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Rectangular tank sizing Calculation Objectives

- To calculate the thickness of tank plates

- To determine the size of stiffening frame for tank - To determine dry and test weights

Assumptions

- Specific gravity of liquid is 1

- Acceleration due to gravity is 9.81 m/s2 - Density of steel is 7850 kg/m3

- Minimum Distance between stiffeners = 1.05m

References

1. UL-142, Steel Aboveground Tanks for flammable and combustible liquids, Underwriters Laboratories Inc.

2 Eugene F. Megyesy, Pressure Vessels Handbook, Pressure Vessels Publishing Inc.

3 Corus Construction and IndustrialStructural Sections to BS 4: Part 1:1993 & BS EN 10056:1999

4 ASME Boiler and Pressure Vessel Code Section II subpart D 5 Trauvay and Cauvin (2001), Piping Equipment

6 Young, W. C. & Budynas, R. G. (2002) Roark's Formulas for Stress and Strain 7th ed., McGraw-Hill. 2002

7 ASME B31.10M - 2000: Welded and Seamless Wrought Steel Pipe 8 ASME B.16.5 - 2009: Pipe Flanges and Flanged Fittings

Notes

1 A total of 10 Stiffeners were used based on a spacing of 1.05 m on the long sides (3 stiffeners on each longer side; and 2 stiffeners on each shorter side) 2 Sump Pump weight was not included in calculations

3 Weights are calculated weights. Final weights to be advised by vendor Weight calulation does not include weir.

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Definition of Terms

- a Length of top plate - b Width of top plate - CA Corossion Allowance - E Modulus of Elasticity - g Gravitational acceleration - H Height of tank

- Imin Minimum Moment of inertia of top edge stiffening - L Length of tank

-

l

Spacing between vertical stiffeners -

l

b Spacing of bottom plate support - R Reaction at top edge

- r Radius of contact of heaviest dead weight on top tank - S Allowable stress of tank material

- t Required thickness - ta Selected thickness - w Load

- W Heaviest Dead weight on top plate

- Zmin Minimum Section Modulus of vertical stiffener

-α Factor Depending on ratio of Length to Width of top plate a/b -β Factor Depending on ratio of Height to Length H/L

ρp Density of tank material ρ Density of liquid in tank ν Poisson ratio of tank material CSA Cross-Sectional Area

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Equipment Tag No. ABH 8000 Project No. No. of equipments 1 1 DESIGN DATA

Tank Material SA-516 Gr. 60

Modulus of Elasticity E = N/m2

Allowable Stress S = N/m2

Density of tank material ρp = kg/m

3 Tank Dimensions: Length L = m Width W = m Height H = m Type of Liquid Specific Gravity = Density of liquid ρ = kg/m3

Acceleration due to gravity g m/s2

No. of vertical stiffeners one side =

Maximum Distance between Stiffners l = m

Corrosion Allowance CA = mm

Height/length ratio (H/L) =

Factor for H/L β = (See Appendix)

2 SIDE PLATE THICKNESS

Required Plate Thickness = m

= mm

Thickness + Corossion Allowance = mm

Selected Plate thickness ts = mm

3 LOAD

= N/m

= N/mm

4 VERTICAL STIFFENING Minimum Section Modulus

= cm3

An equal angle L-section of dimensions 1216 1.05 0.0045733 28252.8 28.25 117.9E+06 203.4E+09 3 1000 1 Water 0.095 0.5714 3 7.57 4.57 2.4 3 4.2 7850 8 9.81 77.538 S gH l t



2

2

gH

w

S Hlw Zmin 0.1284

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5 TOP EDGE STIFFENING

Reaction at top edge = N/mm

Minimum required moment of inertia for top edge stiffening:

= mm4

= cm4

200 x 200 x 16 (moment of inertia = cm3) frame is satisfactory for vertical stiffening

BOTTOM PLATE SUPPORT SPACING

using a minimum plate thickness of mm calculated for side plates above, the maximum spacing of bottom plate supports:

= m

6 TOP PLATE THICKNESS Dimensions of top plate

Length a = m

Width b = m

Constant based on length to width ratio a/b a/b =

α = (See Appendix)

Poisson's ration

Total dead weight on tank top plate = kg (Note 2)

= N

Sum of Radii of load contacts with top plate

r = mm

Total Stress due to dead load on 4.57mm required plate thickness

= N/m2

This Stress value is < S ( N/m2) therefore required thickness for side plates is

Selected thickness = 8 mm 4.4 3.2 3195.0 4.57 -0.000125 30608563 325.69 2251.2 2342 0.3 1.375 8.48 22512126 117.9E+06 adequate 1475 0.406 gH S t lb 1.254

  

r b t W 2 ln 1 2 3 2

w

R

0

.

3

a

Et

RL

I

192

4 min

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7 WEIGHT CALCULATIONS a Weight of Tank Plates

(Surface area of tank * tank thickness * Density of tank material) i- Side plates

=

ii- Bottom Plate kg

= iii- Top Plate

= Total weight of tank plates = b Weight of Stiffeners

Weight of one vertical stiffener

(CSA*Length*density of stiffener) = kg Total Weight of vertical Stiffeners = kg Weight of top edge stiffening

(CSA*Length*density of stiffener) = kg

Total weight of stiffeners = kg

c Weights of nozzles

7 Nos. 2" nozzles @ = kg

2 Nos. 4" nozzles @ = kg

2 Nos. 24" Manways @ kg/MW = kg

Total weight of nozzles = kg

d Total Empty weight of tank

(Weights of tank plates+Stiffners+nozzles) = kg Weight of water to fill tank

(Volume of tank * density of water) = kg e. Operating Weight

(Empty weight of tank + Weight of water at NLL)

NLL = m

Weight of water at NLL = kg/m3

Total Operating Weight = f. Weight of tank filled with water

(Empty weight of tank + Weight of water) = 35982.818 kg 1.06 13356 19098.818 30240 5742.818 281.22 19.06 140.6 1571.256 723.456 791.28 884.224 3845.872 3.63 kg/Nozzle 9.53 kg/Nozzle 325.69 2170.368 25.41 847.8 84.78 ) ( 2t p LHWH

p s

LWt

p s

abt

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TANK SKETCH

Vertical Stiffener Cross-Section

Top-Edge stiffening Cross-Section

150mm

150mm

15mm

200mm

200mm

16mm

2

.4

m

Top Plate

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Summary of Results

-- Tank material SA-516 Gr. 60

-- Thickness of plates

Sides = 8 mm

Bottom = 8 mm

Top = 8 mm

-- Number of vertical stiffeners = 10

-- Stiffener configuration Equal leg (L section) Stiffener Cross-section Dimensions

Vertical = 150mm x 150mm x 15mm

Top edge = 200mm x 200mm x 16mm

-- Dry weight of tank = 5742.818 kg

-- Operating weight of tank = 19098.82 kg

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APPENDIX

Values for factors used

1

2

3

4

5

6

7

8

9

10

11

12

13

Ratio

H/L or

H/

l

0.25 0.286 0.333

0.4

0.5 0.667

1

1.5

2

2.5

3

3.5

4

Constant

β

0.024 0.031 0.041 0.056

0.08 0.116

0.16 0.26 0.34

0.38 0.43 0.47 0.49

Table 1: Values of β

Table from Ref. 3

1

2

3

4

5

6

Ratio

a/b

1

1.2

1.4

1.6

1.8

2

Constant

α

-0.238 -0.08 0.011 0.053 0.068 0.067 0.067

Table 2: Values of β

Table from Ref. 8

Interpolation for β

Interpolation for α

Col. No.

5

6

-0.000125

β

-0.078

0.011

0.5714

0.667

H/L or H/

l

0.5

0.095

β

0.08

0.116

H/L or H/

l

1.2

1.4

1.375

Col. No.

2

3

References

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