott =AAAkgBBBN
¡¡ ¡¡Weight of Annular Platewt_annu =AAAkgBBBN


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A&#192;&Agrave;Capital A, grave accent
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A&#195;&Atilde;Capital A, tilde
A&#196;&Auml;Capital A, dieresis or umlaut mark
A&#197;&Aring;Capital A, ring (Angstrom)
¨¡&#198;&AElig;Capital AE diphthong (ligature)
C&#199;&Ccedil;Capital C, cedilla
E&#200;&Egrave;Capital E, grave accent
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¨¢&#208;&ETH;Capital Eth, Icelandic
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O&#210;&Ograve;Capital O, grave accent
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¡¿&#215;&times;Multiply sign
¨ª&#216;&Oslash;width=130 Capital O, slash
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U&#220;&Uuml;Capital U, dieresis or umlaut mark
Y&#221;&Yacute;Capital Y, acute accent
¨­&#222;&THORN;Capital Thorn, Icelandic
©¬&#223;&szlig;Small sharp s, German (sz ligature)
a&#224;&agrave;Small a, grave accent
a&#225;&aacute;Small a, acute accent
a&#226;&acirc;Small a, circumflex accent
a&#227;&atilde;Small a, tilde
a&#228;&auml;Small a, dieresis or umlaut mark
a&#229;&aring;Small a, ring
©¡&#230;&aelig;Small ae diphthong (ligature)
c&#231;&ccedil;Small c, cedilla
e&#232;&egrave;Small e, grave accent
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o&#242;&ograve;Small o, grave accent
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¡À&#247;&divide;Division sign
©ª&#248;&oslash;Small o, slash
u&#249;&ugrave;Small u, grave accent
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y&#253;&yacute;Small y, acute accent
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10. INSULATION WEIGHT
¹øÈ£012345678
No.Insualtion
Location
MaterialThickness
t x H(mm)
ID
(m)
OD
(m)
Insulation Area
(m²)
Density
(kg/m©ø)
Weight
(kg)
TOTAL WEIGHT
(Ton)
¨çTANK
BOTTOM
"A"
DRY SAND (TOP)t 5046.0001661.91520.0126,305
¨èFORM GLASS (MID)t 45046.0001661.9120.089,743
¨éDRY SAND (BTM)t 10046.0001661.91520.0252,609468.7
¨êTANK
BOTTOM
"B"
PCB (TOP)t 5044.80046.600129.21200.07,753
¨ëLEVEL CONCRETEt 45044.80046.600129.21200.069,77677.5
¨ìTANK
BOTTOM
"C"
DRY SAND (TOP)t 5046.60048.000104.01520.07,905
¨íFORM GLASS (MID)t 45046.60048.000104.0120.05,617
¨îDRY SAND (BTM)t 10046.60048.000104.01520.015,81129.3
¨ðSUSPENDED
DECK
FIBER_GLASSt 60046.6001705.524.024,56024.6
¨ñANNULAR
SPACE
PERLITE (TOP)t: 2500 x H:314043.00048.000357.455.061,715
¨òPERLITE (MIDDLE)t: 900 x H:2806046.20048.000133.255.0205,524
¨óRESILIENT_BLANKETt: 100 x H:2806046.00046.20014.517.57,112274.4
Total Insulation Weight (Ton) 874.5





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12. DOUBLE TANK THERMAL TRANSFER CALCULATION

¿øº»À§Ä¡ : D:/0000_SGP_LNG/SGP LNG BOG °è»ê Dia_61600_Rev_2_20190213_Á¶Çö¹ü.xlsm
STANK_LNG_THERMAL_TRANSFER_FORMULA_0.png



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13. DOUBLE TANK THERMAL TRANSFER CALCULATION

¿øº»À§Ä¡ : D:/0000_SGP_LNG/SGP LNG BOG °è»ê Dia_61600_Rev_2_20190213_Á¶Çö¹ü.xlsm
STANK_LNG_THERMAL_TRANSFER_FORMULA.png



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14. OMAN SALALAH AMMONIA TANK THERMAL ANALYSIS REPORT ( by ANSYS )

¿øº»À§Ä¡ : D:/2_ÇÁ·ÎÁ§Æ®/00_¿À¸¸_SALALAH/±â¼ú¿µ¾÷¼ÛºÎ/OMAN AMMONIA TANK ¿­Àü´Þ Çؼ®_±â¼ú¿¬±¸¼Ò_Àå´öÀÎ
STANK_THERMAL_TRANSFER_ANA1.png
STANK_THERMAL_TRANSFER_ANA_UPR.png
STANK_THERMAL_TRANSFER_ANA_BTM.png
STANK_THERMAL_TRANSFER_ANA2.png
STANK_THERMAL_TRANSFER_ANA0.png



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15. PC-WALL TYPE LNG THERMAL ANALYSIS REPORT ( by ANSYS )

¿øº»À§Ä¡ : D:/0000_SGP_LNG/SGP LNG BOG °è»ê Dia_61600_Rev_2_20190213_Á¶Çö¹ü.xlsm
STANK_LNG_THERMAL_TRANSFER_CASE_A_55degC.png
STANK_LNG_THERMAL_TRANSFER_CASE_B_65degC.png
STANK_LNG_THERMAL_TRANSFER_CASE_B_75degC.png



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10. LOADING DATA

  1. TANK INSULATION MATERIAL AND DENSITY
¡¡
ZONE NO.LOCATIONINSULATION
MATERIAL
Thickness
T (mm)
Density
p (m©ø)
ZRSUSPENDED DECKFIBER GLASS30024.0
ZSSHELL
(ANNULAR SPACE)
RESILIENT BLANKET20017.5
PERLITE POWDER70055.0
P.U.F10045.0
ZBAINNER TANK
AREA "A"
DRY SAND (Upper)501520
FOAM GLASS (Middle)300120
DRY SAND (Lower)501520
ZBBINNER SHELL
BOTTOM "B"
LEVEL CONCRETE (v)1001200
PERLITE CONCRETE BLOCK (PCB)2501200
LEVEL CONCRETE (Lower)1001200


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  1. TANK DESIGN CONDITION
¡¡
1) Storage capacityVsto =10564m©ø (6,000 ton)
2) Design pr¥åssurePi =0.112kg/cm²G - -0.005 kg/cm²G
3) Max. design liquid levelDLL =23500 mm
4) Design density p =568 kglm©ø
5) Design temperatureT =-104~oC - Ambient
6) Seismic FactorCS = 0.148 (horizontal), 0.0 (vertical)
¡¡ ¡¡Refer to Doc.No.N4189-D-Ol
¡¡ ¡¡¡¡Calculation of Tank Main Components
7) Wind Design Wind Speed V =53 m/sec
¡¡ ¡¡Referto Doc.No. N4189-D-Ol
¡¡ ¡¡¡¡Calculation of Tank Main Components
8) Hydrostatic test level HTL =16685 mm
9) Pneumatic test Pressure PTest =0.14g/cm²G (1.25 x 0.112kg/cm 2G)
10) Dimension (mm)
¡¡¡¡¡¡¡¡DescriptionSymbolInner TankOuter TankUnit
Tank inside diameterDi =2400025000mm
Tank heightHT =2430026320mm
Roof radius (Rro=0.8*D)Rro =-20640mm
11) Insulation / Insulation Thickness
¡¡¡¡¡¡¡¡ Deck : Loose Perlite250mm
Shell : Fiberglass + Loose Perlite900mm
Bottom : Foamglass + Dry Sand + Concrete500mm


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4 CALCULATION OF LOADING
¡¡
4.1 Liquid Head Pressure : 1A
¡¡1A = UL x HI x 9.80665 x 10©ø
¡¡ ¡¡= 568 x 23.5 x 9.80665 x 10©ø = 130.9 kN/m²
¡¡Where
¡¡ ¡¡GL : Design density = 568 kg/m©ø
¡¡ ¡¡Hl : Max. design liquid level = 23.5 m
¡¡ ¡¡
4.2 lncreased Bottom Pressure Due to Seismic 1B
¡¡1) Impulsive pressure : P1
¡¡ ¡¡P1 = 0.01051 N/mm² = 10.51 kN/m²
¡¡2) Convective pressure : P2
¡¡ ¡¡P2 = 0.000 13N/mm² 0.13 kN/m²
¡¡3) Tota1 bottom pressure due to seismic : 1B
¡¡ ¡¡1B = Pl + P2 10.51 + 0.13 = 10.64 kN/m²
¡¡ ¡¡Above each values are calculated in accordance with "BASIS OF SEISMIC DESIGN
¡¡ ¡¡PROVISIONS FOR WELDED STEEL OIL STORAGE TANKS"
¡¡ ¡¡(by R.S.Wozniak and W.W.Mitchell)
¡¡ ¡¡
4.3 Water Head Pressure at Hydrostatic Test : 2A
¡¡2A = Gw x Hw x 9.80665 x 10-3
¡¡ ¡¡ = 1,000 x 16.685 x 9.80665 x 10©ø = 163.7 kN/m²
¡¡ Where
¡¡ ¡¡Gw : Density ofwater = 1,000 kg/m©ø
¡¡ ¡¡Hw : Hydrostatic test leve1 = 16.685 m
¡¡ ¡¡
4.4 Design Pressure : 3A
¡¡3A = 11.0 kN/m² (0.112 kg/cm²G)
¡¡ ¡¡
4.5 Line Load Due to 3A: 3B
¡¡3B = D²/ 4 x 3A = 25.814 x 11.0 = 71 kN/m (upward load)
¡¡ ¡¡
4.6 Pneumatic Test Pressure : 4 A
¡¡4A = 11.0 x 1.25 = 13.75 kN/m² (0.14 kg/cm²G)


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16. Weight Summary (INNER TANK)
¡¡
DESCRIPTIONWEIGHTMATERIAL / SIZE (Ư±â)No.
(ton)(kN)
1) Shell 1, 1
¡¡Shell plate470.54614.0 A553-TYPE1 t: 21 ~ 12 mm2, 2
¡¡Top girder and Interm. stiffener11.4111.8 A553-TYPE1 Q'TY : 4 RING 3, 5
¡¡Shell Nozzle (In Tank) Pipe & Att't10.199.0 È®ÀÎÇÊ¿ä(Áß¿ä)4, 6
¡¡Internal ladder supported by shell5.654.9 È®ÀÎÇÊ¿ä(Áß¿ä)5, 7
¡¡Stairway, platform, accessory5.654.9 È®ÀÎÇÊ¿ä(Áß¿ä)6, 8
¡¡External ladder11.2109.8 È®ÀÎÇÊ¿ä(Áß¿ä)7, 9
¡¡Internal ladder supported by shell10.199.0 È®ÀÎÇÊ¿ä(Áß¿ä)8, 10
¡¡Pipe & support For Cool Down Ring10.199.0 È®ÀÎÇÊ¿ä(Áß¿ä)9, 12
¡¡Anchor Strap and pad16.8164.8 È®ÀÎÇÊ¿ä(Áß¿ä)10, 14
¡¡Others5.654.9 È®ÀÎÇÊ¿ä(Áß¿ä)11, 15
Sub-Total557.05462.3 12, 20
2) Bottom 13, 21
¡¡Annular plate11.1108.9 A553-TYPE1 t12 x 806 mm14, 22
¡¡Bottom plate100.0980.7 A553-TYPE1 t8 x2438x9144 mm15, 23
¡¡Others4.544.1 È®ÀÎÇÊ¿ä(Áß¿ä)16, 26
Sub-Total115.61133.6 17, 30
[INNER TANK] EMPTY WEIGHT (1)6736,596 (1) 18, 61
¡¡[LOADING DATA]
19, 62
LIQUID CONTENTS WEIGHT (B)25,974254,715 Wco = Vsto(44705.2m©ø) x SG(0.581) 20, 63
TEST WATER WEIGHT (C)44,705438,408 Wtest = ¥ð*D²/4 * HTL(26.9m) 21, 64


S-Tank Engineering
TANK STRENGTH CALCULATION   Page   [$CP] / [$TP]
[AAA1] [AAA2] 
Doc. No. : [AAA3]Rev. No.[AAA4] 

16. Weight Summary (OUTER TANK)
¡¡
DESCRIPTIONWEIGHTMATERIAL / SIZE (Ư±â)No.
(ton)(kN)
1) Shell 1, 1
¡¡Shell Plate531.75214.2 A553-TYPE1 t:20~10mm, Top Shell:35.0 mm2, 2
¡¡Intermediate wind girder5.352.0 A553-TYPE1 3, 4
¡¡Shell Nozzle (In-Tank Pipe) & All Att't11.2109.8 È®ÀÎÇÊ¿ä(Áß¿ä)4, 5
¡¡Annular Space Stairway, platform, acc'y13.5132.4 È®ÀÎÇÊ¿ä(Áß¿ä)5, 6
¡¡Annular Space ladder4.544.1 È®ÀÎÇÊ¿ä(Áß¿ä)6, 7
¡¡Internal ladder supported by shell5.654.9 È®ÀÎÇÊ¿ä(Áß¿ä)7, 8
¡¡Water spray16.8164.8 È®ÀÎÇÊ¿ä(Áß¿ä)8, 9
¡¡External(internal) Pipe Support9.088.3 È®ÀÎÇÊ¿ä(Áß¿ä)9, 10
¡¡Roof handrail supported by shell2.221.6 È®ÀÎÇÊ¿ä(Áß¿ä)10, 11
¡¡Anchor strap or Anchor Bolts16.8164.8 È®ÀÎÇÊ¿ä(Áß¿ä)11, 12
¡¡Others5.654.9 È®ÀÎÇÊ¿ä(Áß¿ä)12, 13
Sub-Total622.26101.7 13, 20
2) Bottom 14, 21
¡¡Annular plate26.1256.0 A553-TYPE1 t12 x 1861 mm15, 22
¡¡Bottom plate99.5975.8 A553-TYPE1 t8 x2438x9144 mm16, 23
¡¡Cool Down Ring Pipe & support7.977.5 È®ÀÎÇÊ¿ä(Áß¿ä)17, 25
¡¡Pipe Support (+Annular Space)4.544.1 È®ÀÎÇÊ¿ä(Áß¿ä)18, 26
¡¡Others3.433.3 È®ÀÎÇÊ¿ä(Áß¿ä)19, 27
Sub-Total141.41386.7 20, 30
3) Roof 21, 31
¡¡Roof Plate 108.61065.0 A36 Used Thk: 7.0 mm22, 32
¡¡Roof Compression ring45.8449.1 A36 t38x W:1040x 147m23, 33
¡¡Roof Rafter & Girder56.0549.2 A36 24, 34
¡¡Hoist ring beam17.3169.7 A36 2 Ring Beam25, 35
¡¡Roof gauging platform & Acc'y 44.1432.5 È®ÀÎÇÊ¿ä(Áß¿ä)26, 36
¡¡Roof around P/F & walk way & Acc'y18.9185.3 È®ÀÎÇÊ¿ä(Áß¿ä)27, 37
¡¡Water spray system33.7330.5 È®ÀÎÇÊ¿ä(Áß¿ä)28, 38
¡¡Suspended deck (plate & beam) 28.0274.6 LTCS OR S.S (FRAMEÆ÷ÇÔ) 29, 39
¡¡Deck hanger rod and acc'y3.938.2 SS304 RB19 : ROUND BAR30, 40
¡¡Top disc., column base & clip39.3385.4 È®ÀÎÇÊ¿ä(Áß¿ä)31, 41
¡¡Roof Crane Structure
(For pump maintenance)
2.221.6 È®ÀÎÇÊ¿ä(Áß¿ä)32, 42
¡¡Roof nozzle and dipped pipe33.7330.5 È®ÀÎÇÊ¿ä(Áß¿ä)33, 43
Sub-Total431.54231.6 34, 50
4) Shell & Bottom & Roof insulation 35, 51
¡¡Shell side ( Annular Space )0.11.0 È®ÀÎÇÊ¿ä(Áß¿ä)36, 52
¡¡Bottom side0.11.0 È®ÀÎÇÊ¿ä(Áß¿ä)37, 53
¡¡Roof side0.11.0 È®ÀÎÇÊ¿ä(Áß¿ä)38, 54
Sub-Total0.32.9 39, 60
[OUTER TANK] EMPTY WEIGHT (2)1,19511,723 40, 61
¡¡[LOADING DATA]
[INNER/OUTER TANK] EMPTY WEIGHT (A)1,86818,319 (A)=(1)+(2) 41, 62
LIQUID CONTENTS WEIGHT (B)25,974254,715 Wco = Vsto(44705.2m©ø) x SG(0.581) 42, 63
TEST WATER WEIGHT (C)44,705438,408 Wtest = ¥ð*D²/4 * HTL(26.9m) 43, 64
OPERATING WEIGHT (D)27,842273,034 (D)=(A)+(B) 44, 65
HYDROSTATIC-TEST WEIGHT (E)46,573456,727 (E)=(A)+(C) 45, 66
[$PAGE_HEADER]
ROOF STRUCTURE CALCULATION
1. SKETCH DRAWING






Tank Dia. D = 48000mm
Tank Roof Radius Dr = 43200mm
Tank Sectional Area SArea = 1809.557m§³
Tank ROOF TOTAL WEIGHTWtotal = 259600kg259600kN
Dead Load (DL = Wtotal / SArea )DL = 143.5kg/§³1.41kPa
Live Load Lr = 122.4kg/§³1.2kPa
Snow Load S = 0.0kg/§³0kPa
External Load Pe = 20.4kg/§³0.2kPa
Roof Structure Design Load,
Wr = Max[DL+Pv+0.4*Max(Lr, Sn), DL+0.4*Pv+Max(Lr,Sn)] x 5% Up
Wr = 288.0kPa2.824kPa




S-Tank Engineering
[$DOCUMENT_TITLE]   Page   [$CP] / [$TP]
[AAA1] [AAA2] 
Doc. No. : [AAA3]Rev. No.[AAA4] 
1. ALLOWABLE STRESS
2. RAFTER CALCULATION


No.QTYR1R2Ld(R2-R1)HrXYKAngle
EAcmcmcmcmcmcmcm©÷deg.
#1 30450.0970.26520.2686.9291.440.5931553125.979
#2 60970.31476.05505.79149.6269.371.28512958912.979
#3 601476.11959.84483.79210.1251.2100.33683926019.979
#4 601959.82400.00440.16257.9223.6122.24813887726.979

No.WfPuQuVHfVxMfF
kgkg/cmkg/cmkgkgkgkg-cmkg
#1 610.732.7143.1382839.199516.201657.76-682159659.51
#2 1419.602.9261.5253285.447735.242316.87-532008074.76
#3 3285.444.4521.4595792.0410313.364498.71-6108711251.84
#4 5792.045.9111.3278685.8812273.147188.79-5206114223.52

No.MarkSIZE AIe1e2rQ'tyLengthUwtWeight
cm©÷cm©ùcmcmcmEAcmkgkg
#1MainH194X150X6X9 31.922289.639.638.35830527.7930.64845.1
#2MainH194X150X6X9 31.922289.639.638.35830527.7930.64845.1
SubH194X150X6X9 31.922289.639.638.35830527.7930.64845.1
#3MainH194X150X6X9 31.922289.639.638.35830527.7930.64845.1
SubH194X150X6X9 31.922289.639.638.35830527.7930.64845.1
#4MainH194X150X6X9 31.922289.639.638.35830510.4330.64685.8
SubH194X150X6X9 31.922289.639.638.35830510.4330.64685.8

No.MarkSIZE LnL/rFefcfbtfbcFcrFbtFbcSRc=SR©û=SR©ü=SR=
cm<300kg/cm©÷kg/cm©÷kg/cm©÷kg/cm©÷kg/cm©÷kg/cm©÷kg/cm©÷fc/Fcrfbt/Fbtfbc/FbcSRc+Max
(SR1,2)
#1MainH194X150X6X9 527.7963.145048.19302.94294.74-294.741228.721518.66599.320.250.190.490.74
SubH194X150X6X9 527.7963.145048.19302.94294.74-294.741228.721518.66599.320.250.190.490.74
#2MainH194X150X6X9 527.7963.145048.19253.24229.86-229.861228.721518.66599.320.210.150.380.59
SubH194X150X6X9 527.7963.145048.19253.24229.86-229.861228.721518.66599.320.210.150.380.59
#3MainH194X150X6X9 527.7963.145048.19352.88263.94-263.941228.721518.66599.320.290.170.440.73
SubH194X150X6X9 527.7963.145048.19352.88263.94-263.941228.721518.66599.320.290.170.440.73
#4MainH194X150X6X9 510.4361.075397.29446.08224.95-224.951245.511518.66619.700.360.150.360.72
SubH194X150X6X9 510.4361.075397.29446.08224.95-224.951245.511518.66619.700.360.150.360.72



3. RING GIRDER CALCULATION

No.SIZE AIe1e2rLnLengthUwtWeight
cm©÷cm©ùcmcmcmcmcmkgkg
#1L200x200x15 57.821805.4614.546.14494.22827.4345.31280.8
#2L200x200x25 93.834205.8614.146.040203.26096.3173.64486.9
#3L200x200x20 76.028205.6714.336.091309.19274.3059.75536.8
#4L250x250x25 119.469507.1017.907.629410.512314.0393.711538.2

No.AngleRrg¥á¥âHoHiMAoMBoMAiMBiTAoTBoTAiTBi
degcmradradkgkgkg-cm©÷kg-cm©÷kg-cmkg-cmkgkgkgkg
#112.000450.00.1050.0009516.20.074795-3741800452704552000
#26.000970.30.0520.1057735.29516.265507-32758-161267806787379973900-45270-45520
#36.0001476.10.0520.05210313.47735.2132870-66444-99656498359839598530-73799-73900
#46.0001959.80.0520.05212273.110313.4209944-104986-17642088222117093117253-98395-98530

No.M1M2T1T2fbofbifbofbi
kg-cm©÷kg-cm©÷kgkgkg/cm©÷kg/cm©÷kg/cm©÷kg/cm©÷
#174795-374184527045520187.33-498.86-93.72249.57
#2146185-1940252827928630250.48-604.40-332.45802.20
#3182705-1661002449524732367.35-928.43-333.97844.05
#4298166-2814061856218858304.60-767.94-287.48724.77

No.L/rFefaofaiFcrgfactFbcSRoSRi
<300kg/cm©÷kg/cm©÷kg/cm©÷kg/cm©÷ kg/cm©÷  
#115.3485540783.90788.221496.9762.831518.660.6470.855
#233.6417782301.64305.381427.9781.281518.660.3760.742
#350.757815322.31325.421323.49154.571518.660.4850.857
#453.806954155.46157.941301.46164.191518.660.3200.627

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