e-fd-flo049-pro-450-501-ra

8/3/2019 E-FD-FLO049-PRO-450-501-RA

1/4

LAS INFORMACIONES DE ESTE DOCUMENTO SON DE PROPIEDAD DE FLOPEC, SIENDO PROHIBIDA LA UTILIZACIN 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-450-501_A.XLS

NDICE DE REVISIONES

REV. DESCRIPCIN Y/O HOJAS ALTERADAS

A EMISIN PARA REVISIN

INGENIERA TTULO: HOJA DE DATOS DE PROCESO- P-1101A/B CALENTADOR DE PROPANO

N DE CONTRATO:

RESPONSABLE TCNICO: PEDRO PINZN

NMERO INTERTECHMA: E-FD-FLO049-PRO-450-501

PROGRAMA: ESTUDIOS, INGENIERA BSICA E INGENIERA DE DETALLE

REA:TERMINAL MARTIMO Y PLANTA DE ALMACENAMIENTO DE

GLP EN MONTEVERDE

HOJA DE DATOS DE PROCESO No. E-FD-FLO049-PRO-450-501

CLIENTE: FLOTA PETROLERA ECUATORIANA HOJA: 1 de 4

8/3/2019 E-FD-FLO049-PRO-450-501-RA

2/4

Revised: Date: Approved: Date:

Client: FLOPEC

Project:

Location: MONTEVERDE

Tag: P-1101A/B

Service of Unit Item No.

Size 26,0000 x 240,000 inch Type AES Horz. Connected In 1 Parallel 1 Series

Surf/Unit (Gross/Eff) 1720,02 / 1691,35 ft2 Shell/Unit 1 Surf/Shell (Gross/Eff) 1720,02 / 1691,35 ft2

PERFORMANCE OF ONE UNIT

Fluid Allocation

Fluid Name

Fluid Quantity, Total lb/hr

Vapor (In/Out)

Liquid

Steam

Water

Noncondensables

Temperature (In/Out F

Specific Gravity

Viscosity cP

Molecular Weight, Vapor

Molecular Weight, Noncondensables

Specific Heat Btu/lb-F

Thermal Conductivit Btu/hr-ft-F

Latent Heat Btu/lb

Inlet Pressure psia

Velocity ft/sec

Pressure Drop, Allo psi

Fouling Resistance ( ft2-hr-F/BtuHeat Exchanged Btu/hr 25889261 MTD (Corrected) 48,3 F

Transfer Rate, Service 316,81 Btu/ft2-hr-F Clean 427,01 Btu/ft2-hr-F Actual 427,01 Btu/ft2-hr-F

Sketch (Bundle/Nozzle Orientation)

Tube Side

Design/Test Pressur psig

Design TemperatureF

No Passes per Shell

Corrosion Allowanceinch

Connections In inch

Size & Out inch

Rating Intermediate

Tube 438 OD 0,7500 inch Thk(Avg) 0,0650 inch Length 20,000 ft Pitch 0,9843 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) 20,0000 Inlet 30,8061 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 845,52 lb/ft-sec2 Bundle Entrance 599,24 Bundle Exit 1003,19 lb/ft-sec2

Gaskets-Shell Side Reinforced Graphite Tube Side

-Floating Head

Code Requirements TEMA Class RWeight/Shell 12034,7 Filled with Water 17204,7 Bundle 4932,28 lb

Remarks:

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

Reprinted with Permission (v5 )

Reinforced Graphite

1 @ 12,0900

1 @ 12,0900

@

1 @ 12,0900

1 @ 12,0900

@

CONSTRUCTION OF ONE SHELL

270,000 / Per Code

100,00

1

Shell Side

270,000 / Per Code

120.00

2

4,05

5,360

169,000

13,30

28,970

1,0318

0,3392

243,000

0,0601

49,98

1,0193

1,2995

13934001393400

67,98

1,0119

1,0017

0,5087

0,0767

1,0309

0,3488

507383

0,6063

0,1257

40,98

0,5290

-51,26

0,5924

0,2150

507383

507383

Tube Side

1393400

8/3/2010 M.R. 8/3/2010

Shell Side

P.P.

PROPANO AGUA DE MAR

HOJA DE DATOS DE PROCESOCALENTADOR DE PROPANO

Rev. No. Prepared:

SISTEMA IMPERIAL

A N.P. 8/3/2010

TERMINAL MARTIMO Y PLANTA DE ALMACENAMIENTO DE GLP EN MONTEVERDE

E-FD-FLO049-PRO-450-501

Date:

20,000 ft

26,0000 inch

8/3/2019 E-FD-FLO049-PRO-450-501-RA

3/4


Client: FLOPEC

Project:


Tag P-1101A/B

Service of Unit Item No.

Size 660,401 x 6096,00 mm Type AES Horz. Connected In 1 Parallel 1 Series

Surf/Unit (Gross/Eff) 159,79 / 157,13 m2 Shell/Unit 1 Surf/Shell (Gross/Eff) 159,79 / 157,13 m2

PERFORMANCE OF ONE UNIT

Fluid Allocation Shell Side Tube Side

Fluid Name

Fluid Quantity, Total 1000-kg/hr 230,147 632,042

Vapor (In/Out)

Liquid 230,147 230,147 632,042 632,042

Steam

Water

Noncondensables

Temperature (In/Out C -46,25 4,99 19,99 9,99

Specific Gravity 0,5924 0,5290 1,0119 1,0193

Viscosity cP 0,2150 0,1257 1,0017 1,2995

Molecular Weight, Vapor

Molecular Weight, Noncondensables

Specific Heat kcal/kg-C 0,5087 0,6063 1,0309 1,0318

Thermal Conductivit kcal/hr-m-C 0,1141 0,0894 0,5188 0,5046

Latent Heat kcal/kg

Inlet Pressure bar-G 15,741 10,639

Velocity m/s 1,24 4,05

Pressure Drop, Allo bar 0,370 1,997

Fouling Resistance ( m2-hr-C/kcalHeat Exchanged MM kcal 6,5197 MTD (Corrected) 26,8 C

Transfer Rate, Service 1545,74 kcal/m2-hr-CClean 2083,42 kcal/m2-hr-C Actual 2083,42 kcal/m2-hr-C

Sketch (Bundle/Nozzle Orientation)

Shell Side Tube Side

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 6096, mm Pitch 25,000 mm Layout 90

Tube Type Plain Material : SA-213 UNS S31254 (20 Cr, 18 Ni) or similarShell 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) 508,001 Inlet 782,476 mm

Baffles-Long Seal Type

Supports-Tub U-Bend Type

Bypass Seal Arrangement Tube-Tubesheet Joint

Expansion Joint Defined by supplier Type

Rho-V2-Inlet Nozzle 845,52 lb/ft-sec2 Bundle Entrance 599,24 Bundle Exit 1003,19 lb/ft-sec2

Gaskets-Shell Side Reinforced Graphite Tube Side

-Floating Head

Code Requirements TEMA Class RWeight/Shell 5,459 Filled with Water 7,804 Bundle 2,237 Kg

Remarks:

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

Reprinted with Permission (v5 )

@

CONSTRUCTION OF ONE SHELL

2

1 @ 307,087

1 @ 307,087

Reinforced Graphite

18,616 /Per Code

37,78

1

1 @ 307,087

1 @ 307,087

@

18,616 /Per Code

54.44

03-08-10

PROPANO AGUA DE MAR

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


SISTEMA INTERNACIONAL


E-FD-FLO049-PRO-450-501

Rev. N Prepared: Date:

A N.P. 03-08-10

6096, mm

660,401 mm

8/3/2019 E-FD-FLO049-PRO-450-501-RA

4/4


Client: FLOPECProject:


Tag: P-1101A/B

NOTAS:

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

2- El diseo hidrulico y termodinmico del equipo debe ser confirmado por el proveedor.

3- El anlisis de vibracin y el rendimiento acstico del equipo debe ser diseado por el proveedor.

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

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

6- ESTAMPE ASME U : SI

7- Nivel radiogrfico : RT18- Aislamiento Trmico / Proteccin Personal : Ver spec E-ET-FLO049-TUB-200-0039- Corrosin 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 Inorgnico + 5 MILS Epoxico + 2 MILS Poliuretano (Partes no aisladas)

12- Composicin del Propano Comercial.

Ethane

Propane

n-Butane

i-Butane

n-Pentane

H2O

Total

PROPANO COMERCIAL

Mass Fractions

4,60 %

81,40 %

Mole Fractions

6,8 %

82,4 %

100 %

6,1 %

4,5 %

0,1 %

0,0 %

8,00 %

5,90 %

0,10 %

0,00 %

8/3/2010 M.R. 8/3/2010



NOTAS

E-FD-FLO049-PRO-450-5018/3/2010 P.P.

Rev. No. Prepared: Date:

A N.P.

e-fd-flo049-pro-450-501-ra

Documents