CONTENTS:-
SR. NO.
DESCRIPTION
1
DESIGN DATA
2
CALCULATIONS FOR MINIMUM SHELL THICKNESS
3
BOTTOM PLATE DESIGN
4
INTERMEDIATE WIND GIRDER
5
VERIFICATION OF UNSTIFFENED SHELL FOR EXTERNAL PRESSURE
6
DESIGN OF ROOF
7
CALCULATION OF ROOF STIFFENER
8
TANK STABILITY AGAINST UPLIFT DUE TO INTERNAL PRESSURE
9
STABILITY OF TANK AGAINST WIND LOADS 9.1
RESISTANCE TO SLIDING
10
SEISMIC CALCULATION
11
ANCHORAGE FOR UPLIFT LOAD CASES
12
ANCHOR CHAIR CALCULATION
13
WEIGHT SUMMARY
14
FOUNDATION LOADING DATA
15
EVALUATION OF EXTERNAL LOADS ON TANK SHELL OPENINGS AS PER P.3 OF API 650, ADD. 4, 2005
16
VRV AND VENTING CALCULATIONS
(PENDING)
17
DESIGN OF LIFTING TRUNNION
(PENDING)
1)
DESIGN DATA
Design Code
API STANDARD 650 TENTH EDITION, NOVEMBER 1998 ADDENDUM 4, DECEMBER 2005 APPENDICES: J, M & S "Process Equipment Design"
Flat Roof Design
By Lloyd E. Brownell & Edwin H. Young Item No.
:
TK-66202
Description
:
EJECTORS HOT WALL
Material
SA 240 TYPE 316
Density of Contents
: Dc
=
980
Specific Gravity of Contents
G
=
0.980
Material's Yield Strength @ Design Temperature
Fym
=
166.67
Design Temperature
TDSN
=
130
o
Operating Temperature
TOPR
=
80
o
Design Internal Pressure
Pi
=
ATM
C kPa
High Liquid Level
Hl
=
1.600
m
(HLL)
Design Liquid Level
HL1
=
1.900
m
(As Per PIPVESTA002)
Allowable Design Stress @ Design Temperature
Sd
=
148.33
MPa
(Table S-2)
Allowable Hydrostatic Stress @ Ambient Temperature
St
=
186.00
MPa
(Table S-2)
Bottom
=
0
mm
Shell
=
0
mm
Roof
=
0
mm
Structure
=
0
mm degree (Flat Roof)
kg/m3 MPa
(As Per Table S-5)
C 0
Corrosion Allowance
Slope of Tank Roof
q
=
0
Inside Diameter of Tank
Di
=
1.800
m
Outside Diameter of Tank
Do
=
1.812
m
Nominal Tank Diameter = Di + Bottom Shell Thickness
D
=
1.806
m
Height of Tank
H
=
1.900
m
Wc
=
0.348
kN
Weight of Top Curb Angle Weight of Roof Attachments
(Assumed)
W ra
=
10
kN
(Nozzles, Insulation, Railing/Platform)
Weight of Shell Attachments
(Assumed)
W sa
=
14
kN
(Nozzles, Insulation, Ladder & Partition Plates)
V
=
155
kph
Modulus of Elasticity @ Design Temperature
E
=
Live Load on Roof
Lr
=
Design Wind Velocity
2)
185000 MPa 1.20
kPa
(Table S-6) (PIP VESTA002, 3.2.D)
CALCULATIONS FOR MINIMUM SHELL THICKNESS
As per chapter 3, clause 3.6.1.1, the shell thickness for tanks with nominal tank diameter less than 15 m shall not be less than 5 mm. The required minimum thickness of shell plates shall be the greater of the values computed by the following formulas (As per Appendix S, clause S.3.2) Design Shell Thickness
td
=
4.9D (HL1 - 0.3)G + CA
Hydrostatic Test Thickness
tt
=
4.9D (HL1 - 0.3)
(Sd) (E) (St) (E) td = Design shell thickness, mm tt = Hydrostatic test shell thickness, mm G = Specific Gravity of Fluid to be Stored
=
0.980
D = Nominal Dia. of Tank HL1 = Design Liquid Level
= =
1.806 1.900
m m
CA = Corrosion Allowance Sd = Allowable Stress for Design Condition
= =
0 148.33
mm MPa
St = Allowable Stress for Hydrostatic condition
=
186.00
E = Weld Joint Efficiency
=
0.85
MPa (Table S-4)
Shell Course W1
=
1.900 m
HL1
=
1.900 m
Design Shell Thickness
td
=
0.110 mm
Hydrostatic Test Thickness
tt
=
0.090 mm
Shell Thickness Provided
t1
=
6.00
mm
Total Shell Weight (Uncorroded)
=
5.08
kN
Total Shell Weight (including partition plates) (Corroded)
=
5.08
kN
x =
6 780
Thk.
Weight of Top Curb Angle (Uncorroded)
=
0.35
kN
Weight of Top Curb Angle (Corroded)
=
0.35
kN
Width of course
(Including Curb Angle)
Design Height for Shell Course
az Shell Course
1.90
Shell Thickness, mm (Uncorroded)
6.00
Shell Thickness, mm (Corroded)
6.00
Shell Weight, kN (Uncorroded)
5.08
Shell Weight, kN (Corroded)
5.08
Top Curb Angle
(Formed Section) Cross-sectional Area of the Top Curb Angle
3)
1
Shell Width, m
L
65
x
65
mm2
BOTTOM PLATE DESIGN As per API 650, Appendix S, Clause S.3.1 All bottom plates shall have minimum nominal thickness of 5 mm, exclusive of any corrosion allowance. Required Bottom Plate Thickness Used Bottom Plate Thickness
tb
=
tb
=
5
mm
tb used
=
6.00
mm
5+ CA mm
*Weight of Bottom Plate (Uncorroded)
=
137.82
kg
=
1.35
kN
*Weight of Bottom Plate (Corroded)
=
137.82
kg
=
1.35
kN
*Including 50mm Projection Outside of Bottom Shell Course As per API 650, Appendix J, Clause J.3.2 All bottom plates shall have a minimum nominal thickness of 6 mm.
Required Bottom Plate Thickness Used Bottom Plate Thickness
tb
=
6
mm
tb used
=
6.00
mm
Weight of Bottom Plate (Uncorroded)
=
137.82
kg
=
1.35
kN
Weight of Bottom Plate (Corroded)
=
137.82
kg
=
1.35
kN
4)
INTERMEDIATE WIND GIRDERS Maximum Unstiffened Height As per API 650, Chapter 3, Clause 3.9.7 The maximum height of the unstiffened shell shall be calculated as follows: H1 = 9.47 t (t /D)3/2 (190/V)2 As Ordered Thickness of Top Shell Course
t
=
6.00
Nominal Tank Diameter
D
=
1.806 m
Design Wind Speed
V
=
Maximum Height of the Unstiffened Shell
H1
=
517.01 m
=
0.9585
=
495.58 m
Modification Factor as per S.3.6.7
=
Modulus Of Elasticity at Design Temp.
155
mm kph
Modulus Of Elasticity at 40oC *Maximum Height of the Unstiffened Shell (Modified As Per S.3.6.7)
H1
Transformed Shell Height As per API 650, Chapter 3, Clause 3.9.7.2 Transposed width of each shell course W tr = W x (tuniform/tactual)5/2 W = Actual Width of Each Shell Course, mm tuniform = As Ordered Thickness of top Shell Course, mm
6.00 mm
=
tactual = As Ordered Thickness of Shell Course for Which Transposed Width is Being Calculated (mm) Shell Course Thickness of Shell Course W tr1 = W 1 x (ttop/t1)5/2
Transformed Height of Tank Shell
t1
=
6.00
W tr1
=
1900 mm
Htr
=
1900 mm
=
1.90
[As Htr < H1, Intermediate Wind Girders are not required]
5)
VERIFICATION OF UNSTIFFENED SHELL FOR EXTERNAL PRESSURE Need not to be evaluated as the design external pressure is zero. As per Chapter 3, Clause 3.2.1.i, design external pressure shall not be less than 0.25 kPa. The tanks designed as per API 650 can sustain this minimum pressure.
mm
m
6)
DESIGN OF ROOF Roof Plate Thickness Verification for Structurally Stiffened Flat Roof Methodology: Consider a strip of roof plate 1 in. wide located at the outer periphery of the flat roof, and disregard the support offered by the shell. This strip is considered to be essentially a straight, flat, continuous, uniformly loaded beam, the controlling bending moment is equal to wl2 / 12 and occurs over the supporting stiffeners and wl 2 / 24 occurs at the midspan. M max = -w l 2 / 12 = -p(1) l 2 / 12 = -p l 2 / 12
Over supporting rafters
M max = -w l 2 / 24 = -p(1) l 2 / 24 = -p l 2 / 24
At midspan
where l = length of beam (strip) between stiffeners, inches, p = unit load, psi. Introducing the stress resulting from flexure, f=M/z For a rectangular beam, z = bt 2 / 6 where b = width of beam, inches, and, t = thickness of beam, inches. a = Di
For this case, b = 1.0 in. Hence, z = t2 / 6
l=b
f = p l 2 / 2t 2 l = t * SQRT ( ( 2 * f ) / p ) t = l / SQRT ( ( 2 * f ) / p ) Ref. "Process Equipment Design" By Lloyd E. Brownell & Edwin H. Young Chapter 4, Section 4.3 (Roof Design) Allowable Stresses for Roof Plate Material Assumed Roof Plate Thickness
=
6
mm
=
0.2362 in.
Allowable Design Stress @ Design Temperature
=
148.33
MPa
=
21513 psi
Loadings & Critical Combinations Dead Load
DL
=
kPa 4.40
psi 0.64
lb/in. 0.64
Live Load
Lr
=
1.20
0.17
0.17
External Pressure
Pe
=
0.00
0.00
0.00
Internal Pressure
Pi
=
0.00
0.00
0.00
Load Combination 1
p = DL + Lr + Pe
=
5.60
0.81
0.81
Load Combination 2
p = DL + Pi
=
4.40
0.64
0.64
UNIT
Check Adequacy Against Load Combination 1 ( DL + Lr + Pe ) MID
ENDS
Length of beam (strip) between stiffeners
l
=
25.67
25.67
in.
Load Combination 1
p
=
0.812
0.812
lb/in.
Induced Bending Moment
M
=
22
45
lb-in.
Thickness of the beam (strip)
t
=
0.236
0.236
in.
Section Modulus Allowable Bending Stresses
z
= =
0.009
0.009
in.3
21513
21513
psi
Allowable Bending Moment
M allow
=
200
200
lb-in.
Fb M < M allow
[Satisfactory]
(Fb = Sd)
[ Table S - 5 ]
Check Adequacy Against Load Combination 2 ( DL + Pi ) MID
ENDS 25.67
UNIT in.
0.638
lb/in. lb-in.
Length of beam (strip) between stiffeners
l
=
25.67
Load Combination 2
p
=
0.638
Induced Bending Moment
M
=
18
35
Thickness of the beam (strip)
t
=
0.236
0.236
in.
Section Modulus Allowable Bending Stresses
z
0.009
0.009
in.3
Fb
= =
21513
21513
psi
Allowable Bending Moment
M allow
=
200
200
lb-in.
M < Mallow
[Satisfactory]
Stresses in Roof Plate Segment Between the Stiffeners Ref. Table 11.4, Formulas for Flat Plates With Straight Boundaries and Constant Thickness Case no. 8. Rectangular plate, all edges fixed (Uniform loading over entire plate) Smax = ( β2 q b2 ) / t2
(At center) 1.8 0.4872
2.000 0.4974
∞ 0.500
β2
0.1386 0.1794 0.2094 0.2286 0.2406
0.2472
0.250
α
0.0138 0.0188 0.0226 0.0251 0.0267
0.0277
0.028
a/b β1
1 1.2 1.4 0.3078 0.3834 0.4356
a
=
b
=
a/b β2
= =
1.6 0.468
1.800 m 0.652 m
a = Longer Dimension b = Shorter Dimension
2.76 0.25
( See Table Above )
Check Plate Stresses Against Load Combination 1 ( D L + Lr + Pe ) (p = q = DL + Lr + Pe)
Total Design Load
=
5.60
kPa
In Shorter Direction
Smax =
17 MPa
<
148.33 MPa
[Satisfactory]
In Longer Direction
Smax =
126 MPa
<
148.33 MPa
[Satisfactory]
Check Adequacy Against Load Combination 2 ( DL + Pi ) (p = q = DL + Lr + Pe)
Total Design Load
=
4.40
kPa
In Shorter Direction
Smax =
13 MPa
<
148.33 MPa
[Satisfactory]
In Longer Direction
Smax =
99 MPa
<
148.33 MPa
[Satisfactory]
(Fb = Sd)
7)
CALCULATION FOR ROOF STIFFENER
Flange Breadth
55
mm
6
mm
94
mm
6
mm
Thk. Web Depth Thk.
Roof Plate Reference for Centroid Calculation
Built up Tee Section
Table for Centroid Calculation Plate
A
Y
AY
1
564
47
26508
2
564
97.0
54708
Σ
1128
81216
Centroid
=
72 mm
Table for Moment of Inertia Calculation b
h
Ic
A 4
Yc 2
A x Yc2
I = Ic + A x Yc2
4
mm
mm
mm
mm
mm
mm
mm4
6
94
415292
564
25.00
352500
767792
55
6
990
330
25.00
206250
207240
Moment of Inertia of Built Up Tee Section
=
4 975032 mm
Section Modulus
Zprov'd
=
3 34823 mm
Span of Stiffener
a
=
1.80 m
Self Weight of Stiffener
=
0.16 kN
Weight of Roof Plate Within Stiffined Section Weight of Roof Attachments
= =
0.55 kN 10.00 kN
Live Load on Roof
=
1.41 kN
=
6.73 kN/m
Mmax
=
2.7 kN-m
Zreq'd
=
Total Design Load Per Unit Length
W
(Approx.) (Nozzles, Insulation, Railing/Platform)
Considering simply supported end conditions for the stiffener,
27270 mm3
[As Zreq'd < Zprov'd, The stiffener design is adequate] 8)
TANK STABILITY AGAINST UPLIFT DUE TO INTERNAL PRESSURE Need not to be evaluated as the design internal pressure is zero in our case.
W x a2 / 8 Mmax / (0.6 x Fym)
9)
STABILITY OF TANK AGAINST WIND LOAD
(ASCE 7-05)
Wind velocity
V
=
155
kph
Roof Height Above Shell
HR
=
0.04
m
=
43
m/s
Shell Height
H
=
1.90
m
Height of Tank Including Roof Height
HT
=
1.94
m
Effective Wind Gust Factor
G
=
0.85
ASCE 7-05,6.5.8.1
Force Co- Efficient
Cf
=
0.80
By Interpolation (ASCE 7-05, Fig. 6-21)
Wind Directionally Factor
Kd
=
1.3
Velocity Pressure Exposure Co-Eff.
Kz
=
0.85
Topo Graphic Factor
Kzt
=
1
Importance Factor
I
=
Design Wind Pressure
qz
=
Considering 40 mm Thk. Insulation @ Roof
600-58H-0010 ASCE 7-05, Chapter 6, Table 6-3
1.15
600-58H-0010
0.613 x Kz x Kzt x Kd x V2 x I/1000 1.440 kN/m2
ASCE 7-2005, Chapter 6, Eq. 6-15, Clause 6.5.10
Effective Tank Diameter (De)
600-58H-0010
Insulation Thickness
=
40
(OD + 2 x insulation Thk.) x Kd
=
2.460
m
(OD + 2 x insulation Thk.) + 0.6
=
2.492
m
De
=
2.492
m
600-58H-0010
Effective Area Projected
Ae
=
4.83
m2
600-58H-0010
Design Wind Load
P1
=
Greater of
mm
Effective Projected Area (Ae = De x H)
=
qz x G x Cf x Ae 4.73
Unanchored tanks shall satisfy both of the following conditions: Case 1:
0.6 Mw + MPi < MDL / 1.5
Case 2:
Mw + 0.4MPi < ( MDL + MF ) / 2 Mw
=
P1 x H / 2
MPi
=
Pi x A X D / 2
MDL
=
(Weight of shell + roof + bottom) x D / 2
Mw
=
4.6 kN-m
MPi
=
0 kN-m
MDL
=
6.9 kN-m
MF
=
=
3387
ft-lbs
For no fluid in the tank
0
Case 1:
3
<
5
[Satisfactory]
Case 2:
5
<
3
[Unsatisfactory]
[Anchorage against wind pressure is required]
kN
ASCE 7-05, Chapter 6, Eq. 6-28, Clause 6.5.15
9.1)
Resistance To Sliding:
H/2 for Uniform pressure
The wind load pressure on projected area
=
API 650 3.11.4 0.86 kN/m2
=
PENTAGON PENTAGON
18.0 psf
(API 650, Chapter 3, Clause 3.2.1 (f))
This pressure is for wind velocity of 120 mph (190 kph), for all other wind velocities the pressure shall be adjusted in proportion of ratio (V/190)
2
Tank OD
Do
=
Design Wind Velocity
V
=
155
=
0.666
Wind Pressure on vertical plane surfaces
=
0.86
kN/m2
(API 650, Chapter 3, Clause 3.2.1 (f))
Wind Pressure on vertical conical surfaces
=
1.44
2
(API 650, Chapter 3, Clause 3.2.1 (f))
Projected area of roof
=
0.036 m2
Projected area of shell
=
4.73
Vf
Velocity Factor
Fwind
= =
Ffriction
= =
=
(V/190)2
1.812 m kph
kN/m m2
Vf (Wind Pressure on Roof x Projected Area of Roof + Wind Pressure on Shell x Projected Area of Shell) 2.74 kN
(API 650, Chapter 3, Clause 3.2.1 (f))
Maximum of 40% of Weight of Tank 12.27 kN
[Anchorage against sliding is not required]
(API 650, Chapter 3, Clause 3.11.4)
10)
Stability Calculations Against Seismic Load (As per API 650 Addendum Four 2005 ) D
=
1.806
m
Nominal dia of Tank
H
=
1.900
m
Maximum design product level
D/H
=
0.95
H/D
=
1.05
Site Class
=
E
Corroded thickness of bottom plate
tb
=
6.00
mm
Corroded thickness of 1st shell course
ts
=
6.00
mm
Over turning ring wall moment Mrw For Site class 'E'
=
As per API 650 E.4.9.1 Ai =
sqrt{[Ai(WiXi+WsXs+WrXr)]2 + [Ac(WcXc)]2}
As per API 650 E.6.1.5
2.5 x Q x Fa x So ( I / Rwi )
As per Equation E-4
Acceleration-based site coefficient
Fa
=
2.5
From Table E-1
Scaling Factor
Q Ss
= =
1 0.1
As per API 650 E.4.9.1
S1
=
0.04
So
=
0.4 X Ss
=
0.04
As per E.4.2.c
Rwi
=
4
From Table E-4
I
=
1.25
600-58H-0010
Ai
=
0.08
As per Equation E-4
As per Equation E-6, For seismic design categories E & F, 0.5S1(I/Rwi) Ai ≥
As per Equation E-6
≥
0.006
Condition staisfied Wi
=
Effective impulse weight of the liquid
Wi
=
(1-0.218D/H)Wp
Wp
=
Weight of content based on design specific gravity of the product
When D/H <1.33
Wi When D/H < 1.33 Xi
As per Equation E-14
=
46.48
KN
= =
46482 36.85
N KN
=
36850
N
As per E-6.1.2.1 = Height from the bottom of the shell to the center of action of the lateral Siesmic force related to impulsive liquid force
Xi Ws
=
(0.5-0.094D/H)H
=
0.78
= =
Xs
= =
Wr
= =
Xr
= =
As per Equation E-17 m
Total Weight of Shell and appurtenances (Uncorroded) 30
KN
Height from the bottom of the tank shell to center of gravity 1.28
m
Total Weight of fixed tank roof including framing (Uncorroded) 0.00
KN
Height from the top of the shell to the roof and roof appurtenances center of gravity 0.00
m
Tc
=
Natural peroid of the convective (sloshing ) mode of behaviour of the liquid, seconds
Tc
=
1.8 x Ks x sqrt (D)
Ks
=
Sloshing peroid cofficient
Ks
= =
0.578 sqrt (tanh (3.68H/D)) 0.58
As per Equation E-2a As per Equation E-3
As per E 4.8.2
Therefore Tc TL When TC < TL
= =
1.40 4
As per E.4.8.2 As per E.4.9.1
As per E.4.9.1 2.5 x Q x Fa x So x (Ts /Tc) x (I/Rwc) ≤ Ai
Ac
=
Ts
=
(FvS1) / (FaSs)
S1
=
0.04
Fv Rwc
= =
3.5 2
Ts
=
0.56
Ac
=
0.06
As per Equation E-7
Where
Wc
From Table E-2 From Table E-4
=
Effective Convective (sloshing)portion of the liquid Weight
=
0.23 x (D/H) Tanh (3.67 H/D) x Wp
= = Xc
As per API 650 E-2
10.15
KN
10153
N
As per Equation E-15
=
Height from the bottom of the tank shell to the center of action of lateral siemic force related to convective liquid force
=
[1-{Cosh((3.67 x H/D)-1)/((3.67 x H/D) Sinh((3.67 x H/D))}] x H
=
1.70
As per Equation E-18
m
Therefore Ring Wall Moment Mrw
=
5.40
KN-m
=
5404
N-m
=
3985
ft-lbs
Resisting force to be adequate for tank stability J<1.54 Anchorage Ratio J
=
Mrw
As per API 650 E.6.2.1.1.1
D2(wt(1-0.4Av)+wa) Where
Av
=
0.14 x SDS
SDS
=
2.5 x Q x Fa x So
=
0.3
Av wa
=
As per API 650 E.6.1.3 From Equation E-4
= 0.035 99 x ta x (Fy x H x Ge)^0.5 ≤ 1.28 x H x D x Ge
As per API 650 E.6.2.1.1
Where Ge
ta
=
=
Effective specific gravity including vertical seismic effects
=
G x (1-0.4 x Av)
=
0.97
As per API 650 E-2
Corroded thickness of the bott. plate under the shell extending at the distance L from the inside of the shell
ta
=
6.00
mm
wa
=
10391
N/m
wa
=
4.2
N/m
wt
=
[(Ws/πD)+wrs)]
wrs
=
wa
wt
0.004
≤
4.2
N/m
KN/m As per API 650 E.6.2.1.1
Roof load acting on the tank shell (Uncorroded)
=
0.000
KN/m
= =
0 5.37
N/m KN/m N/m
Therefore
=
5373
Anchorage Ratio J
=
0.312
<
1.54
Condition staisfied Tank is self anchored As Anchors Are Being Provided, The Tank Will Be Considered As Mechanically Anchored
10.1)
Shell Compression In Mechanically Anchored Tanks
= 10.2)
As per API 650 E.6.2.2.2
1.26
Mpa
Allowable Longitudinal Membrane Compression Stress in Tank Shell
As per API 650 E.6.2.2.3
G x H x D2
Calculating value of
t2 =
0.17
When GHD2 / t2 is less than 44, then Fc
=
{(83x ts)/(2.5 x D)} + 7.5 x sqrt(G x H)
GXH 0.5 X Fty
= =
1.862 83.335
Fc
=
121
Where
Therefore, Mpa
As ơc < Fc Condition staisfied
10.3)
Seismic Base Shear
(As Per E.6.1)
V Vi
= =
Total Design Base Shear (N) Design Base Shear Due to Impulsive Component (N)
Vc
=
Design Base Shear Due to Convective Component (N)
Vi
=
Ai(Ws+Wr+Wf+Wi)
Vi
=
Vc
=
AcW c
Vc
=
635.11
V
=
Sqrt(Vi2 + Vc2)
V
=
5298.6
N
V
=
5.2986
kN
5260.4 N
N
<
0.5 x Fty
11)
ANCHORAGE FOR UPLIFT LOAD CASES, PER API 650 TABLE 3-21B
Test Pressure
P
=
ATM
kPa
Pt
= =
0.00 0.00
in. of water kPa
=
0.00
in. of water
Dead Load of Shell Minus Any CA and Any Dead Load Other Than Roof W1
=
Weight of shell (Corroded)
=
5424.58 N 1219.5 lbs
=
Dead Load of Shell Minus Any CA and Any Dead Load Including Roof Plate Acting on the Shell Minus Any CA W2
=
Weight of shell (Corroded) + Weight of Roof (corroded)
=
6807.7 N 1530.43 lbs
=
Dead Load of the Shell Using As Built Thicknesses and Any Dead Load Other Than Roof Plate Acting on the Shell Using As Built Thickness W3
=
Weight of Shell
=
5424.6 N 1219.5 lbs
= Yield stress for Anchor Bolts Fy
=
th
=
D MS
= =
36000 psi
SA 307 Gr. B
6 mm
=
1.806 m 5.404 kN-m
= =
0.23622 in. 5.92 ft 3985 ft-lbs
(From Seismic Calculation)
Table 3 - 21 NET UPLIFT FORMULA, U (lbf)
UPLIFT LOAD CASES
*Fy For Anchor Bolts (PSI)
Design Pressure
((P - 8th) x D2 x 4.08) - W 1
-1490.05
15076
Test Pressure
((Pt - 8th) x D2 x 4.08) - W 1
-1490.05
15076
Wind Load
(4 x Mw / D) - W 2
756.36
15076
Seismic Load
(4x Ms/D) -W 2
1160.79
15076
Design Pressure +Seismic
((P-8th) x D² x 4.08) + (4 x Ms/D)-W1
1201.17
15076
Design Pressure + Wind
((P-8th) x D² x 4.08) + (4 x Mw/D)-W1
796.74
15076
UPLIFT LOAD CASES
tb = U / N
Ar = tb/Fall
lbs
in.2
mm2
Design Pressure Test Pressure
-373 -373
-0.025 -0.025
-15.94 -15.94
Wind Load
189
0.013
8.09
Seismic Load
290
0.019
12.42
Design Pressure + Seismic
300
0.020
12.85
Design Pressure + Wind
199
0.013
8.52
U = Net Uplift Load N = No. of Anchor Bolts Ar = Required Bolt Area
As per API 650, Chapter 3, Clause 3.1.1.3 Design Tension Load Per Anchor
=
4MW/dN - W/N
Bolt Circle Diameter (BCD)
d
=
No. of Anchor Bolts Weight of shell plus roof supported by the shell less 0.4 times the force due to internal pressure Design Tension Load Per Anchor
N W
= = =
Required Bolt Area Provided Bolt Area
Consider M30 Bolt
2.000 m 4 Nos. 6 kN 200 lbs
Areq.
=
13 mm2
Aprov.
=
539 mm2
(Uncorroded Root Area)
=
443 mm2
(Corroded Root Area)
[Area of the anchor bolt provided is sufficient] ANCHOR CHAIR CALCULATIONS
P e
C
12)
a
h
As Per AISI E-l, Volume ll, Part Vll
g
Jmin
Ød
f
Top Plate Thickness Calculations: C = [P(0.375g-0.22d)/Sf]0.5
Top Plate Thickness C
=
Top Plate Thickness
S f
= =
Stress At Point
=
25
ksi
Distance From Outside of
=
0.98
in.
g
=
Distance between Gusset Plates
=
3.94
in.
d
=
Anchor Bolt Diameter (corroded)
=
1.06
in.
=
0.45
kips
(AISI E-1)
Top Plate to Edge Of Hole
P
Design Load or Max. Allowable =
Anchor Bolt Load or 1.5 Times Actual Bolt Load, whichever is lesser
.
Top Plate Thickness Calculated
C
=
0.151 in.
=
3.8
mm
Used Top Plate Thickness
C
=
0.551 in.
=
14
mm
[Top Plate Thickness Is Adequate]
Anchor Chair Height Calculations: (Pe/t2)[{1.32*Z/(1.43*a*h2/Rt)+(4ah2)0.333}+{0.031/(Rt)0.5}]
Sind.
=
Z
=
Reduction Factor
=
a
=
Top Plate Width
=
6.00
in.
h
=
Anchor Chair Height
=
6.00
in.
R
=
Nominal Shell Radius
=
35.55
in.
t
=
Shell Thickness
=
0.472
in.
m
=
Bottom Plate Thickness
=
0.236
in.
e
=
Anchor Bolt Eccentricity
=
3.74
in.
Sall.
=
Allowable Stress
=
21.51
ksi
Z
=
0.9849
Sind.
=
0.409
(including repad)
1/[{.177am(m/t)2/(Rt)0.5}+1]
ksi
[Anchor Chair Height Is Adequate] Jmin
Gusset Plate Thickness Calculations:
0.04 ( h - C ) or 1/2"
Gusset Plate Thickness
=
Gusset Plate Thickness Provided
=
[Gusset Plate Thickness Is Adequate]
13)
WEIGHT SUMMARY Empty
=
Weight of Working Fluid
=
Operating Weight
=
Weight of Test Fluid
= =
Test Weight (Full of water)
3282 kg 3990 kg 7272 kg 4835 kg 8117 kg
(Considering HLL = 1600mm)
0.218 in. 14 mm
= =
5.5 mm 0.551 in.
14)
FOUNDATION LOADING DATA
The self weight of roof and live load will be transferred to tank shell Live load transferred to foundation Live Load on roof
Lr
=
1.20
kN/m2
Area of Roof
Ar
=
2.60
m2
Total Live Load
W L = Lr x Ar
=
3.12
kN
Circumference of Tank
C=πxD
=
5.69
m
Live Load transferred to Foundation
LL = W L / C
=
0.55
kN/m
Self Weight of Roof + Stiffeners
Wr
=
1.38
kN
Self Weight of Bottom Plate
Wb
=
1.35
kN
Self Weight of Shell
Ws
=
5.42
kN
Self Weight of shell Attachments
Wa
=
24.02
kN
Total Dead Load acting on shell
Wr + Ws + Wa
=
30.83
kN
Dead Load Transferred to Foundation
W d = DL
=
5.42
kN/m
Dead load transferred to foundation
Operating & Hydrostatic Test Loads Wr + Ws + Wa + W b = 32.18
kN
=
3282
kgs
Weight of Fluid in Tank at Operating Conditions
W f = 39.13
kN
=
3990
kgs
Weight of Water in Tank at Hydrotest Conditions
W w = 47.41
kN
=
4835
kgs
Uniform Load Operating Condition = (Self wt.+ Fluid)/Area
W o = 28.02
kN/m
Uniform Load Hydrotest Condition = (Self wt.+ Water)/Area
W h = 31.07
kN/m2
Self Weight of Tank
2
Wind Load Transferred to Foundation Base Shear due to wind load
Fw
=
4.73
kN
Reaction due to wind load
Rw
=
0.45
kN/m
Moment due to wind load
Mw
=
4.59
kN-m
Reaction due to seismic load
Rs
=
0.52
kN/m
Moment due to seismic load
Ms
=
5.40
kN-m
Base Shear due to seismic load
FS
=
5.30
kN
Seismic Load Transferred to Foundation
Summary of Foundation Loading Data Dead load, shell, roof & ext. structure loads
DL =
5.42
Live load
LL =
0.55
kN/m
Uniform load, operating condition
Wo =
28.02
kN/m2
Uniform load, hydrotest load
W h=
31.07
kN/m2
Base shear due to seismic
FS=
5.30
kN
Reaction due to seismic load
Rs =
0.52
kN/m
Moment due to seismic load
Ms =
5.40
kN-m
Base shear due to wind
Fw =
4.73
kN
Reaction due to wind
Rw =
0.45
kN/m
Moment due to wind load
Mw=
4.59
kN-m
Note : Consider 15-20% variation in weight while designing the foundation
kN/m
AS THE TOTAL HIGHT OF THE STORAGE TANK IS 12 M WE DIVIDED THIS TANK INTO 6 COURSES OF WIDTH OF 2000 mm EACH CALCULATIONS OF THE SHELL THICKNESS FOR COURSE 1 As per chapter 3, clause 3.6.1.1, the shell thickness for tanks with nominal tank diameter less than 15 m shall not be less than 5 mm. The required minimum thickness of shell plates shall be the greater of the values computed by the following formulas (As per Appendix S, clause S.3.2) td
Design Shell Thickness
=
4.9D (HL1 - 0.3)G + CA (Sd) (E)
Hydrostatic Test Thickness
tt
=
td = Design shell thickness, mm
4.9D (HL1 - 0.3) (St) (E)
6.51585
tt = Hydrostatic test shell thickness, mm G = Specific Gravity of Fluid to be Stored D = Nominal Dia. of Tank HL1 = Design Liquid Level CA = Corrosion Allowance Sd = Allowable Stress for Design Condition
= = = = =
St = Allowable Stress for Hydrostatic condition E = Weld Joint Efficiency
= =
4.84512 1 14.008 12 0 145 195 0.85
0.85
Design Height for Shell Course
HL1
Design Shell Thickness
td
Hydrostatic Test Thickness
tt
= = = =
The designed thickness of the course
=
8
Width of course
W1
(including curb angle)
Shell Plates Weight Summary Shell Course Shell Width, m Shell Thickness, mm (Uncorroded) Shell Thickness, mm (Corroded) Shell Weight, kN (Uncorroded) Shell Weight, kN (Corroded) Shell Internal Diameter m Shell External Diameter m Mean Diamter of the Shell course m
Di Do D
2
mm mm
m
12
m
6.515851
mm
4.84512
mm
mm
1 2.00 8.00 8.00 2.75 2.75 14 14.016 14.008
m m mm MPa MPa Table S4
CALCULATIONS OF THE SHELL THICKNESS FOR COURSE 2 As per chapter 3, clause 3.6.1.1, the shell thickness for tanks with nominal tank diameter less than 15 m shall not be less than 5 mm. The required minimum thickness of shell plates shall be the greater of the values computed by the following formulas (As per Appendix S, clause S.3.2) Design Shell Thickness
td
=
Hydrostatic Test Thickness
tt
=
4.9D (HL1 - 0.3)G + CA (Sd) (E) 4.9D (HL1 - 0.3) (St) (E)
td = Design shell thickness, mm tt = Hydrostatic test shell thickness, mm G = Specific Gravity of Fluid to be Stored D = Nominal Dia. of Tank HL1 = Design Liquid Level CA = Corrosion Allowance Sd = Allowable Stress for Design Condition
= = = = =
St = Allowable Stress for Hydrostatic condition E = Weld Joint Efficiency
= =
5.39895
mm
4.0146
mm
1 14 10 0 145 195 0.85
0.85 Width of course
W1
(including curb angle)
Design Height for Shell Course
HL1
Design Shell Thickness
td
Hydrostatic Test Thickness c Shell External Diameter
tt
2
m
10
m
5.398945
mm
4.0146
mm
m m =
The designed thickness of the course 1
Shell Plates Weight Summary Shell Course Shell Width, m Shell Thickness, mm (Uncorroded) Shell Thickness, mm (Corroded) Shell Weight, kN (Uncorroded) Shell Weight, kN (Corroded) Shell Internal Diameter Shell External Diameter Mean Diamter of the Shell course m
= = = =
m m
Di Do D
6 mm
1 2.00 0.00 0.00 0.00 0.00 14 14.012 14.006
m m mm MPa MPa Table S4
CALCULATIONS OF THE SHELL THICKNESS FOR COURSE 3 As per chapter 3, clause 3.6.1.1, the shell thickness for tanks with nominal tank diameter less than 15 m shall not be less than 5 mm. The required minimum thickness of shell plates shall be the greater of the values computed by the following formulas (As per Appendix S, clause S.3.2) Design Shell Thickness
td
=
Hydrostatic Test Thickness
tt
=
4.9D (HL1 - 0.3)G + CA (Sd) (E) 4.9D (HL1 - 0.3) (St) (E)
td = Design shell thickness, mm
4.28576
mm
tt = Hydrostatic test shell thickness, mm G = Specific Gravity of Fluid to be Stored D = Nominal Dia. of Tank HL1 = Design Liquid Level CA = Corrosion Allowance Sd = Allowable Stress for Design Condition
3.18685
mm
= = = = =
St = Allowable Stress for Hydrostatic condition E = Weld Joint Efficiency
= =
1 14 8 0 145 195 0.85
0.85 Width of course
W1
(including curb angle)
Design Height for Shell Course
HL1
Design Shell Thickness
td
Hydrostatic Test Thickness c Shell External Diameter
tt
= = = =
2
m
8
m
4.285761
mm
3.186848
mm
m m
The designed thickness of the course 3
Shell Plates Weight Summary Shell Course Shell Width, m Shell Thickness, mm (Uncorroded) Shell Thickness, mm (Corroded) Shell Weight, kN (Uncorroded) Shell Weight, kN (Corroded) Shell Internal Diameter Shell External Diameter Mean Diamter of the Shell course m
m m
Di Do D
1 2.00 0.00 0.00 0.00 0.00 14 14.012 14.006
m m mm MPa MPa Table S4
AS THE TOTAL HIGHT OF THE STORAGE TANK IS 12 M WE DIVIDED THIS TANK INTO 6 COURSES OF WIDTH OF 2000 mm EACH CALCULATIONS OF THE SHELL THICKNESS FOR COURSE 4 As per chapter 3, clause 3.6.1.1, the shell thickness for tanks with nominal tank diameter less than 15 m shall not be less than 5 mm. The required minimum thickness of shell plates shall be the greater of the values computed by the following formulas (As per Appendix S, clause S.3.2) Design Shell Thickness
td
=
Hydrostatic Test Thickness
tt
=
4.9D (HL1 - 0.3)G + CA (Sd) (E) 4.9D (HL1 - 0.3) (St) (E)
td = Design shell thickness, mm
2.6591
mm
tt = Hydrostatic test shell thickness, mm G = Specific Gravity of Fluid to be Stored D = Nominal Dia. of Tank HL1 = Design Liquid Level CA = Corrosion Allowance Sd = Allowable Stress for Design Condition
2.3591
mm
= = = = =
St = Allowable Stress for Hydrostatic condition E = Weld Joint Efficiency
= =
1 14 6 0 173 195 0.85
0.85 Width of course
W1
(including curb angle)
Design Height for Shell Course
HL1
Design Shell Thickness
td
Hydrostatic Test Thickness
tt
= = = =
2
m
6
m
2.659096
mm
2.359095
mm
The designed thickness of the course
Shell Plates Weight Summary Shell Course Shell Width, m Shell Thickness, mm (Uncorroded) Shell Thickness, mm (Corroded) Shell Weight, kN (Uncorroded) Shell Weight, kN (Corroded) Shell Internal Diameter Shell External Diameter Mean Diamter of the Shell course m
m m
Di Do D
1 2.00 0.00 0.00 0.00 0.00 14 14.012 14.006
m m mm MPa MPa Table S4
AS THE TOTAL HIGHT OF THE STORAGE TANK IS 12 M WE DIVIDED THIS TANK INTO 6 COURSES OF WIDTH OF 2000 mm EACH CALCULATIONS OF THE SHELL THICKNESS FOR COURSE 5 As per chapter 3, clause 3.6.1.1, the shell thickness for tanks with nominal tank diameter less than 15 m shall not be less than 5 mm. The required minimum thickness of shell plates shall be the greater of the values computed by the following formulas (As per Appendix S, clause S.3.2) Design Shell Thickness
td
=
Hydrostatic Test Thickness
tt
=
4.9D (HL1 - 0.3)G + CA (Sd) (E) 4.9D (HL1 - 0.3) (St) (E)
td = Design shell thickness, mm
1.72608
mm
tt = Hydrostatic test shell thickness, mm G = Specific Gravity of Fluid to be Stored D = Nominal Dia. of Tank HL1 = Design Liquid Level CA = Corrosion Allowance Sd = Allowable Stress for Design Condition
1.53134
mm
= = = = =
St = Allowable Stress for Hydrostatic condition E = Weld Joint Efficiency
= =
1 14 4 0 173 195 0.85
0.85 Width of course
W1
(including curb angle)
Design Height for Shell Course
HL1
Design Shell Thickness
td
Hydrostatic Test Thickness
tt
= = = =
2
m
4
m
1.72608
mm
1.531342
mm
The designed thickness of the course
Shell Plates Weight Summary Shell Course Shell Width, m Shell Thickness, mm (Uncorroded) Shell Thickness, mm (Corroded) Shell Weight, kN (Uncorroded) Shell Weight, kN (Corroded) Shell Internal Diameter Shell External Diameter Mean Diamter of the Shell course m
m m
Di Do D
1 2.00 0.00 0.00 0.00 0.00 14 14.012 14.006
m m mm MPa MPa Table S4
AS THE TOTAL HIGHT OF THE STORAGE TANK IS 12 M WE DIVIDED THIS TANK INTO 6 COURSES OF WIDTH OF 2000 mm EACH CALCULATIONS OF THE SHELL THICKNESS FOR COURSE 6 As per chapter 3, clause 3.6.1.1, the shell thickness for tanks with nominal tank diameter less than 15 m shall not be less than 5 mm. The required minimum thickness of shell plates shall be the greater of the values computed by the following formulas (As per Appendix S, clause S.3.2) Design Shell Thickness
td
=
Hydrostatic Test Thickness
tt
=
4.9D (HL1 - 0.3)G + CA (Sd) (E) 4.9D (HL1 - 0.3) (St) (E)
td = Design shell thickness, mm
0.79306
mm
tt = Hydrostatic test shell thickness, mm G = Specific Gravity of Fluid to be Stored D = Nominal Dia. of Tank HL1 = Design Liquid Level CA = Corrosion Allowance Sd = Allowable Stress for Design Condition
0.70359
mm
= = = = =
St = Allowable Stress for Hydrostatic condition E = Weld Joint Efficiency
= =
1 14 2 0 173 195 0.85
0.85 Width of course
W1
(including curb angle)
Design Height for Shell Course
HL1
Design Shell Thickness
td
Hydrostatic Test Thickness
tt
= = = =
2
m
2
m
0.793064
mm
0.70359
mm
The designed thickness of the course
Shell Plates Weight Summary Shell Course Shell Width, m Shell Thickness, mm (Uncorroded) Shell Thickness, mm (Corroded) Shell Weight, kN (Uncorroded) Shell Weight, kN (Corroded) Shell Internal Diameter Shell External Diameter Mean Diamter of the Shell course m
m m
Di Do D
1 2.00 0.00 0.00 0.00 0.00 14 14.012 14.006
m m mm MPa MPa Table S4
BOTTOM PLATE DESIGN
ACCORDING TO THE API 650 CLAUSE 5.4.1 ALL BOTTOM PLATES SHALL HAVE NOMINAL MINIMUM THICKNESS OF 6 MM (0.236 INCH) EXCLUSIVE OF ANY CORROSION ALLOWANCE AND SHELL HAVE MINIMUM NOMIAL WIDTH OF 1800 MM. TOP WIND GIRDER ACCORDING TO API 650 CLAUSE 5.9.6.1 THE REQUIRED SECTION MODULUS OF STIFFENING RING SHALL BE DETERMINED BY THE FOLLOWING EQUATION Z=(D² H2/17)* (V/190)² WHERE Z= REQUIRED MINIMUM SECTION MODULUS D= NOMINAL TANK DIAMETER = 14.008 METERS H2 HIGHT OF THE TANK = 12 METERS V= DESIGN SPEED OF THE WIND (3-SEC GUST) 165 KM/HOUR Z
=
104.4589
cmᵌ
cmᵌ
INTERMEDIATE WIND GIRDERS according to clause 5.9.7.1 of API 650, the maximum hight of the unstiffened shel shall be calculated as follows: as H1 = 9.47 * t * ((t/D)ᵌ)^0.5 * (190/V)² WHERE H1= VERTICAL DISTANCE IN M, BETWEEN THE INTERMEDIATE WIND GIRDER AND TOP ANLE OF THE SHELL (meters) H1 = 21.12045 m t = AS ORDERED THICKNESS UNLESS OR OTHER WISE SPECIFIED OF THE THINNEST SHELL COURSE(mm) t = 6 mm D = NOMINAL SHELL DIAMETER (m) = 14.008 m V = DESIGN WIND SPEED (3- sec - gust) = 165 km/hr H1
=
21.12045 meters
TRANSFORMED SHELL acoording to the clause no: 5.9.7.2 after calculating the maximum hight of the unstiffened shell H1 is detrmined the hight of the transformed shell has to be determined accorging to the following method: (A) with the following equation change the actual width with each of the shell course into transposed width of eachshell course having the top shell thickness
Wtr = W((tuniform)/(t actual))^(5/2) where Wtr = transposed width of the the each shell course (mm) = mm W = actual width of th shell course (mm) = mm t uniform = as ordered thickness of the thinest shell course (mm) = mm t actual = as ordered thickness of the shell course for which transposed width has to be calculated = mm
For course 1 having thickness 8 mm recommended Wtr = W((tuniform)/(t actual))^(5/2) Wtr W t uniform t actual
= = = =
974.2786 2000 6 8
mm mm mm mm
all courses from 2 to 6 having thickness of 6 mm recommended Wtr W t uniform t actual
= = = =
2000 2000 6 6
mm mm mm mm
b. Add the transposed widths of the courses. The sum of the transposed widths of the courses widths of the courses will give the hight of the transpormed shell H transfmd = 10974.28 mm 10.97428 meters as the transformed hight is smaller than the hight of the unstiffened shell there is no need to have a stiffner ring or intermediate wind girder is not required
TANK CONICAL ROOF