Tanques Atmosféricos API 650

8/11/2019 Tanques Atmosfricos API 650

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API 620

DATA SHEET: ATMOSPHERICAL TANK API 620 - FT BY FT METH.

1-Fluid:Product: Water

Cp (cal/gr C) 0.238

Vapor Pressure @ 200 F, psia 11.53SG 1

Viscosity @ 130 F (centistokes) 0.55

PM 18

@ 200 F (lbm/pie3) 60.13

2-Tank Size:Nominal Diameter 35 ft (10,7 meters)

Nominal Heigth 40 ft (12,2 meters)

Lquido Heigth 39 ft (11,9 meters)

Nominal Capacity 1000 cubic meters

3-Tuberias asociadas al Tanque:

Nozzle Service CantN1 Water inlet 1

N2 Service Water Oulet 1

N3 fire fighting Water Oulet 1

N6 Fire Fighting water recirculation inlet 1

N4 Venting 1

N5 Manhole 2

N8 Rebose 1

N7 Drenaje 1

N9 A/B Stand Pipe 2

N10 Low Level Sw 1TOTALS =

4-Datos de Operacion:Desgin Temperature, T1 200F (93 C)

Desging Pressure (ft Water Column) 492

Atmospherical Pressure (Psia) 14.7

Altitude (m.s.n.m.) 350

Inlet Pressure at N1 (Psig)

Inlet Flow at N1 (GPM)

Maximul Allowed Velocity at N1 (m/seg)

5-Nozzles and Conections:

Nozzle Service CantN1 Water inlet 1

N2 Service Water Oulet 1

N3 fire fighting Water Oulet 1

N6 Fire Fighting water recirculation inlet 1

N4 Venting 1

N5 Manhole 2

N8 Overflow Nozzle 1

N7 Drainage Nozzle 1

N9 A/B Stand Pipe 2

N10 Low Level Sw 1


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Original File: Archivo: Mdulo 14.xlsNewFile:

Original Date: 7/30/2004New Date: 4/7/2008

Original Autor: LRRJTraslation: [email protected]

Diameter (inch) Schedule Length (m) Weigh (lb) Weigh (kg) Material8 40

4 40

16 40

8 40

12 40

24

10 40

4 40

2

2 0.00 0.00

Diameter (inch) Weigh (lb) Weigh (kg) Material8 48.50 31.75 A-105

4 20.00 9.07 A-105

16 173.00 78.47 A-105

8 48.50 22.00 A-105

12 100.00 45.35 A-105

24 662.00 300.27 A-105

10 70.00 31.75 A-105

4 20.00 9.07 A-105

2 15.00 6.80 A-105

2 7.50 3.40 A-105
mailto:[email protected]:[email protected]


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1164.50 537.93


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API 620Write input Data Only on not colored cells

Module 14CALCULATIONS

GENERAL DATA

PdDesign Pressure ftwc= Height of the tank (full of water) + 12 ftwc (ft of

water column)396.00

Td Design Temperature, C 93.00D Diameter of the Tank, feet 60.00H Height of the Tank (Calculations Limits = 80 ft), feet 32.00G specific Gravity of the Stored Fluid (Water=1) 1.00Sd Allowable Working stress at Designs conditions, Psi 23,200.00

C.A. Corrosion thickness, inch 0.0625

Angle of Inclination of the Roof with regard to the horizontal one, degrees25.00

CAPt Capacity needed of the Tank, cubic metersSTANDARD SHEET

LENGTH Length of the sheet, feet 20.00WIDTH Width of the sheet, feet 8.00

AREA STD S: Area of Standard Sheet, m2 14.86

DENSITY Density of the Sheet of Steel, Kg/m3 7,901.42

THICKNESS WALLS SHEETRings= Number of Rings with Standard Sheets 4

Aa= Area of A Ring, m2 140.09NLanillo= Number of Sheets Needed by ring 10

TWALL-A1 = Minimum Thickness of sheet in Ring 1, mm 6.8821TWALL-A1n = Thickness of Sheet I Ring 1 Nominal, mm 5.00

TWALL-A2 = Minimum Thickness of sheet in Ring 2, mm 5.5157TWALL-A2n = Thickness of Sheet on Ring 2 Nominal, mm 4.00



TWALL-A5 = Minimum Thickness of sheet in Ring 5, mm N/ATWALL-A5n = Thickness of Sheet on Ring 5 Nominal, mm 0.00




TWALL-A9 = Minimum Thickness of sheet in Ring 9, mm N/ATWALL-A9n = Thickness of Sheet on Ring 9 Nominal, mm 0.00TWALL-A10 = Minimum Thickness of sheet in Ring 10, mm N/A

TWALL-A10n = Thickness of Sheet on Ring 10 Nominal, mm 0.00Vct= Volume of Tanks Body , m3 2.53Pct= Weight of Tanks Body, Kg 19,965.94

ATMOSPHERICAL TANK CALCULATORACCORDING WITH API 650 - FT BY FT METHOD

INLETS

OUTPUTS


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Thicknesses: Sheets of Conical RoofNLtecho= Number of Sheets Needed for the Roof 18.00

Ttecho= minimal needed Thickness of Roof's sheet, INCHES 0.35minimal needed Thickness of Roof's sheet, mm 9.02

Ttecho n = Nominal Thickness of Roof's sheet, mm 6.35Vtt= Volume of the Roof of the Tank, m3 1.70Ptt= Weight of the Roof of the Tank, Kg 13,424.16

Thicknesses: Sheets of FloorNLpiso= Number of Sheets Needed for the Floor 18.00Tpiso= 0.31

minimal needed Thickness of Floor's sheets, INCHES 7.94Tpiso n = minimal needed Thickness of Floor's sheets, mm 10.00

Vpt= Nominal Thickness of Floor's sheets, mm 2.68Ppt= Volume of the Floor of the Tank, m3 21,140.41

Total Weight of the Floor of the Tank, Kg:Volumen= Total volume of Stored Water, m3 2,562.34

Ft3 90,476.20gallons 676,970.02

Barrels (U.S. Liquid) 21,491.11

Peso Total= Total Weight of the Empty Tank, Kilograms 54,530.51Total Weigh of the Tank Full of Water, Kilograms 2,616,869.73

Nominal Tanks Capacity (Barrels): 16,117.17Nominal Tanks Capacity (Gallons): 676,921.19

Nominal Tanks Capacity (Liters): 2,562,146.71Nominal Tanks Capacity (Mts3): 2,562.15

Percent of Volume of Air in the Tank(%): 2.50

Net Tanks Capacity (Barrels): 15,714.24Net Tanks Capacity (Gallons): 659,998.16

Net Tanks Capacity (Liters):2,498,093.04

Net Tanks Capacity (Mts3): 2,498.09


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Archivo: Mdulo 14.xls Fecha 7/30/2004

HOJA DE DATOS PARA TANQUE ATMOSFRICO - API 650 - METODO PIE POR PIE1-Fluido:

Nombre: Agua

Cp (calora/gramo C) 0.238

Presin de Vapor @ 200 F, psia 11.53

SG 1

Viscosidad @ 130 F (centistokes) 0.55

PM 18

@ 200 F (lbm/pie3) 60.13

2-Dimensiones del Tanque:Dimetro Nominal 35 pies (10,7 metros)

Altura Nominal 40 pies (12,2 metros)

Altura del Lquido 39 pies (11,9 metros)

Capacidad Nominal 1000 metros cbicos

3-Tuberias asociadas al Tanque:

Boquilla Servicio Cantidad Dimetro (pulg)N1 Entrada de Agua 1 8

N2 Salida de Agua de Agua Servicio 1 4

N3 Salida Agua Contra Incendio 1 16

N6 Entrada Recirculacin Agua Contra I 1 8

N4 Respiradero 1 12

N5 Manhole 2 24

N8 Rebose 1 10

N7 Drenaje 1 4

N9 A/B Stand Pipe 2 2

N10 Interruptor Bajo Nivel 1 2

TOTALES =

4-Datos de Operacion:Temperatura de Diseo, T1 200F (93 C)

Presin de Diseo (Pies de Columna de Agua) 492

Presin Atmosfrica (Psia) 14.7

Altitud (m.s.n.m.) 350

Presin Entrada a N1 (Psig)

Caudal de Entrada a N1 (GPM)

Velocidad de permisible de Aduccin en N1 (m/seg)

5-Boquillas y Conexiones:

Boquilla Servicio Cantidad Dimetro (pulg)N1 Entrada de Agua 1 8

N2 Salida de Agua de Agua Servicio 1 4

N3 Salida Agua Contra Incendio 1 16

N6 Entrada Recirculacin Agua Contra I 1 8

N4 Respiradero 1 12

N5 Manhole 2 24

N8 Rebose 1 10

N7 Drenaje 1 4

N9 A/B Stand Pipe 2 2

N10 Interruptor Bajo Nivel 1 2

TOTALES =


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Schedule Longitud (m) Peso (lb) Peso (kg) Material40

40

40

40

40

40

40

0.00 0.00

Peso (lb) Peso (kg) Material48.50 31.75 A-105

20.00 9.07 A-105

173.00 78.47 A-105

48.50 22.00 A-105

100.00 45.35 A-105

662.00 300.27 A-105

70.00 31.75 A-105

20.00 9.07 A-105

15.00 6.80 A-105

7.50 3.40 A-105

1164.50 537.93


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Solo ingresar datos en las celdas NO sombreadasMdulo 14CLCULO

DATOS GENERALES

Pd Presin de Diseo en pca=Altura del tanque (lleno de agua) + 12 pca 396.00Td Temperatura de Diseo, C 93.00D Dimetro del Tanque, pies 60.00

H Altura del Tanque (Lmite de Clculo = 80 ft), pies 32.00G Gravedad especfica del Fluido Almacenado (Agua=1) 1.00Sd Esfuerzo admisible para la Condicin de Diseo, Psi 23,200.00

C.A. Espesor de Corrosin, pulg 0.0625 Angulo de Inclinacin del Techo respecto a la horizontal, grados 25.00

CAPt Capacidad requerida del Tanque, metros cbicosLMINAS ESTNDAR

LARGO Largo de la lmina, pies 20.00ANCHO Ancho de la lmina, pies 8.00

AreaLE Area de Lmina Estndar, m2 14.86

DENSIDAD Densidad de la Lmina de Acero, Kg/m3 7,901.42

Espesores: Lminas de ParedAnillos= Nmero de Anillos con Lminas Estndar 4

Aa= rea de Un Anillo, m2 140.09

NLanillo= Nmero de Lminas Requeridas por anillo 10Tpared-A1= Espesor mnimo de lmina en Anillo 1, mm 6.8821

Tpared-A1n = Espesor de Lmina Anillo 1 Nominal, mm 5.00Tpared-A2= Espesor mnimo de lmina en Anillo 2, mm 5.5157

Tpared-A2n = Espesor de Lmina Anillo 2 Nominal, mm 4.00Tpared-A3= Espesor mnimo de lmina en Anillo 3, mm 4.1494

Tpared-A3n = Espesor de Lmina Anillo 3 Nominal, mm 4.00

Tpared-A4= Espesor mnimo de lmina en Anillo 4, mm 2.7831Tpared-A4n = Espesor de Lmina Anillo 4 Nominal, mm 4.00Tpared-A5= Espesor mnimo de lmina en Anillo 5, mm N/A

Tpared-A5n = Espesor de Lmina Anillo 5 Nominal, mm 0.00Tpared-A6= Espesor mnimo de lmina en Anillo 6, mm N/A





Tpared-A10n = Espesor de Lmina Anillo 10 Nominal, mm 0.00

Vct= Volumen del Cuerpo del Tanque, m3 2.53Pct= Peso del Cuerpo del Tanque, Kg 19,965.94

CLCULO DE TANQUES ATMOSFRICOSSEGN API 650 - METODO PIE POR PIE

ENTRADAS

SALIDAS


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Espesores: Lminas de Techo CnicoNLtecho= Nmero de Lminas Requeridas para el Techo 18.00

Ttecho= Espesor mnimo de lmina de Techo requerido, PULGADAS 0.35Espesor mnimo de lmina de Techo requerido, mm 9.02

Ttecho n = Espesor de Lmina Techo Nominal, mm 6.35Vtt= Volumen del Techo del Tanque, m3 1.70Ptt= Peso del Techo del Tanque, Kg 13,424.16

Espesores: Lminas de Piso

NLpiso= Nmero de Lminas Requeridas para el Piso 18.00Tpiso= Espesor mnimo de lmina de Piso requerido, PULGADAS 0.31

Espesor mnimo de lmina de Piso requerido, mm 7.94Tpiso n = Espesor de Lmina de Piso Nominal, mm 10.00

Vpt= Volumen del Piso del Tanque, m3 2.68Ppt= Peso del Piso del Tanque, Kg 21,140.41

Totales:

Volumen= Volumen Total de Agua Almacenada, m3 2,562.34

En pie3 90,476.20En galones 676,970.02

En barriles (U.S. Liquid) 21,491.11Peso Total= Peso Total del Tanque Vaco, Kilogramos 54,530.51

Peso Total del Tanque Lleno de Agua, Kilogramos 2,616,869.73

Capacidad Nominal del Tanque (Barriles): 16,117.17Capacidad Nominal del Tanque (Galones): 676,921.19

Capacidad Nominal del Tanque (Litros): 2,562,146.71

Capacidad Nominal del Tanque (Mts3): 2,562.15

Volumen de Aire en el Tanque (%): 2.50

Capacidad Neta del Tanque (Barriles): 15,714.24Capacidad Neta del Tanque (Galones): 659,998.16

Capacidad Neta del Tanque (Litros): 2,498,093.04

Capacidad Neta del Tanque (Mts3): 2,498.09

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Tanques Atmosféricos API 650