Flare Stack Mechanical Design Calculations

24
DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACK Page : 1 of 24 Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0 Project : Design & procurement of Flare Stack Date : 4.4.2000 Job Name : Propylene Recovery Unit Location : Gulf of Seuz Dwg. No. : Client : ABB/OPC Stack Type : Self supported & Multiple Diameter Item : X-06-02 ELEVATED FLARE STACK SELF SUPPORTED & MULTIPLE DIAMETER BY Eng. Abd El Halim Galala Design General Manager Assistance 1st issue Dated : 6.6.1985

Transcript of Flare Stack Mechanical Design Calculations

Page 1: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 1 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

ELEVATED FLARE STACK

SELF SUPPORTED & MULTIPLE DIAMETER

BY

Eng. Abd El Halim Galala

Design General Manager Assistance

1st issue Dated : 6.6.1985

Page 2: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKAccording to ASME Code, Sec. VIII, Div. 1, Edition 95, Addenda 96. Page : 2 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

ContentsPage

A. Wind Loads as Computed in Accordance with ANSI A58.1. 3

B. Allowable Shell Buckling (Compression) Stress. 5

C. Shell Plate Thickness, Design Procedure. 7

1. Total Uncrodded Stack Weight. 7

2. Computation of the Projected Area. 8

3. Computation of the Wind Loads. 9

4. Computation of the Wind Moments. 11

5. Required Shell Plate Thickness. 12

6. Anchor Bolt Chair. 13

7. Width of Base Ring. 14

8. Base Plate Thickness. 15

9. Top Plate Thickness. 15

D. Vibration Analysis. 16

1. Cantilever Vibration. 16

- Analyzing Technique. 17

- Static Deflection. 18

- Dynamic Deflection. 19

2. Ovaling Vibration. 20

- Design of Ovaling Ring : 22

- Critical Wind Velocity. 22

- Required Ring Section Modulus. 22

E. References. 24

Page 3: Flare Stack Mechanical Design Calculations
Page 4: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKAccording to ASME Code, Sec. VIII, Div. 1, Edition 95, Addenda 96. Page : 4 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

* The method of determining wind loads on vessels of two or more Table 2.

diameters is the same as for a vessel of a uniform diameter. When Vessel OD including insulation Coefficient

the conical transition section is no more than 10% of the total INCH MM Kd

height, cylindrical sections can be assumed to extend to the mid- Less than 36 1.5

hight of the conical section. 36 to 60 1.4

Otherwise, the transition section should be considered as 60 to 84 1.3

separate section. 84 to 108 1.2

over 108 1.18

For Stack material ASTM A285 Grade C

Where,

E = Modulus of elasticity of plate material @ operating temp. 27600000 PSI

Y = Yield point stress of plate material @ operating temp. 30000 PSI

St = Allowable Tensile Strength of Plate Material @ operating temp. 15000 PSI

r = Steel Density 490 lb/ft3

7850 Kg/M3

V30 = 'Wind velocity at 30 ft height. 100 MPH

C = Corrosion allowance 0.125 INCH 3.175 MM

Flare stack segment lengths, Ls

Ls1-2 50 Ft 15240 MM

Ls2-3 16.8 Ft 5120.64 MM

*Ls3-4 17 Ft 5181.6 MM

*Ls4-5 11 Ft 3352.8 MM

*Ls5-6 10 Ft 3048 MM

Ls6-7 10 Ft 3048 MM

Total vessel height 114.8 Ft 34991 MM

Figure (1)

Page 5: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 5 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

B. ALLOWABLE SHELL BUCKLING (COMPRESSION) STRESS.

Intially, some thicknesses at each section are assumed. Allowable compression stresses

at each level are determined from the following formula :

- For ta/d < 0.00425 Sc = (0.56 ta E)/d(1+0.004 E/Y)

- For higher ta/d ratios, the allowable compression stress used is that calculated for t/d = 0.00425

where ta = assumed corroded plate thickness at each level under consideration, in.

d = internal stack diameter at level under consideration, in.

Stack OD1-2 20 INCH 508 MM

Stack OD2-3 20 INCH 508 MM

Stack OD3-4 20 INCH 508 MM

Stack OD4-5 28 INCH 711.2 MM

Stack OD5-6 36 INCH 914.4 MM

Stack OD6-7 36 INCH 914.4 MM

By assuming corroded thicknesses as follows:

ta 1-2 0.166142 INCH 4.22 MM

ta2-3 0.30315 INCH 7.7 MM

ta 3-4 0.492126 INCH 12.5 MM

ta 4-5 0.307087 INCH 7.8 MM

ta 5-6 0.224409 INCH 5.7 MM

ta 6-7 0.275591 INCH 7 MM

Internal vessel dia. at each level, d 1-2 = OD1-2 - 2 ta1-2 19.66772 INCH 499.56 MM

d2-3 19.3937 INCH 492.6 MM

d 3-4 19.01575 INCH 483 MM

d 4-5 27.38583 INCH 695.6 MM

d 5-6 35.55118 INCH 903 MM

d 6-7 35.44882 INCH 900.4 MM

Since the calculated ratio, ta1-2 / d1-2 0.008447 > 0.00425

ta2-3 / d2-3 0.015631 > 0.00425

ta3-4 / d3-4 0.02588 > 0.00425

ta4-5 / d4-5 0.011213 > 0.00425

ta5-6 / d5-6 0.006312 > 0.00425

ta6-7 / d6-7 0.007774 > 0.00425

Page 6: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 6 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

The ratio ta/d to be used in calculations shall be computed as follows :

Use ta1-2 / d1-2 = Min. (Calculated value, 0.00425) 0.00425

ta2-3 / d2-3 0.00425

ta3-4 / d3-4 0.00425

ta4-5 / d4-5 0.00425

ta5-6 / d5-6 0.00425

ta6-7 / d6-7 0.00425

Therefore, the allowable buckling (compression) stress Sc shall be :

Sc = (0.56 ta E) / d(1+ 0.004 E/Y) = (ta/d) (0.56 E) / (1+ 0.004 E/Y)

Final allowable buckling (compression) stress, Sc1-2 14035.9 PSI

Sc2-3 14035.9 PSI

Sc3-4 14035.9 PSI

Sc4-5 14035.9 PSI

Sc5-6 14035.9 PSI

Sc6-7 14035.9 PSI

Page 7: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 7 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

C. SHELL PLATE THICKNESS, DESIGN PROCEDURE.

1. Total Uncrodded Stack Weights.

Weights at each level are calculated by adding corrosion allowance to the thicknesses

assumed above. [Uncorroded mean adding corrosion allowance ]

Wt1-2 = r (3.14) [OD1-22-(d1-2 - 2C)

2] Ls1-2 3067.04 lb

Wt2-3 = r (3.14) [OD2-32-(d2-3 - 2C)

2] Ls2-3 1504.943 lb

Wt3-4 = r (3.14) [OD3-42-(d3-4 - 2C)

2] Ls3-4 2173.824 lb

Wt4-5 = r (3.14) [OD4-52-(d4-5 - 2C)

2] Ls4-5 1400.718 lb

Wt5-6 = r (3.14) [OD5-62-(d5-6 - 2C)

2] Ls5-6 1331.634 lb

Wt6-7 = r (3.14) [OD6-72-(d6-7 - 2C)

2] Ls6-7 1524.498 lb

Total Weight 11002.66 lb Kg

By adding 15% of the calculated weight to compensate weight of piping, internals, platforms, ladders, etc., we get :

Wt1-2 3527.096 lb

Wt2-3 1730.685 lb

Wt3-4 2499.898 lb

Wt4-5 1610.826 lb

Wt5-6 1531.379 lb

Wt6-7 1753.173 lb

(Total Weight + 15%), Wt 12653.06 lb Kg

Page 8: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 8 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

According to ASME Code, Sec. VIII, Div. 1, Edition 95, Addenda 96. Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

2. Computation of the Projected Area, A

An approach to computing A which is often used and is recommended here is to increase the vessel

diameter D to the so-called effective stack diameter De to approximate the combined design wind load :

De = Kd [(Vessel OD + 2 insulation thk.) + (pipe OD + 2 insulation thk. + (platform + ladder)]

The coefficient Kd is given in Table 2.

The required projected area A will then equal to : A = De * Ls

where Ls = Length of the shell section in the zone of the uniform wind velocity.

De = Kd [Stack OD + Fuel Gas Pipe OD + Steam Pipe OD]

N.B. In our case, the size of fuel gas and steam pipes can be neglected.

Stack OD

INCH MM

Coefficient Kd [fromTable 2] Kd1-2 [dia. < 36"] 1.5 20 508

Kd2-3 [dia. < 36"] 1.5 20 508

Kd3-4 [dia. < 36"] 1.5 20 508

Kd4-5 [dia. < 36"] 1.5 28 711.2

Kd5-6 [dia. = 36"] 1.4 36 914.4

Kd6-7 [dia. = 36"] 1.4 36 914.4

Effective Diameter, De = Kd * Stack OD, De1-2 = Kd1-2 * OD1-2 2.5 Ft MM

De2-3 2.5 Ft MM

De3-4 2.5 Ft MM

De4-5 3.5 Ft MM

De5-6 4.2 Ft MM

De6-7 4.2 Ft

Projected Area, A = De * Height Ls A1-2 = De1-2 - Ls1-2 125 Ft2

M2

A2-3 42 Ft2

M2

A3-4 42.5 Ft2

M2

A4-5 38.5 Ft2

M2

A5-6 42 Ft2

M2

A6-7 42 Ft2

M2

Page 9: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 9 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

3. Computation of Wind Loads.

The resultant of the wind pressure load Pw over the area A is given by :

Pw = A * B * Pz

where

Pw = Wind pressure load over the projected area A, lb.

A = Windward surface area projected on the vertical plane normal to the direction of the wind, ft2.

B = Shape Factor, for round objects B = 0.6 0.6

Pz = Design wind pressure, psf, depends upon the geographical area of the job site (see Table 1).

B Pz = Min. net wind pressure, psf. For cylindrical vertical vessels :

- For L/D <= 10, BPz not less than 13 PSF

- For L/D >= 10, BPz not less than 18 PSF

where,

L is the overall tangent-to-tangent length of the vessel, 114.8 Ft 34991 MM

Davg. is the vessel average diameter.

=B451= (L1-2 D1-2 + L2-3 D2-3 + L3-4 D3-4 + L4-5 D4-5 + L5-6 D5-6 + L6-7 D6-7) / L 1.962834 Ft MM

L/Davg. 58.48686 > 10

Therefore, the net wind pressure BPz shall not be less than 18 PSF

Page 10: Flare Stack Mechanical Design Calculations

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Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

Determining Design Wind Pressure B Pz for each Segment [based upon Table 1].

Table 3 From Table 1. Segment Design

Height zone Basic height, H wind

above wind above pessure,

grade pressure, P grade Pz

M PSF M PSF

Design Wind Pressure, Pz1-2 30.722385 34.991 30.722385

20

19

Pz2-3 25.601988 19.751 25.6019875

15

14

Pz3-4 20.48159 14.6304 20.48159

10

Pz4-5 9 9.4488 15.3611925

Pz5-6 15.361193 6.096 15.3611925

Pz6-7 0 3.048 15.3611925

Net wind pressure, NWP shall be as follows :B Pz1-2 18.43343 PSF

B Pz2-3 15.36119 PSF

B Pz3-4 12.28895 PSF

B Pz4-5 9.216716 PSF

B Pz5-6 9.216716 PSF

B Pz6-7 9.216716 PSF

Use the max. following wind pressure : B Pz1-2 = Max (NWP,18) 18.43343 PSF

B Pz2-3 18 PSF

B Pz3-4 18 PSF

B Pz4-5 18 PSF

B Pz5-6 18 PSF

B Pz6-7 18 PSF

Wind Load shall be as follows : Pw = A * B Pz

Pw1-2 = A1-2 B Pz1-2 2304.179 lb Kg

Pw2-3 756 lb Kg

Pw3-4 765 lb Kg

Pw4-5 693 lb Kg

Pw5-6 756 lb Kg

Pw6-7 756 lb Kg

Page 11: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 11 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

4. Computation of Wind Moments.

In the following calculations we assumed that geographical location of

the job site does not required a moment calculation for the earthquake.

Therefore, the total wind moment shall be calculated as follows :

Figure (2)

Moment = Wind Load x Arm

M2 = Pw1-2 (0.5 L1-2) 57604.47 lb-ft

M3 =Pw1-2 (0.5 L1-2+L2-3)+Pw2-3(0.5L2-3) 102665.1 lb-ft

M4 =Pw1-2 (0.5 L1-2+L2-3+L3-4)+Pw2-3(0.5L2-3+L3-4)+ Pw3-4(0.5L3-4) 161190.6 lb-ft

M5 =Pw1-2 (0.5 L1-2+L2-3+L3-4+L4-5)+Pw2-3(0.5L2-3+L3-4+L4-5)+ Pw3-4(0.5L3-4+L4-5)+Pw4-5(0.5 L4-5) 207079.1 lb-ft

M6 =Pw1-2 (0.5 L1-2+L2-3+L3-4+L4-5+L5-6)+Pw2-3(0.5L2-3+L3-4+L4-5+L5-6)+ Pw3-4(0.5L3-4+L4-5+L5-6)+P256040.9 lb-ftM7 =Pw1-2 (0.5 L1-2+L2-3+L3-4+L4-5+L5-6+L6-7)+Pw2-3(0.5L2-3+L3-4+L4-5+L5-6+L6-7)+ Pw3-4(0.5L3-4+L 312562.7 lb-ft Table 4.

Wind Weight

Load Shear Moment @ section

W, lb Q, lb M, lb-ft WT, lb

2304.179

3527.09562

2304.1789 57604.5

756

5257.78058

3060.1789 102665

765

7757.67823

3825.1789 161191

693

9368.50446

4518.1789 207079

756

10899.8834

5274.1789 256041

756

12653.0565

Figure (3) 6030.1789 312563

Page 12: Flare Stack Mechanical Design Calculations
Page 13: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 13 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

6. Ancor Bolt Chair.

Anchor bolt material ASTM A36

Assume No. of anchor bolts, N 16 BOLTS

Bolt Circle Dia, DBC 43.93701 INCH 1116 MM

Max. Allowable stress of Anchor Bolt Material, SB 15000 PSI

The total tension in each anchor bolt is determined from the relationship:

WB = (48 M / N DBC) - Wt / N 20550.83 lb Kg

Thus, the anchor bolt area required at the root of the thread shall be:

AB = WB / SB 1.370055 INCH2

883.905 MM2

Diameter of the anchor bolt at the root of thread, D = (4 AB/3.14)0.5

1.320761 INCH 33.5473 MM

Use 16 holding down bolts with a dia. of , d 1.75 INCH 44.45 MM

Each bolt shall be provided with two hex heavy nuts and washer.

- Length of threaded portion, l INCH 150 MM

- Radius, R INCH 90 MM

- Length, L INCH 350 MM

- Bolt projection INCH MM

- Total length, M INCH 1085 MM

Figure (4) Figure (5)

Page 14: Flare Stack Mechanical Design Calculations

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Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

7. Width of Base Ring, C.

Assume width of base ring, C 11.10236 INCH 282 MM

Bearing pressure on concrete foundation is calculated from

the following formula :

Pb = (48 M / PI Db2 C) + (Wt / 3.14 Db C) 341.9775 PSI < 500

SAFE

where Db = OD at bottom of stack 36 INCH 914.4 MM

Assume C, and note that the value of Pb is limited to :

- For 3000 lb concrete 750 PSI (Max.)

- For 2000 lb concrete 500 PSI (Max.)

N.B. If the calculated Pb exceeds the above limit, the value of C is modified

so that Pb falls within the allowable limit.

Page 15: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 15 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

8. Base Plate Thickness, Tb

Base plate thickness Tb is calculated from the following equation:

Tb = e SQRT(3 Pb / 20000) 1.480195 INCH 37.5969 MM

where e = A + B 6.535433 INCH 166 MM

A 101 MM

B 65 MM

Use Tb 1.771654 INCH 45 MM

Figure (6)

9. Top Plate Thickness, TT

TT = SQRT[ 3 * WB * 6 / (4 * 20000 * e)] 0.841141 INCH 21.365 MM

where WB = Total tension in each bolt 20550.83 PSI

Use TT 1.181102 INCH 30 MM

Page 16: Flare Stack Mechanical Design Calculations

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Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

D. VIBRATION ANALYSIS.

1. Cantilever vibration.

The following criteria is used to establish need for vibration analysis of stacks with Lc/L ratio not

exceeding 0.5 :

- W / L Dr2 <= 20 vibration analysis must be performed 9.443917 < 20 vibration analysisis required

- 20 < W / L Dr2 <= 25 vibration analysis should be performed

- 25 < W / L Dr2 vibration analysis need not be performed

Where Wt = Total corroded stack weight (see next page). 8071.981 lb

Le = Total length of stack. 114.8 ft

Dr = Average internal dia. of top half of stack. 2.72862 ft

Lc = Total length of conical section(s) of stack. 4.002625 ft

Conical section height 28"/20" 2.001312 ft 610 MM

Conical section height 36"/28" 2.001312 ft 610 MM

We note that Lc / L < 0.5 0.034866 OK

O.D. Stack OD1-2 20 INCH 508 MM

Stack OD2-3 20 INCH 508 MM

Stack OD3-4 20 INCH 508 MM

Stack OD4-5 28 INCH 711.2 MM

Stack OD5-6 36 INCH 914.4 MM

Stack OD6-7 36 INCH 914.4 MM

Corroded thickness tr1-2 0.189961 INCH 4.825 MM

Corroded thickness tr2-3 0.308071 INCH 7.825 MM

Corroded thickness tr3-4 0.504921 INCH 12.825 MM

Corroded thickness tr4-5 0.347441 INCH 8.825 MM

Corroded thickness tr5-6 0.229331 INCH 5.825 MM

Corroded thickness tr6-7 0.308071 INCH 7.825 MM

Page 17: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 17 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

Corroded internal diameter in inches : Corroded ID1-2 19.62008 INCH

Corroded ID2-3 19.38386 INCH

Corroded ID3-4 18.99016 INCH

Corroded ID4-5 27.30512 INCH

Corroded ID5-6 35.54134 INCH

Corroded ID6-7 35.38386 INCH

Flare stack segment heights, L1-2 50 Ft 15240 MM

L2-3 16.8 Ft 5120.64 MM

L3-4 17 Ft 5181.6 MM

L4-5 11 Ft 3352.8 MM

L5-6 10 Ft 3048 MM

L6-7 10 Ft 3048 MM

Total Corroded Stack Weights.

Weights at each level are calculated, without taking into account adding

corrosion allowance to the thicknesses assumed above.

Corroded mean neglecting corrosion allowance.

Wt1-2 = r (PI/4) [do2-di

2]1-2 L1-2 2011.418 lb 912.365 Kg

Wt2-3 = r (PI/4) [do2-di

2]2-3 L2-3 1089.511 lb 494.194 Kg

Wt3-4 = r (PI/4) [do2-di

2]3-4 L3-4 1788.879 lb 811.423 Kg

Wt4-5 = r (PI/4) [do2-di

2]4-5 L4-5 1129.776 lb 512.459 Kg

Wt5-6 = r (PI/4) [do2-di

2]5-6 L5-6 876.9458 lb 397.776 Kg

Wt6-7 = r (PI/4) [do2-di

2]6-7 L6-7 1175.45 lb 533.176 Kg

Total corroded stack Weight, Wt 8071.981 lb 3661.39 Kg

Analyzing technique.

Period of vibration is determined as follows :

T = 1.648 (Le2) / Dr E

0.51.515107 second

'where Le = effective length of stack 114.8 ft

Natural frequency of stack vibration, f = 1 / T 0.660019 cps

Critical wind velocity, Vc = 3 f Dr 5.402825 MPH

Page 18: Flare Stack Mechanical Design Calculations
Page 19: Flare Stack Mechanical Design Calculations

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Project : Design & procurement of Flare Stack Date : 4.4.2000

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Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

Dynamic deflection.

At a critical wind velocity, the structure vibrates at resonant frequency, and thus the amplitude of

vibration is magnified greatly. The dynamic coefficient, which is a ratio of dynamic amplitude to static

amplitude, is called the magnification factor. This is a function of the lining, stiffness of the soil and

several other factors. The amount of static deflection must be multiplied by the magnification factor

to determine dynamic deflection. Approximate value of magnification factors for different types of stacks

as suggested by DeGhetto and Long are listed in Table 3.

Table 5. Magnification factors

Types of Spread Spread Piled

stacks footings footings foundations

on soft soil on medium s and spread

(Bearing < (1500 psi < footings

1500 psi) Bearing > on stiff soil

3000 psi) and rocks

Lined

stacks 5 30 50

Unlined

stacks 30 60 90

Using a magnification factor of 30

Dynamic deflection = Static Deflection * Magnification factor Allowed deflection

= Ds * Magnification factor 9.110085 INCH > 8.036

NotT Good

N.B. For dynamic deflection, It is assumed to be within the allowable limits

when allowing about 7-inch deflection per 100 feet* of height of stack.

* "Shortcut method for calculating tower deflection", Hydrocarbon Processing 47. No. 11, Nov. 1968, p 230.

Allowed deflection of stack under consideration = 7 x L / 100 8.036 INCH

Page 20: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 20 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

2. Ovaling vibration.

Natural frequency of the free ring is given by :

fr = (7.58 tr E0.5

) / 60 D2

Vortex shedding frequency is given by : fv = 0.2 V / D

Where V = wind velocity for vortex shedding is 45 MPH 45 MPH

or 66 fps as recommended by Dickey and 66 fps

Woodruff for most economical and safe stack

design as far as vibration is concerned.

Both these frequencies should be calculated at each level using the corresponding thicknesses and diameters.

Corroded internal diameters in feet, D D1-2 1.635007 Ft 498.35 MM

D2-3 1.615322 Ft 492.35 MM

D3-4 1.582513 Ft 482.35 MM

D4-5 2.275427 Ft 693.55 MM

D5-6 2.961778 Ft 902.75 MM

D6-7 2.948655 Ft 898.75 MM

At Section 1-2 : fr1-2 = (7.58 tr1-2 E0.5

) / 60 D2

1-2 47.16253 cps cps = cycle per second

fv1-2 = 0.2 V / D1-2 8.073362 cps

2 fv1-2 16.14672 cps

Since fr > 2 fv , no ovaling rings are required, and the stack is free from ovaling vibration.

N.B. t calculated upon corroded thk. & V = 66 fps.

At Section 2-3 : fr2-3 = (7.58 tr2-3 E0.5

) / 60 D2

2-3 78.36194 cps

fv2-3 = 0.2 V / D2-3 8.171748 cps

2 fv2-3 16.3435 cps

Since fr > 2 fv , no ovaling rings are required, and the stack is free from ovaling vibration.

At Section 3-4 : fr3-4 = (7.58 tr3-4 E0.5

) / 60 D2

3-4 133.814 cps

fv3-4 = 0.2 V / D3-4 8.341163 cps

2 fv3-4 16.68233 cps

Since fr > 2 fv , no ovaling rings are required, and the stack is free from ovaling vibration.

At Section 4-5 : fr4-5 = (7.58 tr4-5 E0.5

) / 60 D2

4-5 44.53771 cps

fv4-5 = 0.2 V / D4-5 5.80111 cps

2 fv4-5 11.60222 cps

Since fr > 2 fv , no ovaling rings are required, and the stack is free from ovaling vibration.

Page 21: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 21 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

At Section 5-6 : fr5-6 = (7.58 tr5-6 E0.5

) / 60 D2

5-6 17.3512 cps

fv5-6 = 0.2 V / D5-6 4.456782 cps

2 fv5-6 8.913564 cps

Since fr > 2 fv , no ovaling rings are required, and the stack is free from ovaling vibration.

At Section 6-7 : fr6-7 = (7.58 tr6-7 E0.5

) / 60 D2

6-7 23.51664 cps

fv6-7 = 0.2 V / D6-7 4.476618 cps

2 fv6-7 8.953235 cps

Since fr > 2 fv , no ovaling rings are required, and the stack is free from ovaling vibration.

Page 22: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 22 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

Design of Ovaling Rings.

If, at any section, fr < 2fv, ovaling rings are required to stiffen that section.

Section modulus of the rings, whenever required, can be determined as follows :

- Critical wind velocity at the section under consideration is :

Vo = ( 60 fr D ) / 2 S FPM

where fr = Natural frequency cps

S = Strouhal number, is 0.2 over a wide range of 0.2

Reynolds numbers.

D = Intenal vessel dia. (corroded) at level under consideration. Ft

Critical wind velocity at Section, Vo1-2 = ( 60 fr1-2 D1-2 ) / 2 S 11566.66 FPM

Vo2-3 = ( 60 fr2-3 D2-3 ) / 2 S 18986.96 FPM

Vo3-4 = ( 60 fr3-4 D3-4 ) / 2 S 31764.36 FPM

Vo4-5 = ( 60 fr4-5 D4-5 ) / 2 S 15201.34 FPM

Vo5-6 = ( 60 fr5-6 D5-6 ) / 2 S 7708.563 FPM

Vo6-7 = ( 60 fr6-7 D6-7 ) / 2 S 10401.37 FPM

Required Section Modulus of the Ring.

Now, the section modulus of stiffeners at section under consideration can be found from the formula

as used by Moody :

Sm = [ (7)10-7

(Vo)2 D

2 (Hr) ] / St INCH

3

Where, Vo = Critical wind velocity at section of consideration FPM

Hr = Spacing throughout the length of the section under considerat0.5 Ls Ft

St = Allowable tensile strength of stiffener material 15000 PSI

Sm1-2 = [ (7)10-7

(Vo1-2)2 D1-2

2 Hr1-2) ] / St 0.417255 INCH

3

Sm2-3 = [ (7)10-7

(Vo2-3)2 D2-3

2 Hr2-3) ] / St 0.368735 INCH

3

Sm3-4 = [ (7)10-7

(Vo3-4)2 D3-4

2 Hr3-4) ] / St 1.002306 INCH

3

Sm4-5 = [ (7)10-7

(Vo4-5)2 D4-5

2 Hr4-5) ] / St 0.307085 INCH

3

Sm5-6 = [ (7)10-7

(Vo5-6)2 D5-6

2 Hr5-6) ] / St 0.121627 INCH

3

Sm6-7 = [ (7)10-7

(Vo6-7)2 D6-7

2 Hr6-7) ] / St 0.219485 INCH

3

Stiffeners having section modulus equal to or greater than Sm should be provided at spacing

Hr throughout the length of the section under consideration. If stiffeners are required for more

than one section, different size and spacing should be used for economy, if possible.

Page 23: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKPage : 23 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

Notes

Page 24: Flare Stack Mechanical Design Calculations

DESIGN CALCULATIONS OF ELEVATED CYLINDRICAL FLARE STACKAccording to ASME Code, Sec. VIII, Div. 1, Edition 95, Addenda 96. Page : 24 of 24

Designed by : Eng. Abdel Halim Galala, Design General Manager (Assistant) REV. : 0

Project : Design & procurement of Flare Stack Date : 4.4.2000

Job Name : Propylene Recovery Unit Location : Gulf of Seuz

Dwg. No. : Client : ABB/OPC

Stack Type : Self supported & Multiple Diameter Item : X-06-02

E. REFERENCES.

1. ANSI A58.1-1955.

2. ASCI 7-1988.

3. Pressure Vessel Design Handbook-2nd Edition, by Henry H. Bednar.

4. Flare stack paper research.

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