e-fd-flo049-pro-450-502-ra
TRANSCRIPT
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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
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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
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Revised: Date: Approved: Date:
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)
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 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.
HOJA DE DATOS DE PROCESOCALENTADOR DE BUTANO
TERMINAL MARÍTIMO Y PLANTA DE ALMACENAMIENTO DE GLP EN MONTEVERDE
E-FD-FLO049-PRO-450-502
Rev. N° Prepared: Date:
A
BUTANO AGUA DE MAR
Shell Side Tube Side
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
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Revised: Date: Approved: Date:
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
HOJA DE DATOS DE PROCESOCALENTADOR DE BUTANO
8/3/2010 P.P.
Rev. No. Prepared:
8/3/2010
Date:
TERMINAL MARÍTIMO Y PLANTA DE ALMACENAMIENTO DE GLP EN MONTEVERDE
E-FD-FLO049-PRO-450-502
Ethane
Propane
BUTANO COMERCIAL
Mass Fractions
0,0 %
7,8 % 6,0 %
Mole Fractions
0,0 %