# API 620 Tank Calculations Xls

October 10, 2017 | Author: Prashant Malve | Category: Foot (Unit), Units Of Measurement, Quantity, Physics & Mathematics, Physics

API 620...

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API 620 DATA SHEET: ATMOSPHERICAL TANK API 620 - FT BY FT METH. 1-Fluid: Product: Cp (cal/gr ºC) Vapor Pressure @ 200 ºF, psia SG Viscosity @ 130 ºF (centistokes) PM

Water 0.238 11.53 1 0.55 18

r @ 200 ºF (lbm/pie3)

60.13

2-Tank Size: Nominal Diameter Nominal Heigth Líquido Heigth Nominal Capacity

35 ft (10,7 meters) 40 ft (12,2 meters) 39 ft (11,9 meters) 1000 cubic meters

3-Tuberias asociadas al Tanque: Nozzle N1 N2 N3 N6 N4 N5 N8 N7 N9 A/B N10

4-Datos de Operacion: Desgin Temperature, T1 Desging Pressure (ft Water Column) Atmospherical Pressure (Psia) Altitude (m.s.n.m.) Inlet Pressure at N1 (Psig) Inlet Flow at N1 (GPM) Maximul Allowed Velocity at N1 (m/seg)

Service Water inlet Service Water Oulet fire fighting Water Oulet Fire Fighting water recirculation inlet Venting Manhole Rebose Drenaje Stand Pipe Low Level Sw TOTALS =

Cant 1 1 1 1 1 2 1 1 2 1

200°F (93 ºC) 492 14.7 350

5-Nozzles and Conections: Nozzle N1 N2 N3 N6 N4 N5 N8 N7 N9 A/B N10

Service Water inlet Service Water Oulet fire fighting Water Oulet Fire Fighting water recirculation inlet Venting Manhole Overflow Nozzle Drainage Nozzle Stand Pipe Low Level Sw

Cant 1 1 1 1 1 2 1 1 2 1

TOTAL =

Original File: NewFile: Original Date: New Date: Original Autor: Traslation:

Diameter (inch) 8 4 16 8 12 24 10 4 2 2

Diameter (inch) 8 4 16 8 12 24 10 4 2 2

Schedule 40 40 40 40 40

Archivo: Módulo 14.xls

7/30/2004 4/7/2008 LRRJ

[email protected]

Length (m)

Weigh (lb)

Weigh (kg)

0.00

0.00

40 40

Weigh (lb) 48.50 20.00 173.00 48.50 100.00 662.00 70.00 20.00 15.00 7.50

Weigh (kg) 31.75 9.07 78.47 22.00 45.35 300.27 31.75 9.07 6.80 3.40

Material A-105 A-105 A-105 A-105 A-105 A-105 A-105 A-105 A-105 A-105

Material

1164.50

537.93

API 620 Write input Data Only on not colored cells Module 14 CALCULATIONS

Pd Td D H G Sd C.A. q CAPt LENGTH WIDTH AREA STD S: DENSITY

Rings= Aa= NLanillo= TWALL-A1 = TWALL-A1n = TWALL-A2 = TWALL-A2n = TWALL-A3 = TWALL-A3n = TWALL-A4 = TWALL-A4n = TWALL-A5 = TWALL-A5n = TWALL-A6 = TWALL-A6n = TWALL-A7 = TWALL-A7n = TWALL-A8 = TWALL-A8n = TWALL-A9 = TWALL-A9n = TWALL-A10 = TWALL-A10n = Vct= Pct=

ATMOSPHERICAL TANK CALCULATOR ACCORDING WITH API 650 - FT BY FT METHOD INLETS GENERAL DATA Design Pressure ftwc= Height of the tank (full of water) + 12 ftwc (ft of water column) Design Temperature, ºC Diameter of the Tank, feet Height of the Tank (Calculations Limits = 80 ft), feet specific Gravity of the Stored Fluid (Water=1) Allowable Working stress at Designs conditions, Psi Corrosion thickness, inch Angle of Inclination of the Roof with regard to the horizontal one, degrees Capacity needed of the Tank, cubic meters STANDARD SHEET Length of the sheet, feet Width of the sheet, feet Area of Standard Sheet, m2 Density of the Sheet of Steel, Kg/m3 OUTPUTS THICKNESS WALLS SHEET Number of Rings with Standard Sheets Area of A Ring, m2 Number of Sheets Needed by ring Minimum Thickness of sheet in Ring 1, mm Thickness of Sheet I Ring 1 Nominal, mm Minimum Thickness of sheet in Ring 2, mm Thickness of Sheet on Ring 2 Nominal, mm Minimum Thickness of sheet in Ring 3, mm Thickness of Sheet on Ring 3 Nominal, mm Minimum Thickness of sheet in Ring 4, mm Thickness of Sheet on Ring 4 Nominal, mm Minimum Thickness of sheet in Ring 5, mm Thickness of Sheet on Ring 5 Nominal, mm Minimum Thickness of sheet in Ring 6, mm Thickness of Sheet on Ring 6 Nominal, mm Minimum Thickness of sheet in Ring 7, mm Thickness of Sheet on Ring 7 Nominal, mm Minimum Thickness of sheet in Ring 8, mm Thickness of Sheet on Ring 8 Nominal, mm Minimum Thickness of sheet in Ring 9, mm Thickness of Sheet on Ring 9 Nominal, mm Minimum Thickness of sheet in Ring 10, mm Thickness of Sheet on Ring 10 Nominal, mm Volume of Tanks Body , m3 Weight of Tanks Body, Kg

396.00 93.00 60.00 32.00 1.00 23,200.00 0.0625 25.00

20.00 8.00 14.86 7,901.42

4 140.09 10 6.8821 5.00 5.5157 4.00 4.1494 4.00 2.7831 4.00 N/A 0.00 N/A 0.00 N/A 0.00 N/A 0.00 N/A 0.00 N/A 0.00 2.53 19,965.94

NLtecho= Ttecho = Ttecho n = Vtt= Ptt= NLpiso= Tpiso= Tpiso n = Vpt= Ppt= Volumen=

Peso Total=

Thicknesses: Sheets of Conical Roof Number of Sheets Needed for the Roof minimal needed Thickness of Roof's sheet, INCHES minimal needed Thickness of Roof's sheet, mm Nominal Thickness of Roof's sheet, mm Volume of the Roof of the Tank, m3 Weight of the Roof of the Tank, Kg Thicknesses: Sheets of Floor Number of Sheets Needed for the Floor minimal needed Thickness of Floor's sheets, INCHES minimal needed Thickness of Floor's sheets, mm Nominal Thickness of Floor's sheets, mm Volume of the Floor of the Tank, m3 Total Weight of the Floor of the Tank, Kg: Total volume of Stored Water, m3 Ft3 gallons Barrels (U.S. Liquid) Total Weight of the Empty Tank, Kilograms Total Weigh of the Tank Full of Water, Kilograms Nominal Tanks Capacity (Barrels): Nominal Tanks Capacity (Gallons): Nominal Tanks Capacity (Liters): Nominal Tanks Capacity (Mts3): Percent of Volume of Air in the Tank(%): Net Tanks Capacity (Barrels): Net Tanks Capacity (Gallons): Net Tanks Capacity (Liters): Net Tanks Capacity (Mts3):

18.00 0.35 9.02 6.35 1.70 13,424.16 18.00 0.31 7.94 10.00 2.68 21,140.41 2,562.34 90,476.20 676,970.02 21,491.11 54,530.51 2,616,869.73 16,117.17 676,921.19 2,562,146.71 2,562.15 2.50 15,714.24 659,998.16 2,498,093.04 2,498.09

Archivo: Módulo 14.xls

Fecha

7/30/2004

HOJA DE DATOS PARA TANQUE ATMOSFÉRICO - API 650 - METODO PIE POR PIE 1-Fluido: Nombre: Cp (caloría/gramo ºC) Presión de Vapor @ 200 ºF, psia SG Viscosidad @ 130 ºF (centistokes) PM

Agua 0.238 11.53 1 0.55 18

r @ 200 ºF (lbm/pie3)

60.13

2-Dimensiones del Tanque: Diámetro Nominal Altura Nominal Altura del Líquido Capacidad Nominal

35 pies (10,7 metros) 40 pies (12,2 metros) 39 pies (11,9 metros) 1000 metros cúbicos

3-Tuberias asociadas al Tanque: Boquilla N1 N2 N3 N6 N4 N5 N8 N7 N9 A/B N10

4-Datos de Operacion: Temperatura de Diseño, T1 Presión de Diseño (Pies de Columna de Agua) Presión Atmosférica (Psia) Altitud (m.s.n.m.) Presión Entrada a N1 (Psig) Caudal de Entrada a N1 (GPM) Velocidad de permisible de Aducción en N1 (m/seg)

Servicio Cantidad Entrada de Agua 1 Salida de Agua de Agua Servicio 1 Salida Agua Contra Incendio 1 Entrada Recirculación Agua Contra Incendio1 Respiradero 1 Manhole 2 Rebose 1 Drenaje 1 Stand Pipe 2 Interruptor Bajo Nivel 1 TOTALES =

Diámetro (pulg) 8 4 16 8 12 24 10 4 2 2

200°F (93 ºC) 492 14.7 350

5-Boquillas y Conexiones: Boquilla N1 N2 N3 N6 N4 N5 N8 N7 N9 A/B N10

Servicio Cantidad Entrada de Agua 1 Salida de Agua de Agua Servicio 1 Salida Agua Contra Incendio 1 Entrada Recirculación Agua Contra Incendio1 Respiradero 1 Manhole 2 Rebose 1 Drenaje 1 Stand Pipe 2 Interruptor Bajo Nivel 1 TOTALES =

Diámetro (pulg) 8 4 16 8 12 24 10 4 2 2

Schedule 40 40 40 40 40

Longitud (m)

Peso (lb)

Peso (kg)

0.00

0.00

40 40

Peso (lb) 48.50 20.00 173.00 48.50 100.00 662.00 70.00 20.00 15.00 7.50 1164.50

Peso (kg) 31.75 9.07 78.47 22.00 45.35 300.27 31.75 9.07 6.80 3.40 537.93

Material A-105 A-105 A-105 A-105 A-105 A-105 A-105 A-105 A-105 A-105

Material

Solo ingresar datos en las celdas NO sombreadas Módulo 14 CÁLCULO

Pd Td D H G Sd C.A. q CAPt LARGO ANCHO AreaLE DENSIDAD

Anillos= Aa= NLanillo= Tpared-A1 = Tpared-A1n = Tpared-A2 = Tpared-A2n = Tpared-A3 = Tpared-A3n = Tpared-A4 = Tpared-A4n = Tpared-A5 = Tpared-A5n = Tpared-A6 = Tpared-A6n = Tpared-A7 = Tpared-A7n = Tpared-A8 = Tpared-A8n = Tpared-A9 = Tpared-A9n = Tpared-A10 = Tpared-A10n = Vct= Pct=

CÁLCULO DE TANQUES ATMOSFÉRICOS SEGÚN API 650 - METODO PIE POR PIE ENTRADAS DATOS GENERALES Presión de Diseño en pca=Altura del tanque (lleno de agua) + 12 pca Temperatura de Diseño, ºC Diámetro del Tanque, pies Altura del Tanque (Límite de Cálculo = 80 ft), pies Gravedad específica del Fluido Almacenado (Agua=1) Esfuerzo admisible para la Condición de Diseño, Psi Espesor de Corrosión, pulg Angulo de Inclinación del Techo respecto a la horizontal, grados Capacidad requerida del Tanque, metros cúbicos LÁMINAS ESTÁNDAR Largo de la lámina, pies Ancho de la lámina, pies Area de Lámina Estándar, m2 Densidad de la Lámina de Acero, Kg/m3 SALIDAS Espesores: Láminas de Pared Número de Anillos con Láminas Estándar Área de Un Anillo, m2 Número de Láminas Requeridas por anillo Espesor mínimo de lámina en Anillo 1, mm Espesor de Lámina Anillo 1 Nominal, mm Espesor mínimo de lámina en Anillo 2, mm Espesor de Lámina Anillo 2 Nominal, mm Espesor mínimo de lámina en Anillo 3, mm Espesor de Lámina Anillo 3 Nominal, mm Espesor mínimo de lámina en Anillo 4, mm Espesor de Lámina Anillo 4 Nominal, mm Espesor mínimo de lámina en Anillo 5, mm Espesor de Lámina Anillo 5 Nominal, mm Espesor mínimo de lámina en Anillo 6, mm Espesor de Lámina Anillo 6 Nominal, mm Espesor mínimo de lámina en Anillo 7, mm Espesor de Lámina Anillo 7 Nominal, mm Espesor mínimo de lámina en Anillo 8, mm Espesor de Lámina Anillo 8 Nominal, mm Espesor mínimo de lámina en Anillo 9, mm Espesor de Lámina Anillo 9 Nominal, mm Espesor mínimo de lámina en Anillo 10, mm Espesor de Lámina Anillo 10 Nominal, mm Volumen del Cuerpo del Tanque, m3 Peso del Cuerpo del Tanque, Kg

396.00 93.00 60.00 32.00 1.00 23,200.00 0.0625 25.00

20.00 8.00 14.86 7,901.42

4 140.09 10 6.8821 5.00 5.5157 4.00 4.1494 4.00 2.7831 4.00 N/A 0.00 N/A 0.00 N/A 0.00 N/A 0.00 N/A 0.00 N/A 0.00 2.53 19,965.94

NLtecho= Ttecho = Ttecho n = Vtt= Ptt= NLpiso= Tpiso= Tpiso n = Vpt= Ppt= Volumen=

Peso Total=