Output Summary Page 1

Released to the following company:

HP
Eduardo
Xist 7.3.2 26/8/2021 00:26 SN: 46639- SI Units

: Summary Unit
Design - Horizontal With Single-Segmental Baffles
No Data Check Messages.
No Runtime Messages.
Process Conditions Cold Shellside Hot Tubeside
Fluid name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Flow rate (kg/s) 15,250 9,6100
Inlet/Outlet Y (Wt. frac vap.) 1,0000 1,0000 1,0000 1,0000
Inlet/Outlet T (Deg C) 537,10 650,00 750,00 558,70
Inlet P/Avg (kPa) 170,00 1080,0 755,39
dP/Allow. (kPa) 63,005 85,000 649,23 540,00
Fouling (m2-K/W) 0,000352 0,000352
Exchanger Performance
Shell h (W/m2-K) 378,01 Actual U (W/m2-K) 210,64
Tube h (W/m2-K) 835,75 Required U (W/m2-K) 180,53
Hot regime (--) Sens. Gas Duty (MegaWatts) 4,1677
Cold regime (--) Sens. Gas Eff. area (m2) 553,91
EMTD (Deg C) 41,7 Overdesign (%) 16,68
Shell Geometry Baffle Geometry
TEMA type (--) AES Baffle type Single-Seg.
Shell ID (mm) 914,40 Baffle cut (Pct Dia.) 25
Series (--) 3 Baffle orientation (--) Perpend.
Parallel (--) 2 Central spacing (mm) 1093,6
Orientation (deg) 0,00 Crosspasses (--) 5
Tube Geometry Nozzles
Tube type (--) Plain Shell inlet (mm)
Tube OD (mm) 44,450 Shell outlet (mm)
Length (m) 6,096 Inlet height (mm) 118,02
Pitch ratio (--) 1,3333 Outlet height (mm) 118,02
Layout (deg) 30 Tube inlet (mm)
Tubecount (--) 116 Tube outlet (mm)
Tube Pass (--) 6
Thermal Resistance; % Velocities; m/s Flow Fractions
Shell 55,72 Min Max A 0,017
Tube 27,23 Tubeside 60,69 93,17 B 0,402
Fouling 15,42 Crossflow 25,55 34,70 C 0,477
Metal 1,63 Window 32,80 39,87 E 0,029
F 0,076

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 Series Summary Page 2
Released to the following company:
HP
Eduardo
Xist 7.3.2 26/8/2021 00:26 SN: 46639- SI Units

: Summary Unit
Design - Horizontal Multipass Flow TEMA AES Shell With Single-Segmental Baffles
Unit # 1 2 3
Performance
Overdesign (%) 17,09 16,80 16,13
Overall U (W/m2-K) 215,30 209,98 206,64
Required U (W/m2-K) 183,87 179,77 177,93
Duty (MegaWatts) 2,1522 1,2654 0,7500
Shellside h (W/m2-K) 385,00 377,10 371,88
Tubeside h (W/m2-K) 869,19 830,71 808,34
Shellside delta P (kPa) 21,891 20,933 20,182
Tubeside delta P (kPa) 232,06 214,56 202,61
EMTD (C) 63,4 38,1 22,8
Process Conditions
Inlet T, Shell (C) 592,32 557,81 537,10
Outlet T, Shell (C) 650,00 592,32 557,81
Inlet T, Tube (C) 750,00 652,38 593,82
Outlet T, Tube (C) 652,38 593,82 558,70
Inlet Y, Shell (Wt. fraction) 1,0000 1,0000 1,0000
Outlet Y, Shell (Wt. fraction) 1,0000 1,0000 1,0000
Inlet Y, Tube (Wt. fraction) 1,0000 1,0000 1,0000
Outlet Y, Tube (Wt. fraction) 1,0000 1,0000 1,0000
Geometry
Shell type (--) E E E
Parallel (--) 2 2 2
Effective area (m2) 184,64 184,64 184,64
Shell orientation (--) Horizontal Horizontal Horizontal
Shell ID (mm) 914,40 914,40 914,40
Shellside fluid (--) Cold Cold Cold
Baffle type (--) Single-Seg. Single-Seg. Single-Seg.
Baffle cut (Pct Dia.) 25 25 25
Baffle orientation (--) Perpend. Perpend. Perpend.
Central spacing (mm) 1093,6 1093,6 1093,6
Crosspasses (--) 5 5 5
Tube type (--) Plain Plain Plain
Tube Pass (--) 6 6 6
Tubecount (--) 116 116 116
Tube length (m) 6,096 6,096 6,096
Tube OD (mm) 44,450 44,450 44,450
Tube layout angle (--) 30 30 30
Pitch ratio (--) 1,3333 1,3333 1,3333

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 Run Log Page 3
Released to the following HTRI Member Company:
HP
Eduardo
Xist 7.3.2 26/8/2021 00:26 SN: 46639- SI Units

: Summary Unit
Design - Horizontal Multipass Flow TEMA AES Shell With Single-Segmental Baffles
Beginning Design Run
Running Shortcut Design
**** DESIGN LOGIC MONITOR ****************************************************
*Shell Const.*** Velocity Drop Heat Transfer Tube Length= 0(ft)
Cross Cent Tube ------- ------- -------------- Over
Diam Pas Spce Pass Shl Tub Shl Tub Shell Tube Uo Area Mtd Delta Dsgn
---- --- ---- --- --- --- --- --- ----- ---- ---- ----- --- ---- ----- ----
0 0 0 6 -.0 -.0 -.0 -.0 0 0 0 0 0 0 1.000 0
0 0 0 6 -.0 -.0 -.0 -.0 0 0 0 0 0 0 1.000 0
Designing Smallest Shell to Pressure Drop. No. in Series= 3 Parallel= 1
60 5 34.1 6 192 164 17. 41. 67 110 34 8412 75 .8188 .9898 51.3
60 5 34.1 6 192 164 17. 41. 67 110 34 8412 75 .8188 .9898 51.3
Designing Smallest Shell to Pressure Drop. No. in Series= 3 Parallel= 2
60 5 38.5 6 86. 82. 4.3 11. 47 64 23 16824 75 .8188 .9910 107.
34 5 43.6 6 113 275 9.8 110 67 166 38 5263 76 .8188 .9977 7.6
44 5 41.9 6 98. 154 6.1 36. 58 105 31 9224 76 .8188 .9952 53.1
37 5 43.2 6 99. 234 7.4 80. 62 146 36 6158 76 .8188 .9977 16.8
40 5 42.7 6 97. 190 6.3 54. 59 123 33 7552 76 .8188 .9962 32.6
38 5 43.1 6 97. 227 6.9 75. 59 142 34 6352 76 .8188 .9977 15.6
Maximizing Heat Transfer to Meet Duty. No. in Series= 3 Parallel= 2
38 5 43.1 6 100 227 6.9 75. 58 142 34 6352 76 .8188 .9977 15.0
38 5 43.1 6 100 227 6.9 75. 58 142 34 6352 76 .8188 .9977 15.0
Running rigorous rating on shortcut design base case.
Running rigorous rating with larger and smaller values of shell inside diameter.
Running rigorous rating with larger and smaller values of shell inside diameter.
Running rigorous rating with larger and smaller values of central baffle spacing.
Running rigorous rating with larger and smaller values of central baffle spacing.
Running best case
Run Completed. Solution Reached in 01:32.

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 HEAT EXCHANGER RATING DATA SHEET Page 4
SI Units

Service of Unit Item No.

Type AES Orientation Horizontal Connected In 2 Parallel 3 Series
Surf/Unit (Gross/Eff) 592,48 / 553,91 m2 Shell/Unit 6 Surf/Shell (Gross/Eff) 98,747 / 92,318 m2
PERFORMANCE OF ONE UNIT
Fluid Allocation Shell Side Tube Side
Fluid Name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Fluid Quantity, Total kg/s 15,250 9,6100
Vapor (In/Out) wt% 100,00 100,00 100,00 100,00
Liquid wt% 0,00 0,00 0,00 0,00
Temperature (In/Out) C 537,10 650,00 750,00 558,70
Density kg/m3 0,6378 0,5595 2,2939 2,8345
Viscosity mN-s/m2 0,0242 0,0283 0,0299 0,0309
Specific Heat kJ/kg-C 2,3627 2,4712 2,3208 2,2108
Thermal Conductivity W/m-C 0,0716 0,0830 0,0886 0,0759
Critical Pressure kPa
Inlet Pressure kPa 170,00 1080,0
Velocity m/s 32,66 85,95
Pressure Drop, Allow/Calc kPa 85,000 63,005 540,00 649,23
Average Film Coefficient W/m2-K 378,01 835,75
Fouling Resistance (min) m2-K/W 0,000352 0,000352
Heat Exchanged 4,1677 MegaWatts MTD (Corrected) 41,7 C Overdesign 16,68 %
Transfer Rate, Service 180,53 W/m2-K Calculated 210,64 W/m2-K Clean 249,07 W/m2-K
CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)
Shell Side Tube Side
Design Pressure kPaG 517,11 1103,2
Design Temperature C 682,22 782,22
No Passes per Shell 1 6
Flow Direction Downward Downward
Connections In mm 1 @ 1 @
Size & Out mm 1 @ 1 @
Rating Liq. Out mm @ 1 @
Tube No. 116,00 OD 44,450 mm Thk(Avg) 1,651 mm Length 6,096 m Pitch 59,267 mm Tube pattern 30
Tube Type Plain Material NI-FE-CR alloy 800 & 800H (N088 Pairs seal strips 1
Shell ID 914,40 mm Kettle ID mm Passlane Seal Rod No.
Cross Baffle Type Perpend. Single-Seg. %Cut (Diam) 25 Impingement Plate None
Spacing(c/c) 1093,6 mm Inlet mm No. of Crosspasses 5
Rho-V2-Inlet Nozzle kg/m-s2 Shell Entrance kg/m-s2 Shell Exit kg/m-s2
Bundle Entrance kg/m-s2 Bundle Exit kg/m-s2
Weight/Shell kg Filled with Water kg Bundle kg
Notes: Thermal Resistance, % Velocities; m/s Flow Fractions
Shell 55,72 Shellside 32,66 A 0,017
Tube 27,23 Tubeside 85,95 B 0,402
Fouling 15,42 Crossflow 34,79 C 0,477
Metal 1,63 Window 117,01 E 0,029
F 0,076

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 HEAT EXCHANGER SPECIFICATION SHEET Page 5
SI Units

Job No.
Customer E-103 Reference No.
Address Proposal No.
Plant Location Date 26/8/2021 Rev
Service of Unit Item No.
Size 914,4 x 6096 mm Type AES Horizontal Connected In 2 Parallel 3 Series
Surf/Unit (Gross/Eff) 592,48 / 553,91 m2 Shell/Unit 6 Surf/Shell (Gross/Eff) 98,747 / 92,318 m2
PERFORMANCE OF ONE UNIT
Fluid Allocation Shell Side Tube Side
Fluid Name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Fluid Quantity, Total kg/hr 54900 34596
Vapor (In/Out) 54900 54900 34596 34596
Liquid
Steam
Water
Noncondensables
Temperature (In/Out) C 537,10 650,00 750,00 558,70
Specific Gravity
Viscosity mN-s/m2 0,0242 0,0283 0,0299 0,0309
Molecular Weight, Vapor
Molecular Weight, Noncondensables
Specific Heat kJ/kg-C 2,3627 2,4712 2,3208 2,2108
Thermal Conductivity W/m-C 0,0716 0,0830 0,0886 0,0759
Latent Heat kJ/kg
Inlet Pressure kPa 170,00 1080,0
Velocity m/s 32,66 85,95
Pressure Drop, Allow/Calc kPa 85,000 63,005 540,00 649,23
Fouling Resistance (min) m2-K/W 0,000352 0,000352
Heat Exchanged 4167660 W MTD (Corrected) 41,7 C
Transfer Rate, Service 180,53 W/m2-K Clean 249,07 W/m2-K Actual 210,64 W/m2-K
CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)
Shell Side Tube Side
Design/Test Pressure kPaG 517,11 / 1103,2 /
Design Temperature C 682,22 782,22
No Passes per Shell 1 6
Corrosion Allowance mm 3,000 3,000
Connections In mm 1 @ 1 @
Size & Out mm 1 @ 1 @
Rating Intermediate @ @
Tube No. 116 OD 44,450 mm Thk(Avg) 1,651 mm Length 6,096 m Pitch 59,267 mm
Tube Type Plain Material NI-FE-CR alloy 800 & 800H (N08800 & H088 Tube pattern30
Shell NI-FE-CR alloy 800 & 800H (N0 ID 914,40 OD mm Shell Cover NI-FE-CR alloy 800 & 800H (Remove.)
Channel or Bonnet NI-FE-CR alloy 800 & 800H (N08800 & H08810) Channel Cover NI-FE-CR alloy 800 & 800H (N08800 &
Tubesheet-Stationary NI-FE-CR alloy 800 & 800H (N08800 & H08810) Tubesheet-Floating NI-FE-CR alloy 800 & 800H (N088
Floating Head Cover NI-FE-CR alloy 800 & 800H (N08800 & H08810) Impingement Plate None
Baffles-Cross NI-FE-CR alloy 800 & 80 Type Single-Seg. %Cut (Diam) 25 Spacing(c/c) 1093,6 Inlet mm
Baffles-Long Seal Type
Supports-Tube U-Bend Type None
Bypass Seal Arrangement 1 pairs seal strips Tube-Tubesheet Joint
Expansion Joint Type
Rho-V2-Inlet Nozzle kg/m-s2 Bundle Entrance Bundle Exit kg/m-s2
Gaskets-Shell Side Ring Joint (Ni Alloy) Tube Side Ring Joint (Ni Alloy)
- Floating Head Ring Joint (Ni Alloy)
Code Requirements ASME TEMA Class
Weight/Shell kg Filled with Water kg Bundle kg
Remarks:

Reprinted with Permission (v7,3.2)

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 Output Summary Page 6
Released to the following company:
HP
Eduardo
Xist 7.3.2 26/8/2021 00:26 SN: 46639- SI Units

: Shell 1
Rating - Horizontal Multipass Flow TEMA AES Shell With Single-Segmental Baffles
See Data Check Messages Report for Informative Messages.
See Runtime Message Report for Warning Messages.
Process Conditions Cold Shellside Hot Tubeside
Fluid name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Flow rate (kg/s) 15,250 9,6100
Inlet/Outlet Y (Wt. frac vap.) 1,0000 1,0000 1,0000 1,0000
Inlet/Outlet T (Deg C) 592,32 650,00 750,00 652,38
Inlet P/Avg (kPa) 128,88 117,93 1080,0 963,97
dP/Allow. (kPa) 21,891 85,000 232,06 540,00
Fouling (m2-K/W) 0,000352 0,000352
Exchanger Performance
Shell h (W/m2-K) 385,00 Actual U (W/m2-K) 215,30
Tube h (W/m2-K) 869,19 Required U (W/m2-K) 183,87
Hot regime (--) Sens. Gas Duty (MegaWatts) 2,1522
Cold regime (--) Sens. Gas Eff. area (m2) 184,64
EMTD (Deg C) 63,4 Overdesign (%) 17,09
Shell Geometry Baffle Geometry
TEMA type (--) AES Baffle type Single-Seg.
Shell ID (mm) 914,40 Baffle cut (Pct Dia.) 25
Series (--) 1 Baffle orientation (--) Perpend.
Parallel (--) 2 Central spacing (mm) 1093,6
Orientation (deg) 0,00 Crosspasses (--) 5
Tube Geometry Nozzles
Tube type (--) Plain Shell inlet (mm) 822,96
Tube OD (mm) 44,450 Shell outlet (mm) 822,96
Length (m) 6,096 Inlet height (mm) 118,02
Pitch ratio (--) 1,3333 Outlet height (mm) 118,02
Layout (deg) 30 Tube inlet (mm) 258,88
Tubecount (--) 116 Tube outlet (mm) 258,88
Tube Pass (--) 6
Thermal Resistance; % Velocities; m/s Flow Fractions
Shell 55,92 Min Max A 0,017
Tube 26,76 Tubeside 67,71 93,17 B 0,401
Fouling 15,77 Crossflow 27,39 34,70 C 0,478
Metal 1,55 Window 35,01 39,87 E 0,029
F 0,076

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 HEAT EXCHANGER RATING DATA SHEET Page 7
SI Units

Service of Unit Item No.

Type AES Orientation Horizontal Connected In 2 Parallel 1 Series
Surf/Unit (Gross/Eff) 197,49 / 184,64 m2 Shell/Unit 2 Surf/Shell (Gross/Eff) 98,747 / 92,318 m2
PERFORMANCE OF ONE UNIT
Fluid Allocation Shell Side Tube Side
Fluid Name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Fluid Quantity, Total kg/s 15,250 9,6100
Vapor (In/Out) wt% 100,00 100,00 100,00 100,00
Liquid wt% 0,00 0,00 0,00 0,00
Temperature (In/Out) C 592,32 650,00 750,00 652,38
Density kg/m3 0,5969 0,5595 2,2939 2,5406
Viscosity mN-s/m2 0,0262 0,0283 0,0299 0,0347
Specific Heat kJ/kg-C 2,4181 2,4712 2,3208 2,2656
Thermal Conductivity W/m-C 0,0774 0,0830 0,0886 0,0886
Critical Pressure kPa
Inlet Pressure kPa 128,88 1080,0
Velocity m/s 34,25 92,03
Pressure Drop, Allow/Calc kPa 85,000 21,891 540,00 232,06
Average Film Coefficient W/m2-K 385,00 869,19
Fouling Resistance (min) m2-K/W 0,000352 0,000352
Heat Exchanged 2,1522 MegaWatts MTD (Corrected) 63,4 C Overdesign 17,09 %
Transfer Rate, Service 183,87 W/m2-K Calculated 215,30 W/m2-K Clean 255,60 W/m2-K
CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)
Shell Side Tube Side
Design Pressure kPaG 517,11 1103,2
Design Temperature C 682,22 782,22
No Passes per Shell 1 6
Flow Direction Downward Downward
Connections In mm 1 @ 822,96 1 @ 258,88
Size & Out mm 1 @ 822,96 1 @ 258,88
Rating Liq. Out mm @ 1 @
Tube No. 116,00 OD 44,450 mm Thk(Avg) 1,651 mm Length 6,096 m Pitch 59,267 mm Tube pattern 30
Tube Type Plain Material NI-FE-CR alloy 800 & 800H (N088 Pairs seal strips 1
Shell ID 914,40 mm Kettle ID mm Passlane Seal Rod No. 3
Cross Baffle Type Perpend. Single-Seg. %Cut (Diam) 25 Impingement Plate None
Spacing(c/c) 1093,6 mm Inlet 1268,4 mm No. of Crosspasses 5
Rho-V2-Inlet Nozzle 344,24 kg/m-s2 Shell Entrance 620,33 kg/m-s2 Shell Exit 661,83 kg/m-s2
Bundle Entrance 458,24 kg/m-s2 Bundle Exit 594,89 kg/m-s2
Weight/Shell 26269 kg Filled with Water 32128 kg Bundle 8505,8 kg
Notes: Thermal Resistance, % Velocities; m/s Flow Fractions
Shell 55,92 Shellside 34,25 A 0,017
Tube 26,76 Tubeside 92,03 B 0,401
Fouling 15,77 Crossflow 36,53 C 0,478
Metal 1,55 Window 122,80 E 0,029
F 0,076

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 HEAT EXCHANGER SPECIFICATION SHEET Page 8
SI Units

Job No.
Customer E-103 Reference No.
Address Proposal No.
Plant Location Date 26/8/2021 Rev
Service of Unit Item No.
Size 914,4 x 6096 mm Type AES Horizontal Connected In 2 Parallel 1 Series
Surf/Unit (Gross/Eff) 197,49 / 184,64 m2 Shell/Unit 2 Surf/Shell (Gross/Eff) 98,747 / 92,318 m2
PERFORMANCE OF ONE UNIT
Fluid Allocation Shell Side Tube Side
Fluid Name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Fluid Quantity, Total kg/hr 54900 34596
Vapor (In/Out) 54900 54900 34596 34596
Liquid
Steam
Water
Noncondensables
Temperature (In/Out) C 592,32 650,00 750,00 652,38
Specific Gravity
Viscosity mN-s/m2 0,0262 0,0283 0,0299 0,0347
Molecular Weight, Vapor
Molecular Weight, Noncondensables
Specific Heat kJ/kg-C 2,4181 2,4712 2,3208 2,2656
Thermal Conductivity W/m-C 0,0774 0,0830 0,0886 0,0886
Latent Heat kJ/kg
Inlet Pressure kPa 128,88 1080,0
Velocity m/s 34,25 92,03
Pressure Drop, Allow/Calc kPa 85,000 21,891 540,00 232,06
Fouling Resistance (min) m2-K/W 0,000352 0,000352
Heat Exchanged 2152237 W MTD (Corrected) 63,4 C
Transfer Rate, Service 183,87 W/m2-K Clean 255,60 W/m2-K Actual 215,30 W/m2-K
CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)
Shell Side Tube Side
Design/Test Pressure kPaG 517,11 / 1103,2 /
Design Temperature C 682,22 782,22
No Passes per Shell 1 6
Corrosion Allowance mm 3,000 3,000
Connections In mm 1 @ 822,96 1 @ 258,88
Size & Out mm 1 @ 822,96 1 @ 258,88
Rating Intermediate @ @
Tube No. 116 OD 44,450 mm Thk(Avg) 1,651 mm Length 6,096 m Pitch 59,267 mm
Tube Type Plain Material NI-FE-CR alloy 800 & 800H (N08800 & H088 Tube pattern30
Shell NI-FE-CR alloy 800 & 800H (N0 ID 914,40 OD 936,63 mm Shell Cover NI-FE-CR alloy 800 & 800H (Remove.)
Channel or Bonnet NI-FE-CR alloy 800 & 800H (N08800 & H08810) Channel Cover NI-FE-CR alloy 800 & 800H (N08800 &
Tubesheet-Stationary NI-FE-CR alloy 800 & 800H (N08800 & H08810) Tubesheet-Floating NI-FE-CR alloy 800 & 800H (N088
Floating Head Cover NI-FE-CR alloy 800 & 800H (N08800 & H08810) Impingement Plate None
Baffles-Cross NI-FE-CR alloy 800 & 80 Type Single-Seg. %Cut (Diam) 25 Spacing(c/c) 1093,6 Inlet 1268,4 mm
Baffles-Long Seal Type None
Supports-Tube U-Bend Type None
Bypass Seal Arrangement 1 pairs seal strips Tube-Tubesheet Joint Expanded (No groove)
Expansion Joint Type
Rho-V2-Inlet Nozzle 344,24 kg/m-s2 Bundle Entrance 458,24 Bundle Exit 594,89 kg/m-s2
Gaskets-Shell Side Ring Joint (Ni Alloy) Tube Side Ring Joint (Ni Alloy)
- Floating Head Ring Joint (Ni Alloy)
Code Requirements ASME TEMA Class R
Weight/Shell 26269 kg Filled with Water 32128 kg Bundle 8505,8 kg
Remarks:

Reprinted with Permission (v7,3.2)

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 Output Summary Page 9
Released to the following company:
HP
Eduardo
Xist 7.3.2 26/8/2021 00:26 SN: 46639- SI Units

: Shell 2
Rating - Horizontal Multipass Flow TEMA AES Shell With Single-Segmental Baffles
See Data Check Messages Report for Informative Messages.
See Runtime Message Report for Warning Messages.
Process Conditions Cold Shellside Hot Tubeside
Fluid name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Flow rate (kg/s) 15,250 9,6100
Inlet/Outlet Y (Wt. frac vap.) 1,0000 1,0000 1,0000 1,0000
Inlet/Outlet T (Deg C) 557,81 592,32 652,38 593,82
Inlet P/Avg (kPa) 149,82 139,35 847,95 740,66
dP/Allow. (kPa) 20,933 85,000 214,56 540,00
Fouling (m2-K/W) 0,000352 0,000352
Exchanger Performance
Shell h (W/m2-K) 377,10 Actual U (W/m2-K) 209,98
Tube h (W/m2-K) 830,71 Required U (W/m2-K) 179,77
Hot regime (--) Sens. Gas Duty (MegaWatts) 1,2654
Cold regime (--) Sens. Gas Eff. area (m2) 184,64
EMTD (Deg C) 38,1 Overdesign (%) 16,80
Shell Geometry Baffle Geometry
TEMA type (--) AES Baffle type Single-Seg.
Shell ID (mm) 914,40 Baffle cut (Pct Dia.) 25
Series (--) 1 Baffle orientation (--) Perpend.
Parallel (--) 2 Central spacing (mm) 1093,6
Orientation (deg) 0,00 Crosspasses (--) 5
Tube Geometry Nozzles
Tube type (--) Plain Shell inlet (mm) 742,95
Tube OD (mm) 44,450 Shell outlet (mm) 742,95
Length (m) 6,096 Inlet height (mm) 118,02
Pitch ratio (--) 1,3333 Outlet height (mm) 118,02
Layout (deg) 30 Tube inlet (mm) 258,88
Tubecount (--) 116 Tube outlet (mm) 258,88
Tube Pass (--) 6
Thermal Resistance; % Velocities; m/s Flow Fractions
Shell 55,68 Min Max A 0,017
Tube 27,31 Tubeside 63,39 85,68 B 0,402
Fouling 15,38 Crossflow 27,13 32,67 C 0,477
Metal 1,64 Window 34,81 37,57 E 0,029
F 0,076

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 HEAT EXCHANGER RATING DATA SHEET Page 10
SI Units

Service of Unit Item No.

Type AES Orientation Horizontal Connected In 2 Parallel 1 Series
Surf/Unit (Gross/Eff) 197,49 / 184,64 m2 Shell/Unit 2 Surf/Shell (Gross/Eff) 98,747 / 92,318 m2
PERFORMANCE OF ONE UNIT
Fluid Allocation Shell Side Tube Side
Fluid Name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Fluid Quantity, Total kg/s 15,250 9,6100
Vapor (In/Out) wt% 100,00 100,00 100,00 100,00
Liquid wt% 0,00 0,00 0,00 0,00
Temperature (In/Out) C 557,81 592,32 652,38 593,82
Density kg/m3 0,6218 0,5969 2,5406 2,7165
Viscosity mN-s/m2 0,0250 0,0262 0,0347 0,0323
Specific Heat kJ/kg-C 2,3840 2,4181 2,2656 2,2314
Thermal Conductivity W/m-C 0,0738 0,0774 0,0886 0,0806
Critical Pressure kPa
Inlet Pressure kPa 149,82 847,95
Velocity m/s 32,40 85,01
Pressure Drop, Allow/Calc kPa 85,000 20,933 540,00 214,56
Average Film Coefficient W/m2-K 377,10 830,71
Fouling Resistance (min) m2-K/W 0,000352 0,000352
Heat Exchanged 1,2654 MegaWatts MTD (Corrected) 38,1 C Overdesign 16,80 %
Transfer Rate, Service 179,77 W/m2-K Calculated 209,98 W/m2-K Clean 248,13 W/m2-K
CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)
Shell Side Tube Side
Design Pressure kPaG 517,11 1103,2
Design Temperature C 682,22 782,22
No Passes per Shell 1 6
Flow Direction Downward Downward
Connections In mm 1 @ 742,95 1 @ 258,88
Size & Out mm 1 @ 742,95 1 @ 258,88
Rating Liq. Out mm @ 1 @
Tube No. 116,00 OD 44,450 mm Thk(Avg) 1,651 mm Length 6,096 m Pitch 59,267 mm Tube pattern 30
Tube Type Plain Material NI-FE-CR alloy 800 & 800H (N088 Pairs seal strips 1
Shell ID 914,40 mm Kettle ID mm Passlane Seal Rod No. 3
Cross Baffle Type Perpend. Single-Seg. %Cut (Diam) 25 Impingement Plate None
Spacing(c/c) 1093,6 mm Inlet 1144,9 mm No. of Crosspasses 5
Rho-V2-Inlet Nozzle 497,49 kg/m-s2 Shell Entrance 759,40 kg/m-s2 Shell Exit 791,09 kg/m-s2
Bundle Entrance 539,90 kg/m-s2 Bundle Exit 454,68 kg/m-s2
Weight/Shell 26046 kg Filled with Water 31849 kg Bundle 8505,8 kg
Notes: Thermal Resistance, % Velocities; m/s Flow Fractions
Shell 55,68 Shellside 32,40 A 0,017
Tube 27,31 Tubeside 85,01 B 0,402
Fouling 15,38 Crossflow 34,52 C 0,477
Metal 1,64 Window 116,09 E 0,029
F 0,076

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 HEAT EXCHANGER SPECIFICATION SHEET Page 11
SI Units

Job No.
Customer E-103 Reference No.
Address Proposal No.
Plant Location Date 26/8/2021 Rev
Service of Unit Item No.
Size 914,4 x 6096 mm Type AES Horizontal Connected In 2 Parallel 1 Series
Surf/Unit (Gross/Eff) 197,49 / 184,64 m2 Shell/Unit 2 Surf/Shell (Gross/Eff) 98,747 / 92,318 m2
PERFORMANCE OF ONE UNIT
Fluid Allocation Shell Side Tube Side
Fluid Name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Fluid Quantity, Total kg/hr 54900 34596
Vapor (In/Out) 54900 54900 34596 34596
Liquid
Steam
Water
Noncondensables
Temperature (In/Out) C 557,81 592,32 652,38 593,82
Specific Gravity
Viscosity mN-s/m2 0,0250 0,0262 0,0347 0,0323
Molecular Weight, Vapor
Molecular Weight, Noncondensables
Specific Heat kJ/kg-C 2,3840 2,4181 2,2656 2,2314
Thermal Conductivity W/m-C 0,0738 0,0774 0,0886 0,0806
Latent Heat kJ/kg
Inlet Pressure kPa 149,82 847,95
Velocity m/s 32,40 85,01
Pressure Drop, Allow/Calc kPa 85,000 20,933 540,00 214,56
Fouling Resistance (min) m2-K/W 0,000352 0,000352
Heat Exchanged 1265432 W MTD (Corrected) 38,1 C
Transfer Rate, Service 179,77 W/m2-K Clean 248,13 W/m2-K Actual 209,98 W/m2-K
CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)
Shell Side Tube Side
Design/Test Pressure kPaG 517,11 / 1103,2 /
Design Temperature C 682,22 782,22
No Passes per Shell 1 6
Corrosion Allowance mm 3,000 3,000
Connections In mm 1 @ 742,95 1 @ 258,88
Size & Out mm 1 @ 742,95 1 @ 258,88
Rating Intermediate @ @
Tube No. 116 OD 44,450 mm Thk(Avg) 1,651 mm Length 6,096 m Pitch 59,267 mm
Tube Type Plain Material NI-FE-CR alloy 800 & 800H (N08800 & H088 Tube pattern30
Shell NI-FE-CR alloy 800 & 800H (N0 ID 914,40 OD 936,63 mm Shell Cover NI-FE-CR alloy 800 & 800H (Remove.)
Channel or Bonnet NI-FE-CR alloy 800 & 800H (N08800 & H08810) Channel Cover NI-FE-CR alloy 800 & 800H (N08800 &
Tubesheet-Stationary NI-FE-CR alloy 800 & 800H (N08800 & H08810) Tubesheet-Floating NI-FE-CR alloy 800 & 800H (N088
Floating Head Cover NI-FE-CR alloy 800 & 800H (N08800 & H08810) Impingement Plate None
Baffles-Cross NI-FE-CR alloy 800 & 80 Type Single-Seg. %Cut (Diam) 25 Spacing(c/c) 1093,6 Inlet 1144,9 mm
Baffles-Long Seal Type None
Supports-Tube U-Bend Type None
Bypass Seal Arrangement 1 pairs seal strips Tube-Tubesheet Joint Expanded (No groove)
Expansion Joint Type
Rho-V2-Inlet Nozzle 497,49 kg/m-s2 Bundle Entrance 539,90 Bundle Exit 454,68 kg/m-s2
Gaskets-Shell Side Ring Joint (Ni Alloy) Tube Side Ring Joint (Ni Alloy)
- Floating Head Ring Joint (Ni Alloy)
Code Requirements ASME TEMA Class R
Weight/Shell 26046 kg Filled with Water 31849 kg Bundle 8505,8 kg
Remarks:

Reprinted with Permission (v7,3.2)

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 Output Summary Page 12
Released to the following company:
HP
Eduardo
Xist 7.3.2 26/8/2021 00:26 SN: 46639- SI Units

: Shell 3
Rating - Horizontal Multipass Flow TEMA AES Shell With Single-Segmental Baffles
See Data Check Messages Report for Informative Messages.
See Runtime Message Report for Warning Messages.
Process Conditions Cold Shellside Hot Tubeside
Fluid name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Flow rate (kg/s) 15,250 9,6100
Inlet/Outlet Y (Wt. frac vap.) 1,0000 1,0000 1,0000 1,0000
Inlet/Outlet T (Deg C) 537,10 557,81 593,82 558,70
Inlet P/Avg (kPa) 170,00 159,91 633,38 532,08
dP/Allow. (kPa) 20,182 85,000 202,61 540,00
Fouling (m2-K/W) 0,000352 0,000352
Exchanger Performance
Shell h (W/m2-K) 371,88 Actual U (W/m2-K) 206,64
Tube h (W/m2-K) 808,34 Required U (W/m2-K) 177,93
Hot regime (--) Sens. Gas Duty (MegaWatts) 0,7500
Cold regime (--) Sens. Gas Eff. area (m2) 184,64
EMTD (Deg C) 22,8 Overdesign (%) 16,13
Shell Geometry Baffle Geometry
TEMA type (--) AES Baffle type Single-Seg.
Shell ID (mm) 914,40 Baffle cut (Pct Dia.) 25
Series (--) 1 Baffle orientation (--) Perpend.
Parallel (--) 2 Central spacing (mm) 1093,6
Orientation (deg) 0,00 Crosspasses (--) 5
Tube Geometry Nozzles
Tube type (--) Plain Shell inlet (mm) 742,95
Tube OD (mm) 44,450 Shell outlet (mm) 742,95
Length (m) 6,096 Inlet height (mm) 118,02
Pitch ratio (--) 1,3333 Outlet height (mm) 118,02
Layout (deg) 30 Tube inlet (mm) 307,09
Tubecount (--) 116 Tube outlet (mm) 307,09
Tube Pass (--) 6
Thermal Resistance; % Velocities; m/s Flow Fractions
Shell 55,57 Min Max A 0,017
Tube 27,61 Tubeside 60,69 81,22 B 0,402
Fouling 15,13 Crossflow 25,55 31,48 C 0,476
Metal 1,69 Window 32,80 36,20 E 0,029
F 0,076

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 HEAT EXCHANGER RATING DATA SHEET Page 13
SI Units

Service of Unit Item No.

Type AES Orientation Horizontal Connected In 2 Parallel 1 Series
Surf/Unit (Gross/Eff) 197,49 / 184,64 m2 Shell/Unit 2 Surf/Shell (Gross/Eff) 98,747 / 92,318 m2
PERFORMANCE OF ONE UNIT
Fluid Allocation Shell Side Tube Side
Fluid Name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Fluid Quantity, Total kg/s 15,250 9,6100
Vapor (In/Out) wt% 100,00 100,00 100,00 100,00
Liquid wt% 0,00 0,00 0,00 0,00
Temperature (In/Out) C 537,10 557,81 593,82 558,70
Density kg/m3 0,6378 0,6218 2,7165 2,8345
Viscosity mN-s/m2 0,0242 0,0250 0,0323 0,0309
Specific Heat kJ/kg-C 2,3627 2,3840 2,2314 2,2108
Thermal Conductivity W/m-C 0,0716 0,0738 0,0806 0,0759
Critical Pressure kPa
Inlet Pressure kPa 170,00 633,38
Velocity m/s 31,32 80,81
Pressure Drop, Allow/Calc kPa 85,000 20,182 540,00 202,61
Average Film Coefficient W/m2-K 371,88 808,34
Fouling Resistance (min) m2-K/W 0,000352 0,000352
Heat Exchanged 0,7500 MegaWatts MTD (Corrected) 22,8 C Overdesign 16,13 %
Transfer Rate, Service 177,93 W/m2-K Calculated 206,64 W/m2-K Clean 243,48 W/m2-K
CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)
Shell Side Tube Side
Design Pressure kPaG 517,11 1103,2
Design Temperature C 682,22 782,22
No Passes per Shell 1 6
Flow Direction Downward Downward
Connections In mm 1 @ 742,95 1 @ 307,09
Size & Out mm 1 @ 742,95 1 @ 307,09
Rating Liq. Out mm @ 1 @
Tube No. 116,00 OD 44,450 mm Thk(Avg) 1,651 mm Length 6,096 m Pitch 59,267 mm Tube pattern 30
Tube Type Plain Material NI-FE-CR alloy 800 & 800H (N088 Pairs seal strips 1
Shell ID 914,40 mm Kettle ID mm Passlane Seal Rod No. 3
Cross Baffle Type Perpend. Single-Seg. %Cut (Diam) 25 Impingement Plate None
Spacing(c/c) 1093,6 mm Inlet 1273,4 mm No. of Crosspasses 5
Rho-V2-Inlet Nozzle 485,04 kg/m-s2 Shell Entrance 740,39 kg/m-s2 Shell Exit 759,40 kg/m-s2
Bundle Entrance 425,54 kg/m-s2 Bundle Exit 539,90 kg/m-s2
Weight/Shell 26195 kg Filled with Water 32074 kg Bundle 8505,8 kg
Notes: Thermal Resistance, % Velocities; m/s Flow Fractions
Shell 55,57 Shellside 31,32 A 0,017
Tube 27,61 Tubeside 80,81 B 0,402
Fouling 15,13 Crossflow 33,33 C 0,476
Metal 1,69 Window 112,13 E 0,029
F 0,076

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri
 HEAT EXCHANGER SPECIFICATION SHEET Page 14
SI Units

Job No.
Customer E-103 Reference No.
Address Proposal No.
Plant Location Date 26/8/2021 Rev
Service of Unit Item No.
Size 914,4 x 6096 mm Type AES Horizontal Connected In 2 Parallel 1 Series
Surf/Unit (Gross/Eff) 197,49 / 184,64 m2 Shell/Unit 2 Surf/Shell (Gross/Eff) 98,747 / 92,318 m2
PERFORMANCE OF ONE UNIT
Fluid Allocation Shell Side Tube Side
Fluid Name AGUA + ORGÁNICOS GASEOSO AGUA GASEOSA
Fluid Quantity, Total kg/hr 54900 34596
Vapor (In/Out) 54900 54900 34596 34596
Liquid
Steam
Water
Noncondensables
Temperature (In/Out) C 537,10 557,81 593,82 558,70
Specific Gravity
Viscosity mN-s/m2 0,0242 0,0250 0,0323 0,0309
Molecular Weight, Vapor
Molecular Weight, Noncondensables
Specific Heat kJ/kg-C 2,3627 2,3840 2,2314 2,2108
Thermal Conductivity W/m-C 0,0716 0,0738 0,0806 0,0759
Latent Heat kJ/kg
Inlet Pressure kPa 170,00 633,38
Velocity m/s 31,32 80,81
Pressure Drop, Allow/Calc kPa 85,000 20,182 540,00 202,61
Fouling Resistance (min) m2-K/W 0,000352 0,000352
Heat Exchanged 749991 W MTD (Corrected) 22,8 C
Transfer Rate, Service 177,93 W/m2-K Clean 243,48 W/m2-K Actual 206,64 W/m2-K
CONSTRUCTION OF ONE SHELL Sketch (Bundle/Nozzle Orientation)
Shell Side Tube Side
Design/Test Pressure kPaG 517,11 / 1103,2 /
Design Temperature C 682,22 782,22
No Passes per Shell 1 6
Corrosion Allowance mm 3,000 3,000
Connections In mm 1 @ 742,95 1 @ 307,09
Size & Out mm 1 @ 742,95 1 @ 307,09
Rating Intermediate @ @
Tube No. 116 OD 44,450 mm Thk(Avg) 1,651 mm Length 6,096 m Pitch 59,267 mm
Tube Type Plain Material NI-FE-CR alloy 800 & 800H (N08800 & H088 Tube pattern30
Shell NI-FE-CR alloy 800 & 800H (N0 ID 914,40 OD 936,63 mm Shell Cover NI-FE-CR alloy 800 & 800H (Remove.)
Channel or Bonnet NI-FE-CR alloy 800 & 800H (N08800 & H08810) Channel Cover NI-FE-CR alloy 800 & 800H (N08800 &
Tubesheet-Stationary NI-FE-CR alloy 800 & 800H (N08800 & H08810) Tubesheet-Floating NI-FE-CR alloy 800 & 800H (N088
Floating Head Cover NI-FE-CR alloy 800 & 800H (N08800 & H08810) Impingement Plate None
Baffles-Cross NI-FE-CR alloy 800 & 80 Type Single-Seg. %Cut (Diam) 25 Spacing(c/c) 1093,6 Inlet 1273,4 mm
Baffles-Long Seal Type None
Supports-Tube U-Bend Type None
Bypass Seal Arrangement 1 pairs seal strips Tube-Tubesheet Joint Expanded (No groove)
Expansion Joint Type
Rho-V2-Inlet Nozzle 485,04 kg/m-s2 Bundle Entrance 425,54 Bundle Exit 539,90 kg/m-s2
Gaskets-Shell Side Ring Joint (Ni Alloy) Tube Side Ring Joint (Ni Alloy)
- Floating Head Ring Joint (Ni Alloy)
Code Requirements ASME TEMA Class R
Weight/Shell 26195 kg Filled with Water 32074 kg Bundle 8505,8 kg
Remarks:

Reprinted with Permission (v7,3.2)

C:\Users\EduRo\OneDrive\Escritorio\intercambiadores\E-103.htri