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TRANSCRIPT
CH2M HILL INC
Burlington, MA
USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103
CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION
4 PIPE-102Pipe Segment
Outlet Stream
STREAM NAME TO UNIT OPERATION
5 TEE-100Tee
Energy Stream
STREAM NAME TO UNIT OPERATION
Q03
PARAMETERS
Pressure Gradient/Pipe Parameters
Pipe Flow Correlation Beggs and Brill Pressure Drop: 138.8 kPa
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PARAMETERS
Fittings Parameters
Segment Number
Fitting Name
VH Factor
FT Factor
Data Source
2
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
4
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
6
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
8
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
Segment Number
Fitting Name
VH Factor
FT Factor
Data Source
10
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
12
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
14
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
16
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
Segment Number
Fitting Name
VH Factor
FT Factor
Data Source
18
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
20
Elbow: 90 Std
0.0000 *
30.00 *
Crane 410M, A-29
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PARAMETERS
Swage Parameters
Segment Number
Swage Name
Swage Angle (deg)
Inlet Diameter
Outlet Diameter
Swage Type
CALCULATION
Pressure Tolerance (kPa)
Temperature Tolerance (C)
Heat Flow Tolerance (kJ/h)
Length Initial Guess (m)
Always Use PH Flash
Do Deposition Calcs
Is Pipe Choked
0.1000
1.000e-002
0.3600
5000
Disabled
Enabled
No
Length Step Size (m)
Flow Initial Guess (kgmole/h)
Flow Step Size (kgmole/h)
Diam. Initial Guess (mm)
Default Increments
Check Choke Flow
1000
360.0
252.0
80.00
5 *
Disabled
User Variables
SIZING
Segment Number 1 2 3 4
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USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
SIZING
Fitting/Pipe
Distance (m)
Elevation Change (m)
Schedule
Nominal Diameter (mm)
Outer Diameter (mm)
Inner Diameter (mm)
Material
Roughness (m)
Conductivity (W/m-K)
Increments
Pipe
7.170 *
7.170 *
Schedule 40
38.10
48.26
40.89
Mild Steel
4.572e-005
45.00
5
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
4.572e-005
45.00
1
Pipe
1.975 *
0.0000
Schedule 40
38.10
48.26
40.89
Mild Steel
4.572e-005
45.00
5
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
4.572e-005
45.00
1
Segment Number
Fitting/Pipe
Distance (m)
Elevation Change (m)
Schedule
Nominal Diameter (mm)
Outer Diameter (mm)
Inner Diameter (mm)
Material
Roughness (m)
Conductivity (W/m-K)
5
Pipe
10.89 *
0.0000
Schedule 40
38.10
48.26
40.89
Mild Steel
4.572e-005
45.00
6
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
4.572e-005
45.00
7
Pipe
13.03 *
0.0000
Schedule 40
38.10
48.26
40.89
Mild Steel
4.572e-005
45.00
8
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
4.572e-005
45.00
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CH2M HILL INC
Burlington, MA
USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
SIZING
Increments 5 1 5 1
Segment Number
Fitting/Pipe
Distance (m)
Elevation Change (m)
Schedule
Nominal Diameter (mm)
Outer Diameter (mm)
Inner Diameter (mm)
Material
Roughness (m)
Conductivity (W/m-K)
Increments
9
Pipe
4.000 *
0.0000
Schedule 40
38.10
48.26
40.89
Mild Steel
4.572e-005
45.00
5
10
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
4.572e-005
45.00
1
11
Pipe
3.750 *
3.750 *
Schedule 40
38.10
48.26
40.89
Mild Steel
4.572e-005
45.00
5
12
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
4.572e-005
45.00
1
Segment Number
Fitting/Pipe
Distance (m)
Elevation Change (m)
Schedule
Nominal Diameter (mm)
Outer Diameter (mm)
Inner Diameter (mm)
Material
13
Pipe
2.950 *
0.0000
Schedule 40
38.10
48.26
40.89
Mild Steel
14
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
15
Pipe
2.025 *
0.0000
Schedule 40
38.10
48.26
40.89
Mild Steel
16
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
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Burlington, MA
USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
SIZING
Roughness (m)
Conductivity (W/m-K)
Increments
4.572e-005
45.00
5
4.572e-005
45.00
1
4.572e-005
45.00
5
4.572e-005
45.00
1
Segment Number
Fitting/Pipe
Distance (m)
Elevation Change (m)
Schedule
Nominal Diameter (mm)
Outer Diameter (mm)
Inner Diameter (mm)
Material
Roughness (m)
Conductivity (W/m-K)
Increments
17
Pipe
0.6400 *
0.0000
Schedule 40
38.10
48.26
40.89
Mild Steel
4.572e-005
45.00
5
18
Elbow: 90 Std
2.044e-003
0.0000
Actual
---
48.26
40.89 *
Mild Steel
4.572e-005
45.00
1
19
Pipe
1.235 *
0.0000
Schedule 40
38.10
48.26
40.89
Mild Steel
4.572e-005
45.00
5
20
Elbow: 90 Std
2.044e-003
0.0000
Schedule 40
50.80
48.26
40.89 *
Mild Steel
4.572e-005
45.00
1
Segment Number
Fitting/Pipe
Distance (m)
Elevation Change (m)
Schedule
Nominal Diameter (mm)
Outer Diameter (mm)
21
Pipe
0.6800 *
0.0000
Schedule 40
38.10
48.26
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
SIZING
Inner Diameter (mm)
Material
Roughness (m)
Conductivity (W/m-K)
Increments
40.89
Mild Steel
4.572e-005
45.00
5
HEAT TRANSFER
Heat Loss: 518.8 kJ/h Ambient Temp: 25.00 C * Overall HTC: 1.760 kJ/h-m2-C
Inside Heat Transfer Coefficient Estimation
Include Inner HTC: Enabled Correlation: Profes
Pipe Wall Resistance Estimation
Include Pipe Wall Resistance: Enabled
Insulation Resistance Estimation
Include Conduction: Enabled Type: Urethane Foam Thermal Cond.: 1.800e-002 W/m-K * Thickness: 5.000e-002 m
Outside Heat Transfer Coefficient Estimation
Include Outer HTC Ambient Medium Ground Type Ground Conductivity Buried Depth
Enabled Ground Dry Peat 0.1700 W/m-K * 1.000 m
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CH2M HILL INC
Burlington, MA
USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Data
Distance
(m)
0.0000
7.170
7.170
9.145
9.145
20.04
20.04
33.06
33.06
37.06
37.06
40.81
40.81
43.76
43.76
45.79
45.79
46.43
Elevation
(m)
0.0000
7.170
7.170
7.170
7.170
7.170
7.170
7.170
7.170
7.170
7.170
10.92
10.92
10.92
10.92
10.92
10.92
10.92
Increments
5
1
5
1
5
1
5
1
5
1
5
1
5
1
5
1
5
1
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Data
Distance
(m)
46.43
47.66
47.66
48.34
Elevation
(m)
10.92
10.92
10.92
10.92
Increments
5
1
5
Pipe Table
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
0.0000
0.0000
358.8
65.30
0.0000
---
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
1.434
1.434
343.8
65.29
0.0000
10.75
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
2.868
2.868
328.8
65.29
0.0000
10.75
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
4.302
4.302
313.8
65.28
0.0000
10.75
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
---
0.3798
---
---
---
---
0.3798
---
---
---
---
0.3798
---
---
---
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
5.736
5.736
298.8
65.28
0.0000
10.75
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
---
0.3798
---
7.170
7.170
283.7
65.27
0.0000
10.75
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
---
0.3798
---
7.170
7.170
283.7
65.27
0.0000
0.0000
Liquid Only
1.000
---
---
---
176.0
---
0.3799
---
7.565
7.170
283.4
65.27
0.0000
10.75
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Deposit Thickness (mm)
Deposit Volume (m3)
---
---
---
---
---
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
7.960
7.170
283.2
65.27
0.0000
10.75
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
8.355
7.170
282.9
65.27
0.0000
10.75
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
8.750
7.170
282.7
65.27
0.0000
10.75
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
9.145
7.170
282.4
65.27
0.0000
10.75
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
Length (m) 9.145 11.32 13.50 15.68
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
7.170
282.4
65.27
0.0000
0.0000
Liquid Only
1.000
---
---
---
176.0
---
0.3799
---
---
---
7.170
281.0
65.26
0.0000
10.74
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
7.170
279.6
65.25
0.0000
10.74
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
7.170
278.2
65.24
0.0000
10.74
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
17.86
7.170
276.8
65.24
20.04
7.170
275.4
65.23
20.04
7.170
275.3
65.23
22.64
7.170
273.7
65.22
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
0.0000
10.74
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
0.0000
10.74
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
0.0000
0.0000
Liquid Only
1.000
---
---
---
176.0
---
0.3799
---
---
---
0.0000
10.73
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
25.25
7.170
272.0
65.21
0.0000
10.73
Liquid Only
27.85
7.170
270.3
65.20
0.0000
10.73
Liquid Only
30.46
7.170
268.6
65.19
0.0000
10.73
Liquid Only
33.06
7.170
267.0
65.18
0.0000
10.72
Liquid Only
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
33.06
7.170
266.9
65.18
0.0000
0.0000
Liquid Only
1.000
---
---
33.86
7.170
266.4
65.18
0.0000
10.72
Liquid Only
1.000
0.6429
0.0000
34.66
7.170
265.9
65.18
0.0000
10.72
Liquid Only
1.000
0.6429
0.0000
35.46
7.170
265.4
65.17
0.0000
10.72
Liquid Only
1.000
0.6429
0.0000
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
---
176.0
---
0.3799
---
---
---
0.0000
176.0
---
0.3798
---
---
---
0.0000
176.0
---
0.3798
---
---
---
0.0000
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
36.26
7.170
264.9
65.17
0.0000
10.72
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
37.06
7.170
264.3
65.17
0.0000
10.72
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
37.06
7.170
264.3
65.17
0.0000
0.0000
Liquid Only
1.000
---
---
---
176.0
---
37.81
7.920
256.5
65.17
0.0000
10.72
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
---
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
0.3798
---
---
---
0.3798
---
---
---
0.3799
---
---
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
38.56
8.670
248.6
65.16
0.0000
10.72
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
---
0.3798
---
---
39.31
9.420
240.7
65.16
0.0000
10.72
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
---
0.3798
---
---
40.06
10.17
232.9
65.16
0.0000
10.72
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
---
0.3798
---
---
40.81
10.92
225.0
65.15
0.0000
10.72
Liquid Only
1.000
0.6429
9.829
0.0000
176.0
---
0.3798
---
---
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Deposit Volume (m3) --- --- --- ---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
40.81
10.92
225.0
65.15
0.0000
0.0000
Liquid Only
1.000
---
---
---
176.0
---
0.3799
---
---
---
41.40
10.92
224.6
65.15
0.0000
10.72
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
41.99
10.92
224.2
65.15
0.0000
10.72
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
42.58
10.92
223.9
65.15
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
43.17
10.92
43.76
10.92
43.76
10.92
44.17
10.92
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
223.5
65.15
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
223.1
65.14
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
223.1
65.14
0.0000
0.0000
Liquid Only
1.000
---
---
---
176.0
---
0.3799
---
---
---
222.8
65.14
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
44.57
10.92
222.5
65.14
0.0000
44.98
10.92
222.3
65.14
0.0000
45.38
10.92
222.0
65.14
0.0000
45.79
10.92
221.7
65.14
0.0000
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
45.79
10.92
221.7
65.14
0.0000
0.0000
Liquid Only
1.000
45.91
10.92
221.6
65.14
0.0000
10.71
Liquid Only
1.000
46.04
10.92
221.5
65.14
0.0000
10.71
Liquid Only
1.000
46.17
10.92
221.5
65.14
0.0000
10.71
Liquid Only
1.000
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
---
---
---
176.0
---
0.3799
---
---
---
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
46.30
10.92
221.4
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
46.43
10.92
221.3
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
46.43
10.92
221.3
65.13
0.0000
0.0000
Liquid Only
1.000
---
---
---
46.67
10.92
221.1
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
176.0
---
0.3798
---
---
---
176.0
---
0.3798
---
---
---
176.0
---
0.3799
---
---
---
176.0
---
0.3798
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
46.92
10.92
220.9
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
47.17
10.92
220.8
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
47.41
10.92
220.6
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
47.66
10.92
220.5
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
---
---
---
---
---
---
---
---
---
---
---
---
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
47.66
10.92
220.4
65.13
0.0000
0.0000
Liquid Only
1.000
---
---
---
176.0
---
0.3799
---
---
---
47.80
10.92
220.3
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
47.93
10.92
220.2
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
48.07
10.92
220.2
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROFILES
Pipe Table
Length (m)
Elevation (m)
Pressure (kPa)
Temperature (C)
Vapour Fraction
Heat Transferred (kJ/h-m)
Flow Regime
Liquid HoldUp
Friction Gradient (kPa/m)
Static Gradient (kPa/m)
Accel. Gradient (kPa/m)
Liq. Reynolds
Vap. Reynolds
Liquid Velocity (m/s)
Vapour Velocity (m/s)
Deposit Thickness (mm)
Deposit Volume (m3)
48.20
10.92
220.1
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
48.34
10.92
220.0
65.13
0.0000
10.71
Liquid Only
1.000
0.6429
0.0000
0.0000
176.0
---
0.3798
---
---
---
CONDITIONS
Name 4 5 Q03
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
CONDITIONS
Vapour
Temperature (C)
Pressure (kPa)
Molar Flow (kgmole/h)
Mass Flow (kg/h)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
0.0000
65.2997
358.8220
6.0000
1800.0000
1.7358
-6.258e+005
-188.4
-3.7547e+06
0.0000
65.1276
219.9756
6.0000
1800.0000
1.7358
-6.259e+005
-188.6
-3.7554e+06
---
---
---
---
---
---
---
---
5.1875e+02
PROPERTIES
Name
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
4
300.0
3.341
1002
1.796
-2086
-0.6281
455.3
1.518
---
---
5
300.0
3.341
1002
1.796
-2086
-0.6288
455.1
1.517
---
---
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROPERTIES
Name
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
(kPa)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(kPa)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
4
---
2.122e-314
0.0000
0.0000
---
3.457
455.3
141.9
1037
4.989e-004
3.817e-002
10.22
---
0.0000
1.019
1.160
5.360e+004
88.26
1037
1.735
1.000
5
---
2.122e-314
0.0000
0.0000
---
3.457
455.1
141.9
1037
4.989e-004
2.341e-002
10.22
---
0.0000
1.019
1.160
5.823e+004
88.25
1037
1.735
1.000
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
PROPERTIES
Name
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kPa)
(kPa)
(m3/h)
4
0.2993
178.7
0.0000
34.38
0.1807
88.46
447.0
1.490
392.5
1.308
272.2
0.9073
1.673
---
---
1.735
1.503
5
0.2993
194.1
0.0000
34.39
0.1808
88.46
446.8
1.489
392.5
1.308
272.2
0.9074
1.672
---
---
1.735
1.503
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
DYNAMICS
Parameters
Pipe Flow Model 'Quick'n Dirty' Methods Pipe Friction Model turbulent Pipe Holdup Type one holdup per segment
Model Holdup Volume Off Base Elevation of Inlet Relative to Ground 0.0000 m *
DEPOSITION
Methods
Method None
Max. Time 6.048e+005 seconds
Time Step 4.320e+004 seconds
Simulation Time ---
Properties
Density 881.0 kg/m3
Thermal Conductivity 0.2596 W/m-K
Yield Strength 2.068 kPa
Profile
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
1
1.43400
---
---
---
---
2
2.86800
---
---
---
---
3
4.30200
---
---
---
---
4
5.73600
---
---
---
---
5
7.17000
---
---
---
---
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Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
DEPOSITION
Profile
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
58.2327
---
---
---
58.2331
---
---
---
58.2334
---
---
---
58.2337
---
---
---
58.2340
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
6
7.56500
---
---
---
---
58.2342
---
---
---
7
7.96000
---
---
---
---
58.2343
---
---
---
8
8.35500
---
---
---
---
58.2344
---
---
---
9
8.75000
---
---
---
---
58.2345
---
---
---
10
9.14500
---
---
---
---
58.2345
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
11
11.3230
---
---
---
---
12
13.5010
---
---
---
---
13
15.6790
---
---
---
---
14
17.8570
---
---
---
---
15
20.0350
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 28 of 33* Specified by user.Licensed to: CH2M HILL INC
CH2M HILL INC
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USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
DEPOSITION
Profile
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
58.2348
---
---
---
58.2353
---
---
---
58.2357
---
---
---
58.2362
---
---
---
58.2366
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
16
22.6400
---
---
---
---
58.2371
---
---
---
17
25.2450
---
---
---
---
58.2377
---
---
---
18
27.8500
---
---
---
---
58.2382
---
---
---
19
30.4550
---
---
---
---
58.2388
---
---
---
20
33.0600
---
---
---
---
58.2393
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
21
33.8600
---
---
---
---
22
34.6600
---
---
---
---
23
35.4600
---
---
---
---
24
36.2600
---
---
---
---
25
37.0600
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 29 of 33* Specified by user.Licensed to: CH2M HILL INC
CH2M HILL INC
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USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
DEPOSITION
Profile
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
58.2397
---
---
---
58.2398
---
---
---
58.2400
---
---
---
58.2402
---
---
---
58.2404
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
26
37.8100
---
---
---
---
58.2405
---
---
---
27
38.5600
---
---
---
---
58.2407
---
---
---
28
39.3100
---
---
---
---
58.2408
---
---
---
29
40.0600
---
---
---
---
58.2410
---
---
---
30
40.8100
---
---
---
---
58.2412
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
31
41.4000
---
---
---
---
32
41.9900
---
---
---
---
33
42.5800
---
---
---
---
34
43.1700
---
---
---
---
35
43.7600
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 30 of 33* Specified by user.Licensed to: CH2M HILL INC
CH2M HILL INC
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USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
DEPOSITION
Profile
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
58.2413
---
---
---
58.2414
---
---
---
58.2416
---
---
---
58.2417
---
---
---
58.2418
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
36
44.1650
---
---
---
---
58.2419
---
---
---
37
44.5700
---
---
---
---
58.2420
---
---
---
38
44.9750
---
---
---
---
58.2421
---
---
---
39
45.3800
---
---
---
---
58.2422
---
---
---
40
45.7850
---
---
---
---
58.2423
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
41
45.9130
---
---
---
---
42
46.0410
---
---
---
---
43
46.1690
---
---
---
---
44
46.2970
---
---
---
---
45
46.4250
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 31 of 33* Specified by user.Licensed to: CH2M HILL INC
CH2M HILL INC
Burlington, MA
USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
DEPOSITION
Profile
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
58.2423
---
---
---
58.2423
---
---
---
58.2424
---
---
---
58.2424
---
---
---
58.2424
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
46
46.6720
---
---
---
---
58.2425
---
---
---
47
46.9190
---
---
---
---
58.2425
---
---
---
48
47.1660
---
---
---
---
58.2426
---
---
---
49
47.4130
---
---
---
---
58.2426
---
---
---
50
47.6600
---
---
---
---
58.2427
---
---
---
Cell
Cum. Length (m)
Init. Dep. Thick. (mm)
Calc. Dep. Thick. (mm)
Dep. Volume (m3)
Dep. Rate (kg/s-m2)
51
47.7960
---
---
---
---
52
47.9320
---
---
---
---
53
48.0680
---
---
---
---
54
48.2040
---
---
---
---
55
48.3400
---
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 32 of 33* Specified by user.Licensed to: CH2M HILL INC
CH2M HILL INC
Burlington, MA
USA
Case Name: DIAGRAMA DE FLUJO1 y media .HSC
Unit Set: SI
Date/Time: Mon Oct 29 09:56:55 2012
Pipe Segment: PIPE-103 (continued)
DEPOSITION
Profile
Film Coefficient (kJ/h-m2-C)
Wall Temperature (C)
Fluid Temperature (C)
Critical Deposition Temperature (C)
58.2427
---
---
---
58.2427
---
---
---
58.2428
---
---
---
58.2428
---
---
---
58.2428
---
---
---
Limits
Allowable Max. Deposit Thickness ---
Allowable Overall Pressure Drop ---
Allowable Deposit Volume ---
Allowable Plug Pressure Drop ---
Max. Deposit Thickness ---
Overall Pressure Drop 138.846 kPa
Deposit Volume ---
Plug Pressure Drop ---
NOTES
Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 33 of 33* Specified by user.Licensed to: CH2M HILL INC