e-fd-flo049-pro-450-501-ra
TRANSCRIPT
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8/3/2019 E-FD-FLO049-PRO-450-501-RA
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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
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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
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8/3/2019 E-FD-FLO049-PRO-450-501-RA
3/4
Revised: Date: Approved: Date:
Client: FLOPEC
Project:
Location: MONTEVERDE
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.
HOJA DE DATOS DE PROCESOCALENTADOR DE PROPANO
SISTEMA INTERNACIONAL
TERMINAL MARTIMO Y PLANTA DE ALMACENAMIENTO DE GLP EN MONTEVERDE
E-FD-FLO049-PRO-450-501
Rev. N Prepared: Date:
A N.P. 03-08-10
6096, mm
660,401 mm
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8/3/2019 E-FD-FLO049-PRO-450-501-RA
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Revised: Date: Approved: Date:
Client: FLOPECProject:
Location: MONTEVERDE
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
TERMINAL MARTIMO Y PLANTA DE ALMACENAMIENTO DE GLP EN MONTEVERDE
HOJA DE DATOS DE PROCESOCALENTADOR DE PROPANO
NOTAS
E-FD-FLO049-PRO-450-5018/3/2010 P.P.
Rev. No. Prepared: Date:
A N.P.