LINE SIZE

OTEPI

CLIENT: PROJECT: LOCATION: PROJECT No: CASE:

PDVSA PRODUCCION USO DE AIRE SECO PARA CONTROL DE INSTRUMENTOS Estacion Orocual EF-ORC-4 D01K1-28000 Clase de Tuberia: HX2

DATE: 2/28/2014 BY: F. J. Arias REV.: H. Bermudez

INPUT  

Line Num be ber Drawing Ref. from to

2 ""-IA -0 -001 1 1/2"-IA -0 -001 1 1/2" -I -IA -0 -0 02 02 1"-IA -0 -003 1/2""-IA -0 -0 04 04 1/2""-IA -0 -005 1/2 "" ""-IA -0 -006 BM20900 BM20900 BM20900 BM20900 BM20900 BM20900 BM20900 V-001 2"-IA-001 2"-IA-001 1 1/2"-IA-001 2"-IA-001 2"-IA-001 1"-IA-003 1 1/2"-IA-002 1/2"-IA-008 1/2"-IA-014 Conex. Futura LCV-260110 PCV-110220 LCV-110110

Nominal or Internal diameter Diameter

[in]

Schedule (only for Nominal diameter) Pipe material Pipe roughness Phase (L, G, or M) Liquid Flowrate Gas Flowrate Temperature Pressure Molecular Weight Liquid Density Gas Density Cp/Cv Gas Compressibility Factor Z Gas Viscosity Liquid / Mixed Phase Viscosity Liquid Surface Tension

[in] [kg/h] [kg/h] [°C] [barg] [kg/m3] [kg/m3]

[cP] [cP] [dynes/cm]

FORMAL PROCESS DATA ANALYSIS FORMAL PIPE DATA ANALYSIS Physical Length Delta Elev ation (Note 1) # of 45° Standard Elbows # of 90° Standard Elbows # of 90° Long Radius Elbows # of Tees: thru flow # of Tees: branch flow # of Valv es - Check # of Valv es - Gate Sudden Enlarg. Nom. Diam. Sudden Contr. Nom. Diam. Pipe Sharp Edged Entrance (K=0.5) Pipe Exit (K=1) Sum of other Equiv. Lengths (L/D) (Note 2) Sum of other K's Sum of other Pressure Drops

[m] [m] (L/D=16) (L/D=30) (L/D=16) (L/D=20) (L/D=60) (L/D=100) (L/D=8) [in] [in]

[bar]

Nominal 2

Nominal 1.5

Nominal 1.5

Nominal 1

Nominal 0.5

Nominal 0.5

Nominal 0.5

STD

S TD

STD

STD

STD

ST D

S TD

Galv a Iron 0.006

Galva Iron 0.006

Galv a Iron 0.006

Galv a Iron 0.006

Galv a Iron 0.006

Galv a Iron 0.006

Galva Iron 0.006

G

G

G

G

G

G

G

90.4 37.7 6.9 28.97

23 37.7 6.9 28.97

27.6 37.7 6.9 28.97

9.2 37.7 6.9 28.97

4.6 37.7 6.9 28.97

4.6 37.7 6.9 28.97

4.6 37.7 6.9 28.97

8.82 1.39 1 0.019

8.82 1.4 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

GAS OK

GAS OK

GAS OK

GAS OK

GAS OK

GAS OK

GAS OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

37 3.7 0 4 0 1 3 0 2 0 1 1 0 0 0 0

25.5 -1 0 3 0 0 3 0 0 0 1 0 0 0 0 0

29.5 -1 0 1 0 0 6 0 0 0 1 0 0 0 0 0

9.5 -1 0 1 0 0 2 0 0 0 1 0 0 0 0 0

4.5 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

4 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

2 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

Turbulent 39 127 1.41 -

Turbulent 12 38 0.00 -

Turbulent 5 16 0.00 -

Turbulent 4 14 0.00 -

Turbulent 2 8 0.00 -

OUTPUT  

Flow Characteristic Equiv alent Length Equiv alent Length Total K Mixed Phase Density Mixed Phase Flow Pattern Gas Density Gas Viscosity k (=Cp/Cv ) Z Sonic Velocity Mach number Maximum Allowable Velocity Minimum Velocity (two phase) Velocity Frictional Pressure Drop per length Frictional Pressure Drop per length Total Frictional Pressure Drop Total Pressure Drop (including Static Head)

[m] [ft] [kg/m3] [kg/m3] [cP]

[m/s] [m/s] [m/s] [m/s] [psi/100ft] [bar/100m] [bar] [bar]

Turbulent 48 159 6.50 -

Turbulent 32 104 1.41 -

-

-

-

-

-

-

-

8.820 0.019 1.390 1.000 352.2 0.004 41.1 1.32 0.02 0.00 0.00 0.01

8.820 0.019 1.400 1.000 353.4 0.002 41.1 0.55 0.01 0.00 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.66 0.01 0.00 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.001 41.1 0.52 0.01 0.00 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

Note 1: Only positive Delta Elevation (end point higher than start point) Note 2: For a collection of L/D values see Table: EQUIVALENT LENGTH OF VARIOUS VALVES VALVES AND FITTINGS (F5 + LENGTHS).

214181139.xls.ms_office anexo

1 DE 3

OTEPI

CLIENT: PROJECT: LOCATION: PROJECT No: CASE:

PDVSA PRODUCCION USO DE AIRE SECO PARA CONTROL DE INSTRUMENTOS Estacion Orocual EF-ORC-4 D01K1-28000 Clase de Tuberia: HX2

DATE: 2/28/2014 BY: F. J. Arias REV.: H. Bermudez

INPUT  

Line Number Drawing Ref. from to

1/2""-IA-007 1/2""-IA-008 1/2""-IA-009 1/2""-IA-010 1/2""-IA-011 1/2""-IA-012 1/2""-IA-013 BM20900 BM20900 BM20900 BM20900 BM20900 BM20900 BM20900 1 1/2"-IA-001 1 1/2"-IA-001 1 1/2"-IA-002 1 1/2"-IA-002 1 1/2"-IA-002 1 1/2"-IA-002 1 1/2"-IA-002 PCV-110110 PCV-110410 LCV-110210 LCV-110610 LCV-110410 LCV-250310 LCV-260210

Nominal or Internal diameter Diameter

[in]

Schedule (only for Nominal diameter) Pipe material Pipe roughness

[in]

Phase (L, G, or M) Liquid Flowrate Gas Flowrate Temperature Pressure Molecular Weight Liquid Density Gas Density Cp/Cv Gas Compressibility Factor Z Gas Viscosity Liquid / Mixed Phase Viscosity Liquid Surface Tension

[kg/h] [kg/h] [°C] [barg] [kg/m3] [kg/m3]

[cP] [cP] [dynes/cm]

FORMAL PROCESS DATA ANALYSIS FORMAL PIPE DATA ANALYSIS Physical Length Delta Elevation (Note 1) # of 45° Standard Elbows # of 90° Standard Elbows # of 90° Long Radius Elbows # of Tees: thru flow # of Tees: branch flow # of Valves - Check # of Valves - Gate Sudden Enlarg. Nom. Diam. Sudden Contr. Nom. Diam. Pipe Sharp Edged Entrance (K=0.5) Pipe Exit (K=1) Sum of other Equiv. Lengths (L/D) (Note 2) Sum of other K's Sum of other Pressure Drops

[m] [m] (L/D=16) (L/D=30) (L/D=16) (L/D=20) (L/D=60) (L/D=100) (L/D=8) [in] [in]

[bar]

Nominal 0.5

Nominal 0.5

Nominal 0.5

Nominal 0.5

Nominal 0.5

Nominal 0.5

Nominal 0.5

STD

STD

STD

STD

STD

STD

STD

Galva Iron 0.006

Galva Iron 0.006

Galva Iron 0.006

Galva Iron 0.006

Galva Iron 0.006

Galva Iron 0.006

Galva Iron 0.006

G

G

G

G

G

G

G

4.6 37.7 6.9 28.97

4.6 37.7 6.9 28.97

4.6 37.7 6.9 28.97

4.6 37.7 6.9 28.97

4.6 37.7 6.9 28.97

4.6 37.7 6.9 28.97

4.6 37.7 6.9 28.97

8.82 1.39 1 0.019

8.82 1.4 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

GAS OK

GAS OK

GAS OK

GAS OK

GAS OK

GAS OK

GAS OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

2.5 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

2 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

5 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

2.5 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

5 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

3 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

7 -1 0 0 0 0 0 0 0 0 0 0 0 0 0 0

Turbulent 5 18 0.00 -

Turbulent 3 9 0.00 -

Turbulent 5 18 0.00 -

Turbulent 3 11 0.00 -

Turbulent 7 23 0.00 -

OUTPUT  

Flow Characteristic Equivalent Length Equivalent Length Total K Mixed Phase Density Mixed Phase Flow Pattern Gas Density Gas Viscosity k (=Cp/Cv) Z Sonic Velocity Mach number Maximum Allowable Velocity Minimum Velocity (two phase) Velocity Frictional Pressure Drop per length Frictional Pressure Drop per length Total Frictional Pressure Drop Total Pressure Drop (including Static Head)

[m] [ft] [kg/m3] [kg/m3] [cP]

[m/s] [m/s] [m/s] [m/s] [psi/100ft] [bar/100m] [bar] [bar]

Turbulent 3 9 0.00 -

Turbulent 2 8 0.00 -

-

-

-

-

-

-

-

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.400 1.000 353.4 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

Note 1: Only positive Delta Elevation (end point higher than start point) Note 2: For a collection of L/D values see Table: EQUIVALENT LENGTH OF VARIOUS VALVES AND FITTINGS (F5 + LENGTHS).

214181139.xls.ms_office

anexo (1)

2 DE 3

OTEPI

LINE SIZE & PRESSURE DROP CALCULATION CLIENT: PROJECT: LOCATION: PROJECT No: CASE:

PDVSA PRODUCCION DATE: 2/28/2014 USO DE AIRE SECO PARA CONTROL DE INSTRUMENTOS BY: F. J. Arias Estacion Orocual EF-ORC-4 REV.: H. Bermudez D01K1-28000 Clase de Tuberia: HX2 hasta la linea 1/2"-IA-014 y HA2 desde la linea 1 1/2"-PA-001 hasta 1"-PA-004 INPUT  

Line Num ber Drawing Ref. from to

1/2""-IA-014 1 1 /2"-PA-001 1"-PA-002 1"-PA-00 3 1"-PA-004 BM20900 BM20900 BM20900 BM20900 BM20900 1 1/2"-IA-002 2"-IA-001 1 1/2"-PA-001 1 1/2"-PA-001 1 1/2"-PA-001 LCV-260210 1"-PA-003 EST. 1 EST. 2 EST. 3

Nominal or Internal diameter Diameter

[in]

Schedule (only for Nominal diameter) Pipe material Pipe roughness

[in]

Phase (L, G, or M) Liquid Flowrate Gas Flowrate Temperature Pressure Molecular Weight Liquid Density Gas Density Cp/Cv Gas Compressibility Factor Z Gas Viscosity Liquid / Mixed Phase Viscosity Liquid Surface Tension

[kg/h] [kg/h] [°C] [barg] [kg/m3] [kg/m3]

[cP] [cP] [dynes/cm]

FORMAL PROCESS DATA ANALYSIS FORMAL PIPE DATA ANALYSIS Physical Length Delta Elevation (Note 1) # of 45° Standard Elbows # of 90° Standard Elbows # of 90° Long Radius Elbows # of Tees: thru flow # of Tees: branch flow # of Valves - Check # of Valves - Gate Sudden Enlarg. Nom. Diam. Sudden Contr. Nom. Diam. Pipe Sharp Edged Entrance (K=0.5) Pipe Exit (K=1) Sum of other Equiv. Lengths (L/D) (Note 2) Sum of other K's Sum of other Pressure Drops

[m] [m] (L/D=16) (L/D=30) (L/D=16) (L/D=20) (L/D=60) (L/D=100) (L/D=8) [in] [in]

[bar]

Nominal 0.5

Nominal 1.5

Nominal 1

Nominal 1

Nominal 1

Internal

Nominal

STD

STD

STD

STD

STD

##########

STD

Galva Iron 0.006

Default 0.0018

Default 0.0018

Default 0.0018

Default 0.0018

Galva Iron

Galva Iron

G

G

G

G

G

G

G

4.6 37.7 6.9 28.97

60 37.7 6.9 28.97

27 37.7 6.9 28.97

27 37.7 6.9 28.97

27 37.7 6.9 28.97

8.82 1.39 1 0.019

8.82 1.4 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

8.82 1.39 1 0.019

GAS OK

GAS OK

GAS OK

GAS OK

GAS OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

DIAM. OK SCHED. OK

Missing Gas Flow Missing Pipe Dia.

Missing Gas Flow Missing Pipe Dia.

6.5 -1 0 1 0 0 0 0 1 0 1 0 0 0 0 0

60 -1.5 0 2 0 0 3 0 2 0 1 0 0 0 0 0

5 -1.5 0 1 0 0 0 0 1 0 1 0 0 0 0 0

5 -1.5 0 1 0 0 0 0 1 0 1 0 0 0 0 0

47 -1.5 0 1 0 0 0 0 1 0 1 0 0 0 0 0

Turbulent 6 19 0.00 -

Turbulent 6 19 0.00 -

Turbulent 48 157 0.00 -

#DIV/0! #NUM! #NUM! 0.00 -

#N/A #N/A #N/A 0.00 -

OUTPUT  

Flow Characteristic Equivalent Length Equivalent Length Total K Mixed Phase Density Mixed Phase Flow Pattern Gas Density Gas Viscosity k (=Cp/Cv) Z Sonic Velocity Mach number Maximum Allowable Velocity Minimum Velocity (two phase) Velocity Frictional Pressure Drop per length Frictional Pressure Drop per length Total Frictional Pressure Drop Total Pressure Drop (including Static Head)

[m] [ft] [kg/m3] [kg/m3] [cP]

[m/s] [m/s] [m/s] [m/s] [psi/100ft] [bar/100m] [bar] [bar]

Turbulent 7 22 0.00 -

Turbulent 68 223 1.41 -

-

-

-

-

-

-

-

8.820 0.019 1.390 1.000 352.2 0.002 41.1 0.74 0.03 0.01 0.00 0.00

8.820 0.019 1.400 1.000 353.4 0.004 41.1 1.44 0.03 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.004 41.1 1.53 0.05 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.004 41.1 1.53 0.05 0.01 0.00 0.00

8.820 0.019 1.390 1.000 352.2 0.004 41.1 1.53 0.05 0.01 0.01 0.00

0.000 #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0!

0.000 #DIV/0! #DIV/0! #DIV/0! #DIV/0! #N/A #N/A #N/A #N/A

Note 1: Only positive Delta Elevation (end point higher than start point) Note 2: For a collection of L/D values see Table: EQUIVALENT LENGTH OF VARIOUS VALVES AND FITTINGS (F5 + LENGTHS).

214181139.xls.ms_office

anexo (2)

3 DE 3