e-fd-flo049-pro-450-502-ra

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LAS INFORMACIONES DE ESTE DOCUMENTO SON DE PROPIEDAD DE FLOPEC, SIENDO PROHIBIDA LA UTILIZACIÓN FUERA DE SU FINALIDAD.

APROBADO M.R.

ELABORADO N.P.

VERIFICADO P.P.

PROYECTO INTER+TEC

FECHA 03/08/10

REV. B REV. 0REV. A

NOMBRE DEL ARCHIVO: EXCEL / E-FD-FLO049-PRO-450-502_A.XLS

ÍNDICE DE REVISIONES

REV. DESCRIPCIÓN Y/O HOJAS ALTERADAS

A EMISIÓN PARA REVISIÓN

INGENIERÍATÍTULO:

HOJA DE DATOS DE PROCESO- P-1102 CALENTADOR DE BUTANONº DE CONTRATO:

RESPONSABLE TÉCNICO: PEDRO PINZÓN

NÚMERO INTERTECHMA: E-FD-FLO049-PRO-450-502

PROGRAMA:INGENIERÍA BÁSICA

ÁREA: TERMINAL MARÍTIMO Y PLANTA DE ALMACENAMIENTO DEGLP EN MONTEVERDE

HOJA DE DATOS DE PROCESONo.

E-FD-FLO049-PRO-450-502

CLIENTE: FLOTA PETROLERA ECUATORIANA HOJA: 1 de 4



Revised: Date: Approved: Date:

Client: FLOPEC

Project:

Location: MONTEVERDE

Tag P-1102

Service of Unit PROPANE HEATER Item No.

Size 26,0000 x 192,000 inch Type AES Horz. Connected In 1 Parallel 1 Series

Surf/Unit (Gross/Eff) 1376,01 / 1347,35 ft^2 Shell/Unit 1 Surf/Shell (Gross/Eff) 1376,01 / 1347,35 ft^2

PERFORMANCE OF ONE UNIT

Fluid Allocation

Fluid Name

Fluid Quantity, Total lb/hr

Vapor (In/Out)

Liquid

Steam

Water

Noncondensables

Temperature (In/Out) °F 40,98 67,98

Specific Gravity

Viscosity cP

Molecular Weight, Vapor

Molecular Weight, Noncondensables

Specific Heat Btu/lb-°F

Thermal Conductivity Btu/hr-ft-°F

Latent Heat Btu/lb

Inlet Pressure psia

Velocity ft/sec

Pressure Drop, Allow/Calc psi

Fouling Resistance (min) f t2-hr-°F/BtuHeat Exchanged Btu/hr 7794367 MTD (Corrected) 27,8 F

Transfer Rate, Service 208,03 Btu/ft2-hr-°F Clean 236,32 Btu/ft2-hr-°F Actual 236,32 Btu/ft2-hr-°F

Shell Side Tube Side

Design/Test Pressure psig

Design Temperature °F

No Passes per Shell

Corrosion Allowance inch

Connections In inch

Size & Out inch

Rating Intermediate

Tube No 438 OD 0,7500 inch Thk(Avg) 0,0650 inch Length 16,000 ft Pitch 1,0000 inch Layout 90

Tube Type Plain Material : SA-213 UNS S31254 (20 Cr, 18 Ni) or similarShell ID 26,0000 inch OD inch Shell Cover A-203 Gr.D or similar

Channel or Bonnet By supplier Channel Cover By supplier

Tubesheet-Stationary By supplier Tubesheet-Floating By supplier

Floating Head Cover By supplier Impingement Plate None

Baffles-Cross Type SINGLE-SEG. %Cut (Diam) 30,0 Spacing(c/c) 23,6220 Inlet 34,9450 inch

Baffles-Long Seal Type

Supports-Tube U-Bend Type

Bypass Seal Arrangement Tube-Tubesheet Joint

Expansion Joint Defined by supplier Type

Rho-V2-Inlet Nozzle 1039,86 lb/ft-sec2 Bundle Entrance 531,70 Bundle Exit 546,19 lb/ft-sec2

Gaskets-Shell Side Tube Side Reinforced Graphite

-Floating Head

Code Requirements TEMA Class RWeight/Shell 10222,8 Filled with Water 14387,2 Bundle 4042,66 lb

Remarks:

- Design by ASME VIII-Div-1 2007 ADD 2009 & TEMA 8th Ed.

Reprinted with Permission (v5 )

Shell Side

567359

Tube Side

419520

AGUA DE MARBUTANO

1

3,436

169,000

4,00

243,000

3,44

265,000 / Per Code

70,00

2

A N.P. 8/3/2010 8/3/2010 M.R. 8/3/2010P.P.

HOJA DE DATOS DE PROCESOCALENTADOR DE BUTANO

Rev. No. Prepared: Date:

SISTEMA IMPERIAL

E-FD-FLO049-PRO-450-502

TERMINAL MARÍTIMO Y PLANTA DE ALMACENAMIENTO DE GLP EN MONTEVERDE

0,6023 1,0119

567359

0,0591

0,5863

0,1956

0,5408

0,0563

0,2263

1,03090,5174

0,3488

49,98

1,0193

1,2995

1,0318

0,3392

1,0017

14,95

567359 419520419520

1 @ 8,0710

1 @ 8,0710

@

Reinforced Graphite

2,940

Sketch (Bundle/Nozzle Orientation)CONSTRUCTION OF ONE SHELL

1 @ 12,0900

1 @ 12,0900

@

265,000 / Per Code

110,00

16,000 ft

26,0000 inch




Client: FLOPEC

Project:

Location: MONTEVERDETag P-1102

Service of Unit Item No.

Size 660,401 x 4876,80 mm Type AES Horz. Connected In 1 Parallel 1 Series

Surf/Unit (Gross/Eff) 127,84 / 125,17 m2 Shell/Unit 1 Surf/She ll (Gross/Eff) 127,84 / 125,17 m2

PERFORMANCE OF ONE UNIT

Fluid Allocation

Fluid Name

Fluid Quantity, Total 1000-kg/hr

Vapor (In/Out)

Liquid

Steam

Water

NoncondensablesTemperature (In/Out C

Specific Gravity

Viscosity cP

Molecular Weight, Vapor

Molecular Weight, Noncondensables

Specific Heat kcal/kg-C

Thermal Conductivit kcal/hr-m-C

Latent Heat kcal/kg

Inlet Pressure bar-G

Velocity m/s

Pressure Drop, Allo bar

Fouling Resistance ( m2-hr-C/kcal

Heat Exchanged MM kcal 1,9628 MTD (Corrected) 15,4 C

Transfer Rate, Service 1014,99 kcal/m2-hr-C Clean 1153,02 kcal/m2-hr-C Actual 1153,02 kcal/m2-hr-C

CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)


Design/Test Pressur barG

Design TemperatureC

No Passes per Shell

Corrosion Allowancemm

Connections In mm

Size & Out mm

Rating Intermediate

Tube 438 OD 19,050 mm Thk(Avg) 1,650 mm Length 4877, mm Pitch 25,400 mm Layout 90

Tube Type Plain Material : SA-213 UNS S31254 (20 Cr, 18 Ni) or similar

Shell ID 660,401 mm OD mm Shell Cover A-203 Gr.D or similar

Channel or Bonnet By supplier Channel Cover By supplier

Tubesheet-Stationary By supplier Tubesheet-Floating By supplier

Floating Head Cover By supplier Impingement Plate None

Baffles-Cross Type SINGLE-SEG. %Cut (Diam) 30,0 Spacing(c/c) 600,000 Inlet 887,605 mm

Baffles-Long Seal Type

Supports-Tube U-Bend Type

Bypass Seal Arrangement Tube-Tubesheet Joint

Expansion Joint Defined by supplier Type

Rho-V2-Inlet Nozzle 1039,86 lb/ft-sec2 Bundle Entrance 531,70 Bundle Exit 546,19 lb/ft-sec2

Gaskets-Shell Side Tube Side Reinforced Graphite

-Floating Head

Code Requirements TEMA Class R

Weight/Shell 4,637 Filled with Water 6,526 Bundle 1,834 Kg

Remarks:

- Design by ASME VIII-Div-1 2007 ADD 2009 & TEMA 8th Ed.

Reprinted with Permission (v5 )

03-08-10

SISTEMA INTERNACIONAL

N.P. 03-08-10 P.P. 03-08-10 M.R.



E-FD-FLO049-PRO-450-502

Rev. N° Prepared: Date:

A

BUTANO AGUA DE MAR


190,293257,352

257,352 190,293

-9,47

0,6023

0,2263

0,5174

0,0879

257,352

4,99

0,5863

0,1956

0,5408

0,0837

19,99

1,0119

1,0017

1,0309

0,5188

190,293

9,99

1,0193

1,2995

1,0318

0,5046

15,741

1,05

10,639

1,22

18,271 / Per Code

21,11

0,237 0,203

1 @ 307,087

1 @ 307,087

Reinforced Graphite

@

18,271 / Per Code

43,33

2

1 @ 205,004

1 @ 205,004

@

1

4877, mm

660,401 mm




Client: FLOPEC

Project:

Location: MONTEVERDE

Tag P-1102

NOTAS:

1- El proveedor debe garantizar el rendimiento hidráulico y termodinamico del equipo para las condiciones operativas.

2- El diseño hidráulico y termodinámico del equipo debe ser confirmado por el proveedor.

3- El análisis de vibración y el rendimiento acústico del equipo debe ser diseñado por el proveedor.

4- Toda la información en esta hoja de datos se refiere a cada equipo.

5- El proveedor de los calentadores debe proveer los CLIPS para el aislamiento térmico.

6- ESTAMPE ASME U : SI

7- Nivel radiográfico : RT1

8- Aislamiento Térmico / Protección Personal :Ver spec E-ET-FLO049-TUB-200-003

9- Corrosión admisible : 1/8"

10- Material sugerido esparragos/tuercas: A-320 Gr. L7 / A-194 Gr.4

11- Recubrimiento (Si se usa CS ) : 3-MILS Zinc Inorgánico + 5 MILS Epoxico + 2 MILS Poliuretano (Partes no aisladas)

12- Composición del Butano Comercial.

47,0 %

100 %Total

45,0 %

2,0 %

0,00 %

n-Butane

i-Butane

46,3 %

n-Pentane

H2O

1,6 %

0,0 %

44,3 %

SISTEMA IMPERIAL

M.R.A N.P. 8/3/2010


8/3/2010 P.P.

Rev. No. Prepared:

8/3/2010

Date:


E-FD-FLO049-PRO-450-502

Ethane

Propane

BUTANO COMERCIAL

Mass Fractions

0,0 %

7,8 % 6,0 %

Mole Fractions

0,0 %

e-fd-flo049-pro-450-502-ra

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