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Case Name:
1.Diseño (48°C-80barg).hsc
Unit Set:
TEG SHELL - 1066
Date/Time:
Mon May 20 16:45:04 2019
6
Absorber: G01-K01 TEG CONTACTOR @Main
7
8
9
CONDITIONS
10
11
Name
12
Vapour
13
Temperature
14
Pressure
15
Molar Flow
16
Mass Flow
(kg/h)
17
Std Ideal Liq Vol Flow
18
Molar Enthalpy
19
Molar Entropy
20
Heat Flow
LEAN TEG @Main
COLUMN GAS INLET @Main
RICH TEG @Main
0.0000
1.0000
0.0000
1.0000
48.0000
49.0115
49.1483
79.5000
*
DRY GAS OUTLET @Main
(C)
56.0000
(bar_g)
81.2143
80.0000
80.0000
(MMSCMD*)
0.0112
1.4998
0.0144
1.4966
2820.4803
63925.6441
2944.6641
63801.4604
(m3/h)
2.5023
171.6839
2.6883
171.4979
(kJ/kgmole)
-7.725e+005
-8.572e+004
-6.571e+005
-8.535e+004
(kJ/kgmole-C)
147.9
150.0
124.4
150.3
(kW)
-4.2312e+03
-6.2940e+04
-4.6334e+03
-6.2538e+04
21
PROPERTIES
22
23
Name
24
Molecular Weight
25
Molar Density
26
Mass Density
27
LEAN TEG @Main
COLUMN GAS INLET @Main
RICH TEG @Main
DRY GAS OUTLET @Main
143.0
24.18
116.0
24.19
(kgmole/m3)
7.336
4.171
8.871
4.098
(kg/m3)
1049
100.9
1029
99.13
Act. Volume Flow
(m3/h)
2.688
633.8
2.862
643.6
28
Mass Enthalpy
(kJ/kg)
-5401
-3544
-5665
-3529
29
Mass Entropy
(kJ/kg-C)
1.034
6.203
1.073
6.213
30
Heat Capacity
(kJ/kgmole-C)
346.1
75.17
287.1
74.40
31
Mass Heat Capacity
(kJ/kg-C)
2.420
3.108
2.475
3.076
32
LHV Molar Basis (Std)
(kJ/kgmole)
3.075e+006
1.146e+006
2.477e+006
1.148e+006
33
LHV Mass Basis (Std)
(kJ/kg)
2.150e+004
4.740e+004
2.135e+004
4.746e+004
34
Phase Fraction [Vol. Basis]
0.0000
1.000
1.404e-008
1.000
35
Phase Fraction [Mass Basis]
0.0000
1.000
4.769e-009
1.000
36
Partial Pressure of CO2
(bar_g)
-1.013
-0.7498
-1.013
-0.7516
37
Cost Based on Flow
(Cost/s)
0.0000
0.0000
0.0000
0.0000
38
Act. Gas Flow
(ACT_m3/h)
---
633.8
---
643.6
39
Avg. Liq. Density
(kgmole/m3)
7.880
15.40
9.442
15.38
40
Specific Heat
(kJ/kgmole-C)
346.1
75.17
287.1
74.40
41
Std. Gas Flow
(STD_m3/d)
1.119e+004
1.500e+006
1.440e+004
1.497e+006
42
Std. Ideal Liq. Mass Density
(kg/m3)
1127
372.3
1095
372.0
43
Act. Liq. Flow
(m3/h)
2.688
---
2.862
---
44
Z Factor
0.4096
---
---
0.7331
45
Watson K
8.817
17.32
8.922
17.33
46
User Property
---
---
---
---
47
Partial Pressure of H2S
-1.013
-1.013
-1.013
-1.013
48
Cp/(Cp - R)
1.025
1.124
1.030
1.126
49
Cp/Cv
1.054
1.769
1.066
1.748
50
Heat of Vap.
(kJ/kgmole)
---
8953
---
9010
51
Kinematic Viscosity
(cSt)
10.07
0.1551
9.701
0.1573
52
Liq. Mass Density (Std. Cond)
(kg/m3)
1062
129.9
1041
129.8
53
Liq. Vol. Flow (Std. Cond)
(m3/h)
2.656
492.0
2.829
491.4
54
Liquid Fraction
1.000
0.0000
1.000
0.0000
55
Molar Volume
(m3/kgmole)
0.1363
0.2398
0.1127
0.2440
56
Mass Heat of Vap.
(kJ/kg)
---
370.2
---
372.5
57
Phase Fraction [Molar Basis]
0.0000
1.0000
0.0000
1.0000
58
Surface Tension
59
Thermal Conductivity
60
Viscosity
61
Cv (Semi-Ideal)
62
Mass Cv (Semi-Ideal)
63
Cv
64
Mass Cv
65
Cv (Ent. Method)
66
Mass Cv (Ent. Method)
67
Cp/Cv (Ent. Method)
68
Reid VP at 37.8 C
69
Aspen Technology Inc.
(bar_g)
(dyne/cm)
42.48
---
41.30
---
(W/m-K)
0.1955
4.099e-002
0.1903
4.089e-002
(cP)
10.57
1.565e-002
9.983
1.560e-002
(kJ/kgmole-C)
337.8
66.86
278.7
66.09
(kJ/kg-C)
2.362
2.765
2.403
2.732
(kJ/kgmole-C)
328.4
42.50
269.3
42.57
(kJ/kg-C)
2.296
1.757
2.321
1.760
(kJ/kgmole-C)
---
---
---
---
(kJ/kg-C)
---
---
---
---
---
---
---
---
---
---
---
---
(bar_g)
Licensed to: Company Name Not Available
Aspen HYSYS Version 10
Page 1 of 4
* Specified by user.
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Case Name:
1.Diseño (48°C-80barg).hsc
Unit Set:
TEG SHELL - 1066
Date/Time:
Mon May 20 16:45:04 2019
6
Absorber: G01-K01 TEG CONTACTOR @Main (continued)
7
8
9
PROPERTIES
10
11
Name
12
True VP at 37.8 C
13
Liq. Vol. Flow - Sum(Std. Cond)
14
Viscosity Index
15
LEAN TEG @Main
COLUMN GAS INLET @Main
RICH TEG @Main
DRY GAS OUTLET @Main
(bar_g)
---
---
---
---
(m3/h)
2.656
492.0
2.829
491.4
23.61
---
23.40
---
HHV Molar Basis (Std)
(kJ/kgmole)
3.349e+006
1.251e+006
2.703e+006
1.253e+006
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HHV Mass Basis (Std)
(kJ/kg)
2.341e+004
5.172e+004
2.330e+004
5.178e+004
17
CO2 Loading
---
---
---
---
18
CO2 Apparent Mole Conc.
(kgmole/m3)
2.976e-005
---
8.437e-003
---
19
CO2 Apparent Wt. Conc.
(kgmol/kg)
2.836e-008
---
8.199e-006
---
20
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
4.903e-008
1.000
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Mass Exergy
10.78
414.5
11.50
414.3
22
Ideal Gas Cp/Cv
1.036
1.206
1.045
1.205
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Ideal Gas Cp
(kJ/kgmole-C)
242.0
48.73
193.0
48.84
24
Mass Ideal Gas Cp
(kJ/kg-C)
1.692
2.015
1.664
2.019
25
Bubble Point Pressure
(bar_g)
-0.2523
120.0
80.00
10.44
(kJ/kg)
26
SUMMARY
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28
Flow Basis:
Mass
29
The composition option is selected
Feed Composition
30
@TEG Pobre
GAS Rico
Flow Rate (kg/h)
2.820480e+03
6.392564e+04
---
---
Nitrogen
0.0000
0.0076
34
CO2
0.0000
0.0059
35
Methane
0.0000
0.4416
36
Ethane
0.0000
0.1997
37
Propane
0.0000
0.1841
38
i-Butane
0.0000
0.0279
39
n-Butane
0.0000
0.0804
40
i-Pentane
0.0000
0.0179
41
n-Pentane
0.0000
0.0175
42
n-Hexane
0.0000
0.0116
43
n-Heptane
0.0000
0.0032
44
n-Octane
0.0000
0.0014
45
n-Nonane
0.0000
0.0000
46
n-Decane
0.0000
0.0000
47
H2O
0.0067
0.0012
48
Oxygen
0.0000
0.0000
49
TEGlycol
0.9931
0.0000
50
CO
0.0000
31
32
33
51
Flow Basis:
0.0000
Mass
52
The composition option is selected
Feed Flows
53
@TEG Pobre
GAS Rico
Flow Rate (kg/h)
2.820480e+03
6.392564e+04
---
---
Nitrogen (kg/h)
0.0012
487.7248
57
CO2 (kg/h)
0.0035
378.2528
58
Methane (kg/h)
0.1004
2.823100e+04
59
Ethane (kg/h)
0.1020
1.276403e+04
60
Propane (kg/h)
0.1200
1.176880e+04
61
i-Butane (kg/h)
0.0171
1.783262e+03
62
n-Butane (kg/h)
0.0459
5.138803e+03
63
i-Pentane (kg/h)
0.0053
1.141327e+03
64
n-Pentane (kg/h)
0.0054
1.121202e+03
65
n-Hexane (kg/h)
0.0008
742.9752
66
n-Heptane (kg/h)
0.0000
202.3720
67
n-Octane (kg/h)
0.0000
86.8180
68
n-Nonane (kg/h)
0.0000
54
55
56
69
Aspen Technology Inc.
Licensed to: Company Name Not Available
0.0000
Aspen HYSYS Version 10
Page 2 of 4
* Specified by user.
1
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4
5
Case Name:
1.Diseño (48°C-80barg).hsc
Unit Set:
TEG SHELL - 1066
Date/Time:
Mon May 20 16:45:04 2019
6
Absorber: G01-K01 TEG CONTACTOR @Main (continued)
7
8
9
SUMMARY
10
11
@TEG Pobre
GAS Rico
12
n-Decane (kg/h)
0.0000
0.0000
13
H2O (kg/h)
18.9291
79.0817
14
Oxygen (kg/h)
0.0000
0.0000
15
TEGlycol (kg/h)
2.801150e+03
0.0000
16
CO (kg/h)
0.0000
17
18
0.0000
Products
Flow Basis:
Mass
19
The composition option is selected
Product Compositions
20
@GAS Pobre
@TEG Rico
Flow Rate (kg/h)
6.380146e+04
2.944664e+03
---
---
Nitrogen
0.0076
0.0000
24
CO2
0.0059
0.0004
25
Methane
0.4423
0.0032
26
Ethane
0.1999
0.0032
27
Propane
0.1843
0.0041
28
i-Butane
0.0279
0.0007
29
n-Butane
0.0804
0.0028
30
i-Pentane
0.0179
0.0005
31
n-Pentane
0.0175
0.0007
32
n-Hexane
0.0116
0.0007
33
n-Heptane
0.0032
0.0002
34
n-Octane
0.0014
0.0001
35
n-Nonane
0.0000
0.0000
36
n-Decane
0.0000
0.0000
37
H2O
0.0000
0.0323
38
Oxygen
0.0000
0.0000
39
TEGlycol
0.0000
0.9510
40
CO
0.0000
21
22
23
41
Flow Basis:
0.0000
Mass
42
The composition option is selected
Product Flows
43
@GAS Pobre
44
Flow Rate (kg/h)
45
@TEG Rico
*
6.380146e+04
---
2.944664e+03
*
---
46
Nitrogen (kg/h)
487.6732
*
0.0528
*
47
CO2 (kg/h)
377.1937
*
1.0625
*
48
Methane (kg/h)
2.822183e+04
*
9.2768
*
49
Ethane (kg/h)
1.275468e+04
*
9.4541
*
50
Propane (kg/h)
1.175682e+04
*
12.1014
*
51
i-Butane (kg/h)
1.781093e+03
*
2.1858
*
52
n-Butane (kg/h)
5.130559e+03
*
8.2904
*
53
i-Pentane (kg/h)
1.139736e+03
*
1.5966
*
54
n-Pentane (kg/h)
1.119041e+03
*
2.1661
*
55
n-Hexane (kg/h)
741.0432
*
1.9329
*
56
n-Heptane (kg/h)
201.6743
*
0.6977
*
57
n-Octane (kg/h)
86.4142
*
0.4038
*
58
n-Nonane (kg/h)
0.0000
*
0.0000
*
59
n-Decane (kg/h)
0.0000
*
0.0000
*
60
H2O (kg/h)
2.9413
*
95.0695
*
61
Oxygen (kg/h)
0.0000
*
0.0000
*
62
TEGlycol (kg/h)
0.7759
*
2.800374e+03
*
63
CO (kg/h)
0.0000
*
0.0000
64
Flow Basis:
Mass
65
Product Recoveries
66
67
Flow Rate (kg/h)
68
69
*
The composition option is selected
@GAS Pobre
@TEG Rico
6.380146e+04
2.944664e+03
---
Aspen Technology Inc.
Licensed to: Company Name Not Available
---
Aspen HYSYS Version 10
Page 3 of 4
* Specified by user.
1
2
3
4
5
Case Name:
1.Diseño (48°C-80barg).hsc
Unit Set:
TEG SHELL - 1066
Date/Time:
Mon May 20 16:45:04 2019
6
Absorber: G01-K01 TEG CONTACTOR @Main (continued)
7
8
9
SUMMARY
10
11
@GAS Pobre
@TEG Rico
12
Nitrogen (%)
99.9892
0.0108
13
CO2 (%)
99.7191
0.2809
14
Methane (%)
99.9671
0.0329
15
Ethane (%)
99.9259
0.0741
16
Propane (%)
99.8972
0.1028
17
i-Butane (%)
99.8774
0.1226
18
n-Butane (%)
99.8387
0.1613
19
i-Pentane (%)
99.8601
0.1399
20
n-Pentane (%)
99.8068
0.1932
21
n-Hexane (%)
99.7398
0.2602
22
n-Heptane (%)
99.6552
0.3448
23
n-Octane (%)
99.5349
0.4651
24
n-Nonane (%)
0.0000
0.0000
25
n-Decane (%)
0.0000
0.0000
26
H2O (%)
3.0010
96.9990
27
Oxygen (%)
0.0000
0.0000
28
TEGlycol (%)
0.0277
99.9723
29
CO (%)
0.0000
0.0000
30
COLUMN PROFILES
31
32
Reflux Ratio:
8.070e-003
Reboil Ratio:
---
33
The Flows Option is Selected
Flow Basis:
Mass
Column Profiles Flows
34
Temp
Pres
Net Liq
Net Vap
Net Feed
Net Draws
Duty
35
(C)
(bar_g)
(kg/h)
(kg/h)
(kg/h)
(kg/h)
(kW)
36
[email protected]
49.1
79.50
2875
---
2820
6.380e+004
---
37
[email protected]
49.0
79.75
2883
6.386e+004
---
---
---
38
[email protected]
49.0
80.00
---
6.386e+004
6.393e+004
2945
---
39
Column Profiles Energy
40
Temperature
Liq Enthalpy
Vap Enthalpy
Heat Loss
41
(C)
(kJ/kgmole)
(kJ/kgmole)
(kW)
42
[email protected]
49.15
-7.262e+005
-8.535e+004
---
43
[email protected]
49.02
-7.165e+005
-8.539e+004
---
44
[email protected]
49.01
-6.571e+005
-8.543e+004
---
45
FEEDS / PRODUCTS
46
47
Flow Basis:
Mass
48
Stream
Type
Duty
49
50
51
52
53
54
Enthalpy
(kg/h)
(kJ/kgmole)
Temp
(C)
Feed
---
Liquid
2.82e+003
*
-7.7e+005
*
56.00
*
@GAS Pobre
Draw
---
Vapour
6.38e+004
*
-8.5e+004
*
49.15
*
GAS Rico
Feed
---
Vapour
6.39e+004
*
-8.6e+004
*
48.02
*
@TEG Rico
Draw
---
Liquid
2.94e+003
*
-6.6e+005
*
49.01
*
3
*
[email protected]
[email protected]
[email protected]
PERFORMANCE SUMMARY FOR INTERNAL OPTION:
56
57
Number Of Stages
58
Total Height
59
Total Head Loss
60
Total Pressure Drop
61
Number Of Sections
62
Number Of Diameters
63
Pressure Drop Across Sump
Section
CS-1
[email protected]@[email protected]
(m)
1.800
(mm)
483.7
(mbar)
48.99
1
1
Start
(bar)
End
65
66
Flows
@TEG Pobre
55
64
State
(kW)
[email protected]
[email protected]
4.236e-003
Height
Diameter
Internals
Tray or Packing
Section Pressure Drop
Approach To Flood
Limiting
(m)
(m)
Type
Type
(mbar)
(%)
Stage
Trayed
Bubble Cap
48.99
56.76
0.6000
*
1.203
*
67
68
69
Aspen Technology Inc.
Licensed to: Company Name Not Available
Aspen HYSYS Version 10
Page 4 of 4
* Specified by user.