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IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 
__________________________________________________________________________________________ 
Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 972 
OPTIMIZATION OF LOCATION AND SIZE OF OPENING IN A PRESSURE VESSEL CYLINDER FOR SPHERICAL AND ELLIPTICAL HEAD Jagadishkumar1, Srikumar Biradar2, Balaji V3 1PG student Department of Mechanical Engg, Vijay vittala institute of technology, Bangalore 2Asst professor, Department of Mechanical Engg, Vijay vittala institute of technology, Bangalore 3Lecture, Department of Mechanical Engg Shirdi Sai Engg College Bangalore Abstract Pressure vessel cylinders find wide applications in thermal and nuclear power plants, process and chemical industries, in space and ocean depths, and fluid supply systems in industries. The failure of pressure vessel may result in loss of life, health hazards and damage of property. In addition to the pressure, the pressure vessels area also subjected to support loads that may be steady or variable, piping reactions, and thermal shocks which require an overall knowledge of the stresses imposed by these conditions on various vessel shapes and appropriate design means to ensure safe and long life. Basic considerations in the design of pressure vessel include recognition of most likely modes of failure, stresses induced due to temperature and pressure, selection of suitable material capable of withstanding the effects of pressure and thermal loads and effects of environment and effect of concentration of stresses. In the present work, emphasis is on effect of stress concentration. It will be shown that an appropriate location and size of the opening in a pressure vessel results in minimizing the stresses induced due to the stress concentration resulting from the end flanges and other attachments. In this present work we also design and optimize the spherical and elliptical head profile with hole on the head, also Analysis the above profiles for various stress parameter. 
-----------------------------------------------------------------------***---------------------------------------------------------------------- 1. INTRODUCTION The term pressure vessel referred to those reservoirs or containers, which are subjected to internal or external pressures. The pressure vessels are used to store fluids under pressure. The fluid being stored may undergo a change of state inside the pressure vessels as in case of steam boilers or it may combine with other reagents as in chemical plants. Pressure vessels find wide applications in thermal and nuclear power plants, process and chemical industries, in space and ocean depths, and in water, steam, gas and air supply system in industries. The material of a pressure vessel may be brittle such as cast iron, or ductile such as mild steel. 1.1 High Pressure Vessels 
High Pressure vessels are used as reactors, separators and heat exchangers. They are vessel with an integral bottom and a removable top head, and are generally provided with an inlet, heating and cooling system and also an agitator system. High Pressure vessels are used for a pressure range of 15 N/mm2 to a maximum of 300 N/mm2. These are essentially thick walled cylindrical vessel, ranging in size from small tubes to several meters diameter. Both the size of the vessel and the pressure involved will dictate the type of construct 
1.2 Few Methods of Construction of Pressure Vessels. 
1. A solid wall vessel produced by forging or boring a solid rod of metal. 
2. A cylinder formed by bending a sheet of metal with longitudinal weld. 
3. Shrink fit construction in which, the vessel is built up of two or more concentric shells, each shell progressively shrunk on from the inside outward. From economic and fabrication considerations, the number of shells should be limited to two. 
4. A vessel built up by wire winding around a central cylinder. The wire is wound under tension around a cylinder of about 6 to 10 mm thick. 
5. A vessel built up by wrapping a series of sheets of relatively thin metal tightly round one another over a core tube, and holding each sheet with a longitudinal weld. Rings are inserted in the ends to hold the inner shell round while subsequent layers are added. The
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 
__________________________________________________________________________________________ 
Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 973 
liner cylinder generally up to12 mm thick, while the 
subsequent layers are up to 6 mm thick. 
In designing high pressure vessels, the main factors to be 
considered are: 
 Dimensions – Diameter, length, and their limitations. 
 Operating conditions – Pressure and temperature. 
 Available materials and their physical 
properties and cost. 
 Corrosive nature of reactants and products. 
 Theories of failure. 
 Types of construction i.e. forged, welded or 
casted. 
 Method of fabrication 
 Fatigue, Brittle failure and Creep. 
 Economic considerations. 
1.3 Design of Solid Walled Pressure Vessel 
A solid wall vessel consists of a single cylindrical shell, with 
closed ends. Due to high internal pressure and large thickness 
the shell is considered as a „thick‟ cylinder. In general, the 
physical criteria are governed by the ratio of diameter to wall 
thickness and the shell is designed as thick cylinder, if its wall 
thickness exceeds one-tenth of the inside diameter. 
Drawing of solid wall pressure vessel 
Design Pressure -21 N/mm2, 
Design Temperature T-200C 
Design Cod -ASME Sec.VIII 
Division-1 
Inside Radius of vessel Ri-1143 mm 
Inside Diameter of vessel, I - 2286 mm 
Joint EfficiencyJ-1 
Safety FactorF.S-4 
Corrosion Allowance, C.A-3.0 mm 
Allowable Stress: 123 N/mm2 
1.4 Material of Construction 
Description Material UTS(MPa) YS MPa 
Vessel SA515GR70 492.9 267.6 
Dished Ends SA 515GR70 492.9 267.6 
2. CALCULATION 
2.1. Thickness 
The thickness of the Vessel is calculated from the equation 
t=219mm 
2.2 Design of Hemispherical Dished End 
The thickness of the dished end is given by 
= 102.26 mm 
2.3 Calculation of Hydrostatic Test Pressure (In 
Horizontal Position) 
The hydrostatic pressure is taken as 1.3 times the design 
pressure. 
= 1.3 * 21 
= 27.3 N/mm2 
2.4 Stress Developed During Hydrostatic Test: 
2.4.1 In Vessel 
The Stress developed inside the vessel is calculated from the 
equation, 
-1] C.A 
(SJ - P) 
(S J P) 
t R [ i  
 
 
-1] 3.0 
(123 x 1 - 21) 
(123 x 1 21) 
t 1143 [  
 
 
C.A 
2 S J 0.2 P 
P R 
t 
i 
d  
 
 
3.0 
2 x 123 x 1.0 0.2 x 21 
21 x 1143 
t d  
 
 
P 1.3x Design Pressure H  
-1] 
(SJ - P) 
(S J P) 
t R [ i 
 

IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 
__________________________________________________________________________________________ 
Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 974 
S = 157.33 N/mm2 
The stress developed (157.33 N/mm2) is less than the 
allowable stress value (267.6N/mm2) 
2.4.2 In Dished End 
The Stress developed inside the Dish is given by the equation, 
= 73.97 N/mm2 
The stress developed (73.97 N/mm2) is less than the allowable 
stress value (267.6N/mm2) 
3. DESIGN OF ELLIPTICAL HEAD 
PARAMETERS 
ASME design equation for elliptical head 
t=PDK/(2SE-0.2P) 
Thickness of elliptical head=t in mm 
P=design pressure in N/mm2 
D=outer diameter in mm 
Design Pressure (P) =21 N/mm2 
Allowable Stress value(S) =123 N/mm2 
Joint Efficiency (E) =1 
Stress concentration factor (k) =1/6 [2+(〖a/b)〗^2 ] 
Major axis length (a) =2724mm 
Minor axis length (b) =771.34mm 
k=1/6 [2+(〖2724/771.34)〗^2 ]=0.62 
t=(21×2724)/(2×123×1-0.2×21)=146.67≈147 
Hoop stress (σ_t1) =(P×D)/(2×t) 
= (21×2724)/(2×147) =195 mpa 
Longitudinal stress (σ_t2) =(P×D)/(4×t)=(21×2724)/(4×147)= 
97MPa 
3.1 3D Models 
Elliptical head with no hole Eliipitical head with hole 
-1] 
(S*1.0 - 27.3) 
(S *1.0 27.3) 
219 1143 [ 
 
 
2 * t 
P R 0.2 P t 
S H i H 
Hd 
 
 
2 x 219 
27.3 x 1143 0.2 x 27.3 x 219 
S 
HD 
 

IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 
__________________________________________________________________________________________ 
Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 975 
Spherical head without hole spherical head with hole 3.2 Analysis of Pressure Vessel Displacement Stress Strain Elliptical head without hole Displacement Stress Strain Elliptical head with hole
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 
__________________________________________________________________________________________ 
Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 976 
Displacement Stress Strain Spherical head without hole Displacement Stress Strain Spherical head with hole NOTE : Similar Analysis can done by changing the different location and different size of the hole and there result as shown 3.3 Changing Distances and Diameters (Spherical And Elliptical) 
500mm DIA, DISTANCE- 500mm 
DIA 400mm, DISTANCE- 400mm 
450mm DIA, DISTANCE- 350mm 
Displacement (mm) 
11.682 
6.146 
7.367 
Stress (N/mm2) 
499.219 
619.242 
661.739 
Strain 
0.003401 
0.004317 
0.004583 
550mm DIA, DISTANCE- 700mm 
500mm DIA, DISTANCE- 750mm 
DIAMETER-450mm, DISTANCE- 350mm 
Displacement (mm) 
17.494 
15.246 
14.411 
Stress (N/mm2) 
1349 
1208 
907.861 
Strain 
0.009381 
0.008418 
0.006356
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 
__________________________________________________________________________________________ 
Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 977 
4. CONCLUSIONS 
 In this project, a pressure vessel is designed according to the company specifications. 3D modelling is done in Pro/Engineer. The pressure vessel head used is in the shape of elliptical head without hole. In this we are replacing with spherical head and also by taking holes. 
 Analysis is done on the pressure vessel to verify the strength. Analysis is done for elliptical and spherical heads, without and with holes and also by changing the diameters and distances of hole. 
 By observing the analysis results of without and with holes, for the spherical head without hole less stress is developed. 
 The spherical head with hole diameter of 500mm and distance of 500mm is better since the stress value is less when compared with other parameters 
 Thermal analysis is done on the optimized pressure vessel to determine the heat transfer rates. The heat transfer rate is 9.313W/mm2. 
REFERENCES 
[1] Brownell and Young, “Process Equipment Design” Seely, F.B., and Smith, 
[2] John F.Henvey “ Pressure Vessel Design -Nuclear and Chemical Applications” An East-west Edition, Newyork 
[3] Henry H.Bednar “ Pressure Vessel Code Book” 
[4] Fratcher, G.E : New alloys for Multilayer Vessels” Vol 33 
[5] Harold.H.Wait e, “Pressure Vessel and Piping Design Analysis” 
[6] Mc Cabe, J.S and Rothrock, E.W., “ Multilayer Vessels for High Pressure,” ASME Mechanical Engineering PP 34-39. 
[7] Mc Cabe, J.S and Rothrock, E.W., “ Recent Developments in Multilayer Vessels,” British chemical engineering Vol.16, No6,1971 
[8] Noel, M.R., “Multiwall Pressure Vessels,” British chemical Engineering Vol.15, No7,1970. 
[9] O.C.Zienkeewz.”The Finite Element Method in Structural and Continuum Mechanics. 
[10] R.S.Khurmi and J.K.Gupta., “A Test Book of Machine Design” S.Chand publications. 
[11] Ansys User‟s Manual, Swanson Anlysis Systems, Inc.1995.

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Optimization of location and size of opening in a pressure vessel cylinder for spherical and elliptical head

  • 1. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 972 OPTIMIZATION OF LOCATION AND SIZE OF OPENING IN A PRESSURE VESSEL CYLINDER FOR SPHERICAL AND ELLIPTICAL HEAD Jagadishkumar1, Srikumar Biradar2, Balaji V3 1PG student Department of Mechanical Engg, Vijay vittala institute of technology, Bangalore 2Asst professor, Department of Mechanical Engg, Vijay vittala institute of technology, Bangalore 3Lecture, Department of Mechanical Engg Shirdi Sai Engg College Bangalore Abstract Pressure vessel cylinders find wide applications in thermal and nuclear power plants, process and chemical industries, in space and ocean depths, and fluid supply systems in industries. The failure of pressure vessel may result in loss of life, health hazards and damage of property. In addition to the pressure, the pressure vessels area also subjected to support loads that may be steady or variable, piping reactions, and thermal shocks which require an overall knowledge of the stresses imposed by these conditions on various vessel shapes and appropriate design means to ensure safe and long life. Basic considerations in the design of pressure vessel include recognition of most likely modes of failure, stresses induced due to temperature and pressure, selection of suitable material capable of withstanding the effects of pressure and thermal loads and effects of environment and effect of concentration of stresses. In the present work, emphasis is on effect of stress concentration. It will be shown that an appropriate location and size of the opening in a pressure vessel results in minimizing the stresses induced due to the stress concentration resulting from the end flanges and other attachments. In this present work we also design and optimize the spherical and elliptical head profile with hole on the head, also Analysis the above profiles for various stress parameter. -----------------------------------------------------------------------***---------------------------------------------------------------------- 1. INTRODUCTION The term pressure vessel referred to those reservoirs or containers, which are subjected to internal or external pressures. The pressure vessels are used to store fluids under pressure. The fluid being stored may undergo a change of state inside the pressure vessels as in case of steam boilers or it may combine with other reagents as in chemical plants. Pressure vessels find wide applications in thermal and nuclear power plants, process and chemical industries, in space and ocean depths, and in water, steam, gas and air supply system in industries. The material of a pressure vessel may be brittle such as cast iron, or ductile such as mild steel. 1.1 High Pressure Vessels High Pressure vessels are used as reactors, separators and heat exchangers. They are vessel with an integral bottom and a removable top head, and are generally provided with an inlet, heating and cooling system and also an agitator system. High Pressure vessels are used for a pressure range of 15 N/mm2 to a maximum of 300 N/mm2. These are essentially thick walled cylindrical vessel, ranging in size from small tubes to several meters diameter. Both the size of the vessel and the pressure involved will dictate the type of construct 1.2 Few Methods of Construction of Pressure Vessels. 1. A solid wall vessel produced by forging or boring a solid rod of metal. 2. A cylinder formed by bending a sheet of metal with longitudinal weld. 3. Shrink fit construction in which, the vessel is built up of two or more concentric shells, each shell progressively shrunk on from the inside outward. From economic and fabrication considerations, the number of shells should be limited to two. 4. A vessel built up by wire winding around a central cylinder. The wire is wound under tension around a cylinder of about 6 to 10 mm thick. 5. A vessel built up by wrapping a series of sheets of relatively thin metal tightly round one another over a core tube, and holding each sheet with a longitudinal weld. Rings are inserted in the ends to hold the inner shell round while subsequent layers are added. The
  • 2. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 973 liner cylinder generally up to12 mm thick, while the subsequent layers are up to 6 mm thick. In designing high pressure vessels, the main factors to be considered are:  Dimensions – Diameter, length, and their limitations.  Operating conditions – Pressure and temperature.  Available materials and their physical properties and cost.  Corrosive nature of reactants and products.  Theories of failure.  Types of construction i.e. forged, welded or casted.  Method of fabrication  Fatigue, Brittle failure and Creep.  Economic considerations. 1.3 Design of Solid Walled Pressure Vessel A solid wall vessel consists of a single cylindrical shell, with closed ends. Due to high internal pressure and large thickness the shell is considered as a „thick‟ cylinder. In general, the physical criteria are governed by the ratio of diameter to wall thickness and the shell is designed as thick cylinder, if its wall thickness exceeds one-tenth of the inside diameter. Drawing of solid wall pressure vessel Design Pressure -21 N/mm2, Design Temperature T-200C Design Cod -ASME Sec.VIII Division-1 Inside Radius of vessel Ri-1143 mm Inside Diameter of vessel, I - 2286 mm Joint EfficiencyJ-1 Safety FactorF.S-4 Corrosion Allowance, C.A-3.0 mm Allowable Stress: 123 N/mm2 1.4 Material of Construction Description Material UTS(MPa) YS MPa Vessel SA515GR70 492.9 267.6 Dished Ends SA 515GR70 492.9 267.6 2. CALCULATION 2.1. Thickness The thickness of the Vessel is calculated from the equation t=219mm 2.2 Design of Hemispherical Dished End The thickness of the dished end is given by = 102.26 mm 2.3 Calculation of Hydrostatic Test Pressure (In Horizontal Position) The hydrostatic pressure is taken as 1.3 times the design pressure. = 1.3 * 21 = 27.3 N/mm2 2.4 Stress Developed During Hydrostatic Test: 2.4.1 In Vessel The Stress developed inside the vessel is calculated from the equation, -1] C.A (SJ - P) (S J P) t R [ i    -1] 3.0 (123 x 1 - 21) (123 x 1 21) t 1143 [    C.A 2 S J 0.2 P P R t i d    3.0 2 x 123 x 1.0 0.2 x 21 21 x 1143 t d    P 1.3x Design Pressure H  -1] (SJ - P) (S J P) t R [ i  
  • 3. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 974 S = 157.33 N/mm2 The stress developed (157.33 N/mm2) is less than the allowable stress value (267.6N/mm2) 2.4.2 In Dished End The Stress developed inside the Dish is given by the equation, = 73.97 N/mm2 The stress developed (73.97 N/mm2) is less than the allowable stress value (267.6N/mm2) 3. DESIGN OF ELLIPTICAL HEAD PARAMETERS ASME design equation for elliptical head t=PDK/(2SE-0.2P) Thickness of elliptical head=t in mm P=design pressure in N/mm2 D=outer diameter in mm Design Pressure (P) =21 N/mm2 Allowable Stress value(S) =123 N/mm2 Joint Efficiency (E) =1 Stress concentration factor (k) =1/6 [2+(〖a/b)〗^2 ] Major axis length (a) =2724mm Minor axis length (b) =771.34mm k=1/6 [2+(〖2724/771.34)〗^2 ]=0.62 t=(21×2724)/(2×123×1-0.2×21)=146.67≈147 Hoop stress (σ_t1) =(P×D)/(2×t) = (21×2724)/(2×147) =195 mpa Longitudinal stress (σ_t2) =(P×D)/(4×t)=(21×2724)/(4×147)= 97MPa 3.1 3D Models Elliptical head with no hole Eliipitical head with hole -1] (S*1.0 - 27.3) (S *1.0 27.3) 219 1143 [   2 * t P R 0.2 P t S H i H Hd   2 x 219 27.3 x 1143 0.2 x 27.3 x 219 S HD  
  • 4. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 975 Spherical head without hole spherical head with hole 3.2 Analysis of Pressure Vessel Displacement Stress Strain Elliptical head without hole Displacement Stress Strain Elliptical head with hole
  • 5. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 976 Displacement Stress Strain Spherical head without hole Displacement Stress Strain Spherical head with hole NOTE : Similar Analysis can done by changing the different location and different size of the hole and there result as shown 3.3 Changing Distances and Diameters (Spherical And Elliptical) 500mm DIA, DISTANCE- 500mm DIA 400mm, DISTANCE- 400mm 450mm DIA, DISTANCE- 350mm Displacement (mm) 11.682 6.146 7.367 Stress (N/mm2) 499.219 619.242 661.739 Strain 0.003401 0.004317 0.004583 550mm DIA, DISTANCE- 700mm 500mm DIA, DISTANCE- 750mm DIAMETER-450mm, DISTANCE- 350mm Displacement (mm) 17.494 15.246 14.411 Stress (N/mm2) 1349 1208 907.861 Strain 0.009381 0.008418 0.006356
  • 6. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Special Issue: 03 | May-2014 | NCRIET-2014, Available @ http://www.ijret.org 977 4. CONCLUSIONS  In this project, a pressure vessel is designed according to the company specifications. 3D modelling is done in Pro/Engineer. The pressure vessel head used is in the shape of elliptical head without hole. In this we are replacing with spherical head and also by taking holes.  Analysis is done on the pressure vessel to verify the strength. Analysis is done for elliptical and spherical heads, without and with holes and also by changing the diameters and distances of hole.  By observing the analysis results of without and with holes, for the spherical head without hole less stress is developed.  The spherical head with hole diameter of 500mm and distance of 500mm is better since the stress value is less when compared with other parameters  Thermal analysis is done on the optimized pressure vessel to determine the heat transfer rates. The heat transfer rate is 9.313W/mm2. REFERENCES [1] Brownell and Young, “Process Equipment Design” Seely, F.B., and Smith, [2] John F.Henvey “ Pressure Vessel Design -Nuclear and Chemical Applications” An East-west Edition, Newyork [3] Henry H.Bednar “ Pressure Vessel Code Book” [4] Fratcher, G.E : New alloys for Multilayer Vessels” Vol 33 [5] Harold.H.Wait e, “Pressure Vessel and Piping Design Analysis” [6] Mc Cabe, J.S and Rothrock, E.W., “ Multilayer Vessels for High Pressure,” ASME Mechanical Engineering PP 34-39. [7] Mc Cabe, J.S and Rothrock, E.W., “ Recent Developments in Multilayer Vessels,” British chemical engineering Vol.16, No6,1971 [8] Noel, M.R., “Multiwall Pressure Vessels,” British chemical Engineering Vol.15, No7,1970. [9] O.C.Zienkeewz.”The Finite Element Method in Structural and Continuum Mechanics. [10] R.S.Khurmi and J.K.Gupta., “A Test Book of Machine Design” S.Chand publications. [11] Ansys User‟s Manual, Swanson Anlysis Systems, Inc.1995.