HEAT EXCHANGER SPECIFICATION SHEET
Customer
Address
Plant Location
Service of Unit
Size
438.151 x 1828.94 mm
Surf/Unit (Gross/Eff) 21.89 / 19.77 m2
Page 1
SI Units
Job No.
Reference No.
Proposal No.
Date
2/3/2021
Rev
Item No.
Type AEW
Horz.
Connected In
1 Parallel
1 Series
Shell/Unit
1
Surf/Shell (Gross/Eff) 21.89 / 19.77 m2
PERFORMANCE OF ONE UNIT
Shell Side
Tube Side
Fluid Allocation
Fluid Name
Water
Fluid Quantity, Total
kg/hr
7200.04
1961830
Vapor (In/Out)
Liquid
7200.04
1961830
1961830
7200.04
Steam
Water
7200.04
7200.04
1961830
1961830
Noncondensables
Temperature (In/Out)
C
360.23
295.24
287.24
287.57
Specific Gravity
0.5267
0.7419
0.7566
0.7560
Viscosity
mN-s/m2
0.0602
0.0914
0.0945
0.0944
Molecular Weight, Vapor
Molecular Weight, Noncondensables
Specific Heat
kJ/kg-C
15.075
5.2590
5.1202
5.1254
Thermal Conductivity
W/m-C
0.4115
0.5742
0.5871
0.5866
Latent Heat
kJ/kg
Inlet Pressure
kPa
18720.3
18720.3
Velocity
m/s
7.794e-2
16.73
Pressure Drop, Allow/Calc kPa
18720.3
2.232
18720.3
373.108
Fouling Resistance (min)
m2-K/W
0.000125
0.000125
Heat Exchanged W
MTD (Corrected)
31.7 C
957767
Transfer Rate, Service
1528.14 W/m2-K
Clean
2672.29 W/m2-K
1555.19 W/m2-K
Actual
CONSTRUCTION OF ONE SHELL
Sketch (Bundle/Nozzle Orientation)
Shell Side
Tube Side
Design/Test Pressure
kPaG
18618.9 /
18618.9 /
Design Temperature
C
360.23
360.23
No Passes per Shell
1
1
Corrosion Allowance
mm
Connections
In
mm
1 @ 52.553
1 @ 394.336
Size &
Out
mm
1 @ 52.553
1 @ 394.336
Rating
Intermediate
@
@
Tube No.
Thk(Avg) 1.245 mm
Length 1.829 m
Pitch 23.812 mm
Layout 45
200 OD 19.050 mm
Tube Type
Plain
Material CARBON STEEL
Shell
ID 438.151 mm
OD
mm
Shell Cover
Channel or Bonnet
Channel Cover
Tubesheet-Stationary
Tubesheet-Floating
Floating Head Cover
Impingement Plate
Circular plate
Baffles-Cross
Type SINGLE-SEG.
%Cut (Diam) 25.00
Spacing(c/c) 175.000
Inlet 213.297 mm
Baffles-Long
Seal Type
Supports-Tube
U-Bend
Type
Bypass Seal Arrangement
Tube-Tubesheet Joint
Expansion Joint
Type
Rho-V2-Inlet Nozzle
1614.76 kg/m-s2
Bundle Entrance 31.57
Bundle Exit
47.42
kg/m-s2
Gaskets-Shell Side
Tube Side
-Floating Head
Code Requirements
TEMA Class
Weight/Shell 1762.28
Filled with Water 2261.22
Bundle 362.67
kg
Remarks:
438.15
mm
1.829
m
Reprinted with Permission (v6 )
D:\data te a\Data FIX HTRI\Heat Exchanger 1 bahan carbon steel.htri