Output Summary
Page 1
Released to the following HTRI Member Company:
TEMA INDIA
MKH Units
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
70N-SOR : Summary Unit
Rating - Horizontal
1 No Data Check Messages.
2 No Runtime Messages.
3
Process Conditions
4 Fluid name
5 Total flow rate
6 Inlet/Outlet Y
7 Inlet/Outlet T
8 Inlet P/Avg
9 dP/Allow.
10 Fouling
Cold Shellside
0.0889
232.00
162.63
1.459
HDF RX Effluent
36.403
0.0752
129.00
161.90
2.100
0.000300
Exchanger Performance
12 Shell h
13 Tube h
14 Hot regime
15 Cold regime
16 EMTD
17
(kcal/m2-hr-C)
(kcal/m2-hr-C)
(--)
(--)
(Deg C)
736.86
1955.7
37.7
Actual U
Required U
Total duty
Eff. area
Overdesign
(kcal/m2-hr-C)
(kcal/m2-hr-C)
(MM kcal/hr)
(m2)
(%)
Shell Geometry
18 TEMA type
19 Shell ID
20 Series
21 Parallel
22 Orientation
23
DFU
710.00
2
1
0.00
(--)
(mm)
(--)
(--)
(deg)
Baffle type
Baffle cut
Baffle orientation
Central spacing
Crosspasses
32 Shell
33 Tube
34 Fouling
35 Metal
36
(Pct Dia.)
(--)
(mm)
(--)
27.23
Parallel
198.00
27
Nozzles
(--)
(mm)
(mm)
(--)
(deg)
(--)
(--)
Thermal Resistance, %
281.28
269.73
2.9900
293.94
4.28
Baffle Geometry
Tube Geometry
24 Tube type
25 Tube OD
26 Length
27 Pitch ratio
28 Layout
29 Tubecount
30 Tube Pass
31
CHPS Liquid
33.906
0.0023
0.0076
60.00
210.00
14.233
1.131
2.100
0.000400
(1000-kg/hr)
(Wt. frac vap.)
(Deg C)
(kgf/cm2A)
(kgf/cm2)
(m2-hr-C/kcal)
11
Hot Tubeside
Plain
19.050
6086.
1.3333
45
418
2
Shell inlet
Shell outlet
Inlet height
Outlet height
Tube inlet
Tube outlet
(mm)
(mm)
(mm)
(mm)
(mm)
(mm)
Velocities, m/s
38.24
28.48 Tubeside
27.65 Crossflow
5.63 Longitudinal
Min
4.67
0.28
0.23
131.78
54.980
91.849
131.78
131.78
Flow Fractions
Max
5.64
1.10
0.44
A
B
C
E
F
0.226
0.555
0.055
0.164
0.000
Series Summary
Page 2
Released to the following HTRI Member Company:
TEMA INDIA
MKH Units
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Shell #
1
2
2 Unit
Shell 1
Shell 2
3 Performance
4 Overdesign
5 Overall U
6 Required U
7 Unit Duty
8 Shellside h
9 Tubeside h
10 Shellside delta P
11 Tubeside delta P
12 EMTD
(%)
(kcal/m2-hr-C)
(kcal/m2-hr-C)
(MM kcal/hr)
(kcal/m2-hr-C)
(kcal/m2-hr-C)
(kgf/cm2)
(kgf/cm2)
(C)
3.81
305.34
294.14
1.2080
816.88
2291.7
0.566
0.725
27.9
4.85
257.22
245.31
1.7820
660.10
1665.8
0.566
0.734
49.4
154.02
210.00
232.00
191.93
0.0049
0.0076
0.0889
0.0823
60.00
154.02
191.93
129.00
0.0023
0.0049
0.0823
0.0752
F
1
146.97
Horizontal
710.00
Cold
Single-Seg.
27.23
Parallel
198.00
27
Plain
2
418
6086.
19.050
45
1.3333
F
1
146.97
Horizontal
710.00
Cold
Single-Seg.
27.23
Parallel
198.00
27
Plain
2
418
6086.
19.050
45
1.3333
13 Process Conditions
14 Inlet T, Shell
15 Outlet T, Shell
16 Inlet T, Tube
17 Outlet T, Tube
18 Inlet Y, Shell
19 Outlet Y, Shell
20 Inlet Y, Tube
21 Outlet Y, Tube
(C)
(C)
(C)
(C)
(Wt. fraction)
(Wt. fraction)
(Wt. fraction)
(Wt. fraction)
22 Geometry
(--)
23 Shell type
(--)
24 Parallel
(m2)
25 Effective area
26 Shell orientation (--)
(mm)
27 Shell ID
(--)
28 Shellside fluid
(--)
29 Baffle type
(Pct Dia.)
30 Baffle cut
31 Baffle orientation (--)
32 Central spacing (mm)
(--)
33 Crosspasses
(--)
34 Tube type
(--)
35 Tube Pass
(--)
36 Tubecount
(mm)
37 Tube length
(mm)
38 Tube OD
39 Tube layout angle (--)
(--)
40 Pitch ratio
HEAT EXCHANGER RATING DATA SHEET
Page 10
1
Released to the following HTRI Member Company:
2
MKH Units
TEMA INDIA
3
4
5 Service of Unit Reactor Effluent / CHPS Liquid Exchanger
Item No. 1837-E-003A-B
6 Type
DFU
Orientation Horizontal
Connected In
1 Parallel
2 Series
7 Surf/Unit (Gross/Eff)
304.50 / 293.94 m2
Shell/Unit 2
Surf/Shell (Gross/Eff)
152.25 / 146.97 m2
8
PERFORMANCE OF ONE UNIT
9 Fluid Allocation
Shell Side
Tube Side
10 Fluid Name
CHPS Liquid
HDF RX Effluent
11 Fluid Quantity, Total
1000-kg/hr
33.906
36.403
12 Vapor (In/Out)
wt%
0.23
0.76
8.89
7.52
13 Liquid
wt%
99.77
99.24
91.11
92.48
14 Temperature (In/Out)
C
60.00
210.00
232.00
129.00
kg/m3
15 Density
2.6400 V/L 803.20 4.8526 V/L 715.69 12.180 V/L 697.50 12.716 V/L 771.40
cP
16 Viscosity
0.0110 V/L 5.5770 0.0170 V/L 0.6560 0.0140 V/L 0.6550 0.0120 V/L 1.8883
kcal/kg-C
17 Specific Heat
1.4710 V/L 0.5060 0.8669 V/L 0.6530 2.2460 V/L 0.7090 2.5320 V/L 0.6010
kcal/hr-m-C
18 Thermal Conductivity
0.0830 V/L 0.0840 0.0821 V/L 0.0680 0.2460 V/L 0.1010 0.2090 V/L 0.1180
kgf/cm2A
19 Critical Pressure
kgf/cm2A
20 Inlet Pressure
14.233
162.63
m/s
21 Velocity
0.86
5.23
kgf/cm2
22 Pressure Drop, Allow/Calc
2.100
1.131
2.100
1.459
kcal/m2-hr-C
23 Average Film Coefficient
736.86
1955.7
m2-hr-C/kcal
24 Fouling Resistance (min)
0.000400
0.000300
2.9900 MM kcal/hr
25 Heat Exchanged
MTD (Corrected)
37.7 C
Overdesign
4.28 %
269.73 kcal/m2-hr-C
26 Transfer Rate, Service
Calculated
281.28 kcal/m2-hr-C Clean
391.40 kcal/m2-hr-C
27
CONSTRUCTION OF ONE SHELL
Sketch (Bundle/Nozzle Orientation)
28
Shell Side
Tube Side
29 Design Pressure
kgf/cm2G
130.50
169.60
30 Design Temperature
C
289.00
343.00
31 No Passes per Shell
2
2
32 Flow Direction
Upward
Downward
Connections
33
In
mm
1
@
1
@ 131.78
Size &
34
Out
mm
1
@ 131.78
1
@ 131.78
Rating
35
Liq. Out mm
@
1
@
OD 19.050 mm
36 Tube No. 418.00
Thk(Avg) 4.684
mm
Length 6086. mm Pitch 25.400 mm
Tube pattern 45
Pairs seal strips
37 Tube Type Plain
Material SA-213 T22
3
Passlane Seal Rod No.
38 Shell ID
710.00 mm
Kettle ID
mm
0
Impingement Plate
39 Cross Baffle Type
Parallel
%Cut (Diam) 27.23
Rods
No. of Crosspasses
40 Spacing(c/c)
198.00 mm
Inlet
727.00 mm
27
Shell Exit
41 Rho-V2-Inlet Nozzle
kg/m-s2
Shell Entrance
kg/m-s2
kg/m-s2
Bundle Exit
42
Bundle Entrance
kg/m-s2
kg/m-s2
43 Weight/Shell
kg
Filled with Water
kg
Bundle
kg
44 Notes:
Thermal Resistance, %
Velocities, m/s
Flow Fractions
45
Shell
38.24 Shellside
0.86 A
0.226
46
Tube
28.48 Tubeside
5.23 B
0.555
47
Fouling
27.65 Crossflow
0.89 C
0.055
48
Metal
5.63 Window
0.81 E
0.164
0.000
F
49
HEAT EXCHANGER SPECIFICATION SHEET
Page 11
1
Released to the following HTRI Member Company:
MKH Units
2
TEMA INDIA
3
Job No.
4
Gujarat Refinery, IOCL
Reference No.
5 Customer
Vadodara, Gujarat
Proposal No.
6 Address
Lupech Project
Date
7/21/2023
Rev
7 Plant Location
Reactor Effluent / CHPS Liquid Exchanger
Item No.
1837-E-003A-B
8 Service of Unit
710 x 6086
mm
Type
DFU
Horizontal
Connected In
1
Parallel
2 Series
9 Size
304.5 / 293.94 m2
Shell/Unit
2
Surf/Shell (Gross/Eff)
152.25 / 146.97 m2
10 Surf/Unit (Gross/Eff)
PERFORMANCE OF ONE UNIT
11
Shell Side
Tube Side
12 Fluid Allocation
CHPS Liquid
HDF RX Effluent
13 Fluid Name
kg/hr
33906
36403
14 Fluid Quantity, Total
77.306
258.41
3236.2
2737.2
15 Vapor (In/Out)
33829
33648
33167
33666
16 Liquid
17 Steam
18 Water
19 Noncondensables
C
60.00
210.00
232.00
129.00
20 Temperature (In/Out)
0.8036
0.7160
0.6978
0.7718
21 Specific Gravity
cP
0.0110 V/L 5.5770 0.0170 V/L 0.6560 0.0140 V/L 0.6550 0.0120 V/L 1.8883
22 Viscosity
23 Molecular Weight
24 Molecular Weight, Noncondensables
kcal/kg-C
1.4710 V/L 0.5060
0.8669 V/L 0.6530 2.2460 V/L 0.7090 2.5320 V/L 0.6010
25 Specific Heat
kcal/hr-m-C
0.0830 V/L 0.0840
0.0821 V/L 0.0680 0.2460 V/L 0.1010 0.2090 V/L 0.1180
26 Thermal Conductivity
kcal/kg
611.11
611.11
265.30
593.29
27 Latent Heat
kgf/cm2A
14.233
162.63
28 Inlet Pressure
m/s
0.86
5.23
29 Velocity
kgf/cm2
2.100
1.131
2.100
1.459
30 Pressure Drop, Allow/Calc
m2-hr-C/kcal
0.000400
0.000300
31 Fouling Resistance (min)
2990000 kcal/hr
MTD (Corrected)
37.7
C
32 Heat Exchanged
269.73 kcal/m2-hr-C
Clean 391.40 kcal/m2-hr-C
Actual
281.28 kcal/m2-hr-C
33 Transfer Rate, Service
CONSTRUCTION OF ONE SHELL
Sketch (Bundle/Nozzle Orientation)
34
Shell Side
Tube Side
35
kgf/cm2G
130.50 /
169.60 /
36 Design/Test Pressure
C
289.00
343.00
37 Design Temperature
2
2
38 No Passes per Shell
mm
4.500
4.500
39 Corrosion Allowance
Connections
In
mm
1 @
1 @ 131.78
40
Size &
Out
mm
1 @ 131.78
1 @ 131.78
41
Rating
Intermediate
@
@
42
OD 19.050 mm
Thk(Avg) 4.684 mm
Length 6086.
mm
Pitch 25.400 mm
43 Tube No. 209U
Material SA-213 T22
Tube pattern45
44 Tube Type Plain
SA-387 GR 22 CL 2
ID 710.00 OD 792.55 mm Shell Cover
SA-387 GR 22 CL 2
(Integ.)
45 Shell
SA-336 F22 CL 3
Channel Cover SA-336 F22 CL 3
46 Channel or Bonnet
SA-336 F22 CL 3
Tubesheet-Floating
47 Tubesheet-Stationary
Impingement Plate Rods
48 Floating Head Cover
SA-387 GR 22 CL 2
Type
%Cut (Diam) 27.23 Spacing(c/c) 198.00
Inlet 727.00 mm
49 Baffles-Cross
Seal Type Lamiflex
50 Baffles-Long
U-Bend
Type Full support
51 Supports-Tube
3
pairs seal strips
Tube-Tubesheet Joint Expanded and strength welded
52 Bypass Seal Arrangement
Type
53 Expansion Joint
kg/m-s2
Bundle Entrance
Bundle Exit
kg/m-s2
54 Rho-V2-Inlet Nozzle
Tube Side
Mach. Mtl. (Kammprofile\Flex. Face)
55 Gaskets-Shell Side Mach. Mtl. (Kammprofile\Flex. Face)
- Floating Head
56
TEMA Class
57 Code Requirements ASME
kg
Filled with Water
kg
Bundle
kg
58 Weight/Shell
59 Remarks:
60
61
62
Reprinted with Permission
63
Input Reprint
Page 13
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Exchanger Data
2 Unit identifier
3 Service type
4 TEMA type
5 Run mode
6 Hot fluid location
7 Unit orientation
8 Number of shells in series
9 Number of shells in parallel
10 Multiple service configuration
11 Minimize piping between series shells
12 Flow in 1st tubepass
13 Train flow direction
14
15 Construction Data
16 Shell material
17 Tube material
18 Shell cover material
19 Channel or bonnet material
20 Tubesheet-Stationary material
21 Baffle-Cross material
22 Shellside gasket
23 Tubeside gasket
24 Shellside design pressure
25 Tubeside design pressure
26 Shellside vacuum pressure
27 Tubeside vacuum pressure
28 Shellside design temperature
29 Tubeside design temperature
30 Shellside corrosion allowance
31 Tubeside corrosion allowance
32 Tubesheet design temperature
33 Shellside radiography
34 Tubeside radiography
35 TEMA class
36 Small exchanger
37 Shell outside diameter
38 Shell inside diameter
39 Shell wall thickness
40 Front head outside diameter
41 Front head inside diameter
42 Front head thickness
43 Rear head outside diameter
44 Rear head inside diameter
45 Rear head thickness
46 Total tubesheet thickness
47 Double tubesheet
48 Shell expansion joint
49 Suppress mechanical calculations
50
Summary Unit
Generic shell and tube
DFU
Rating
Tubeside
Horizontal
2
1
Hot and Cold in Series
No
Countercurrent
Countercurrent
SA-387 GR 22 CL 2
SA-213 T22
SA-387 GR 22 CL 2
SA-336 F22 CL 3
SA-336 F22 CL 3
SA-387 GR 22 CL 2
Mach. Mtl. (Kammprofile\Flex. Face)
Mach. Mtl. (Kammprofile\Flex. Face)
130.50 kgf/cm2G
169.60 kgf/cm2G
Full
Full
289.00 C
343.00 C
4.500 mm
4.500 mm
343.00 C
Full
Full
R
No
792.55 mm
710.00 mm
41.275 mm
811.60 mm
710.00 mm
50.800 mm
805.25 mm
710.00 mm
47.625 mm
171.00 mm
No
No
No
Input Reprint
Page 14
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Tube Data
2 Tube type
3 Tube outside diameter
4 Tube wall thickness
5 Tube pitch
6 Tube pitch ratio
7 Tubepasses per shell
8 Tube pattern
9 Number of tubes per shell
10 Tube count method
11 Tube length
12 Tube material
13
14 Baffle Data
15 Baffle type
16 Baffle orientation
17 Baffle cut percent
18 Adjust baffle cut
19 Double segmental set center baffle at inlet
20 Number of crosspasses
21 Central baffle spacing
22 Inlet/outlet spacing
23 Variable baffle spacing
24 Window cut from baffles
25 Use deresonating baffles
26
27 Supports Data
28 Full support at U-Bend
29 Support distance to U-bend tangent
30 Number of U-bend supports
31 Include inlet vibration support
32 Include outlet vibration support
33
34 Longitudinal Baffle Data
35 Insulated longitudinal baffle
36 Seal type
37
38
39
40
41
42
43
44
45
46
47
48
49
50
Plain
19.050 mm
4.684 mm
25.400 mm
1.333
2
45 degrees
418.00
Rigorous
6086. mm
SA-213 T22
Single segmental
Parallel
27.230 % shell ID
No adjustment
Program set
27
198.00 mm
727.00 mm
No
No
No
Full support
40.000 mm
2
No
No
No
Lamiflex
Input Reprint
Page 15
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Nozzle Data
2 Shellside
3 Nozzle standard
4 Shell entrance type
5 Shell exit type
6
7 Nozzle outside diameter
8 Nozzle schedule
9 Nozzle inside diameter
10 Number at this position
11 Tubeside
12 Nozzle standard
13
14 Nozzle outside diameter
15 Nozzle schedule
16 Nozzle inside diameter
17 Number at this position
18
19 Nozzle Location Data
20 Radial position on shell inlet nozzle
21 Radial position on shell outlet nozzle
22 Location of nozzle at U-bend
23 Tubeside entry type
24 Tubeside inlet position
25 Tubeside exit type
26
27 Impingement Data
28 Impingement type
29 Use tube positions to place rods
30 Impingement rod rows
31 Impingement rod diameter
32 Impingement rod pitch
33 Impingement rods on centerline
34 Impingement rod layout angle
35 Rod row width to nozzle diameter
36
37 Tube Layout Data
38 Pass partition construction
39 Force symmetric layout
40 Force continuous cleaning lanes
41 Force uniform layout
42 Align across primary passlanes
43 Fill knock out area with dummy tubes
44 Fill bundle periphery with dummy tubes
45 Fill passlanes with dummy tubes
46 Shifted staggered layout
47 Use crossed U-bends
48 Minimum U-bend diameter
49 Use tube layout drawing as input
50
01-ANSI_B36_10.TABLE
Use impingement device
Remove tubes if TEMA requires
Inlet
Outlet Liq. Outlet
114.30
168.28
-- mm
STD
STD
-101.60
131.78
-- mm
1
1
--
Inlet
168.28
STD
131.78
1
01-ANSI_B36_10.TABLE
Outlet Liq. Outlet
168.28
-- mm
STD
-131.78
-- mm
1
--
Program decides
Program decides
After U-bend
Radial
Front head
Same as inlet
Rods
No
2
20.000 mm
25.400 mm
Yes
45.00 deg
2.3180
Program set
Yes
No
No
No
Program set
Program set
Program Set
Program set
No
76.200 mm
No
Input Reprint
Page 16
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Clearance Data
2 Number of seal strip pairs
3 Block A stream
4 Block E stream
5 Block F stream
6 Number of passlane seal rods
7 Tubes to remove for tie rods
8 Number of tie rods
9 Tie rod outside diameter
10 Tube to baffle clearance
11 Baffle to shell clearance
12 Bundle to shell clearance
13 Baffle clearance type
14
15 Process Conditions Data
16 Phase condition
17 Flow rate
18 Inlet temperature
19 Outlet temperature
20 Inlet pressure
21 Allowable pressure drop
22 Exchanger duty
23 Duty multiplier
24
25 Process Fouling Data
26 Fouling resistance
27
28 Hot Fluid Property Data
29 Fluid name
30 Physical property method
31 Temperature interpolation option
32 Flash type
33 Quantity units
34 Heat release type
35 Hot Fluid Physical Property Data
36 Pressure Set, 162.63 kgf/cm2A
37
Vapor
38
Mass
39
Temp.
Enthalpy Fraction
40
C
kcal/kg
41
232.00
167.60
0.0889
42
227.00
163.00
0.0874
43
221.00
158.50
0.0865
44
216.00
153.90
0.0857
45
210.00
149.40
0.0849
46
205.00
145.00
0.0841
47
200.00
140.50
0.0833
48
194.00
136.10
0.0826
49
189.00
131.70
0.0819
50
3
No
No
No
Calculated
1
12
12.700 mm
0.800 mm
4.800 mm
20.190 mm
TEMA
Hot Fluid
Two phase
36.403
232.00
129.00
162.63
2.100
Cold Fluid
Two phase
33.906 1000-kg/hr
60.00 C
210.00 C
14.233 kgf/cm2A
2.100 kgf/cm2
2.9900 MM kcal/hr
1.0000
Hot Fluid
0.0003
Cold Fluid
0.0004 m2-hr-C/kcal
HDF RX Effluent
Property tables
Program
Integral
Moles
Specific enthalpy
Vapor
Density
kg/m3
12.180
12.170
12.170
12.170
12.180
12.190
12.210
12.230
12.260
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0140
0.2460
0.0140
0.2440
0.0140
0.2420
0.0140
0.2400
0.0140
0.2380
0.0140
0.2370
0.0140
0.2350
0.0140
0.2330
0.0130
0.2310
Vapor
Heat
Capacity
kcal/kg-C
2.2460
2.2630
2.2790
2.2950
2.3120
2.3270
2.3420
2.3570
2.3720
Liquid
Density
kg/m3
697.50
701.90
706.20
710.40
714.60
718.70
722.80
726.80
730.80
Liquid
Dynamic
Viscosity
cP
0.6550
0.6850
0.7170
0.7510
0.7870
0.8260
0.8680
0.9120
0.9610
Input Reprint
Page 17
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Hot Fluid Physical Property Data
2 Pressure Set, 162.63 kgf/cm2A
3
Vapor
4
Mass
5
Temp.
Enthalpy Fraction
6
C
kcal/kg
7
183.00
127.40
0.0812
8
178.00
123.00
0.0805
9
173.00
118.70
0.0798
10
167.00
114.50
0.0792
11
162.00
110.20
0.0786
12
156.00
106.00
0.0780
13
151.00
101.80
0.0774
14
146.00
97.700
0.0768
15
140.00
93.600
0.0762
16
135.00
89.500
0.0757
17
129.00
85.400
0.0751
18
19 Pressure Set, 162.63 kgf/cm2A
20
Liquid
Liquid
21
Thermal
Heat
22
Temp.
Cond.
Capacity
23
C
kcal/hr-m-C kcal/kg-C
24
232.00
0.1010
0.7090
25
227.00
0.1020
0.7030
26
221.00
0.1030
0.6980
27
216.00
0.1040
0.6920
28
210.00
0.1050
0.6860
29
205.00
0.1060
0.6810
30
200.00
0.1070
0.6750
31
194.00
0.1080
0.6690
32
189.00
0.1090
0.6630
33
183.00
0.1100
0.6580
34
178.00
0.1110
0.6520
35
173.00
0.1120
0.6460
36
167.00
0.1120
0.6410
37
162.00
0.1130
0.6350
38
156.00
0.1140
0.6290
39
151.00
0.1150
0.6240
40
146.00
0.1160
0.6180
41
140.00
0.1170
0.6120
42
135.00
0.1170
0.6060
43
129.00
0.1180
0.6010
44
45
46
47
48
49
50
Vapor
Density
kg/m3
12.290
12.330
12.370
12.410
12.460
12.510
12.560
12.620
12.680
12.740
12.810
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0130
0.2290
0.0130
0.2270
0.0130
0.2250
0.0130
0.2230
0.0130
0.2210
0.0130
0.2190
0.0130
0.2170
0.0130
0.2150
0.0130
0.2130
0.0120
0.2110
0.0120
0.2090
Liquid
Surface
Tension
dyne/cm
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
Liquid
Critical
Pressure
kgf/cm2A
12.733
12.733
12.833
12.833
12.833
12.933
12.933
12.933
13.033
13.033
13.033
13.133
13.133
13.233
13.233
13.333
13.333
13.433
13.433
13.533
Vapor
Heat
Capacity
kcal/kg-C
2.3870
2.4020
2.4170
2.4320
2.4460
2.4610
2.4750
2.4890
2.5040
2.5190
2.5330
Liquid
Density
kg/m3
734.70
738.60
742.40
746.20
749.90
753.60
757.20
760.80
764.40
767.90
771.30
Liquid
Dynamic
Viscosity
cP
1.0130
1.0690
1.1310
1.1980
1.2700
1.3500
1.4370
1.5330
1.6390
1.7580
1.8910
Input Reprint
Page 18
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Hot Fluid Physical Property Data
2 Pressure Set, 161.23 kgf/cm2A
3
Vapor
4
Mass
5
Temp.
Enthalpy Fraction
6
C
kcal/kg
7
232.00
167.60
0.0885
8
227.00
163.00
0.0875
9
221.00
158.50
0.0866
10
216.00
153.90
0.0858
11
210.00
149.40
0.0849
12
205.00
145.00
0.0841
13
200.00
140.50
0.0834
14
194.00
136.10
0.0826
15
189.00
131.70
0.0819
16
183.00
127.40
0.0812
17
178.00
123.00
0.0805
18
173.00
118.70
0.0799
19
167.00
114.50
0.0793
20
162.00
110.20
0.0786
21
156.00
106.00
0.0780
22
151.00
101.80
0.0774
23
146.00
97.700
0.0769
24
140.00
93.500
0.0763
25
135.00
89.400
0.0757
26
129.00
85.400
0.0752
27
28 Pressure Set, 161.23 kgf/cm2A
29
Liquid
Liquid
30
Thermal
Heat
31
Temp.
Cond.
Capacity
32
C
kcal/hr-m-C kcal/kg-C
33
232.00
0.1010
0.7090
34
227.00
0.1020
0.7030
35
221.00
0.1030
0.6980
36
216.00
0.1040
0.6920
37
210.00
0.1050
0.6860
38
205.00
0.1060
0.6810
39
200.00
0.1070
0.6750
40
194.00
0.1080
0.6690
41
189.00
0.1090
0.6630
42
183.00
0.1100
0.6580
43
178.00
0.1110
0.6520
44
173.00
0.1120
0.6460
45
167.00
0.1120
0.6410
46
162.00
0.1130
0.6350
47
156.00
0.1140
0.6290
48
151.00
0.1150
0.6240
49
146.00
0.1160
0.6180
50
Vapor
Density
kg/m3
12.090
12.080
12.080
12.080
12.090
12.110
12.120
12.150
12.170
12.200
12.240
12.280
12.320
12.370
12.420
12.470
12.530
12.590
12.650
12.720
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0140
0.2460
0.0140
0.2440
0.0140
0.2420
0.0140
0.2400
0.0140
0.2380
0.0140
0.2370
0.0140
0.2350
0.0130
0.2330
0.0130
0.2310
0.0130
0.2290
0.0130
0.2270
0.0130
0.2250
0.0130
0.2230
0.0130
0.2210
0.0130
0.2190
0.0130
0.2170
0.0130
0.2150
0.0130
0.2130
0.0120
0.2110
0.0120
0.2090
Liquid
Surface
Tension
dyne/cm
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
Liquid
Critical
Pressure
kgf/cm2A
12.733
12.733
12.833
12.833
12.833
12.933
12.933
12.933
13.033
13.033
13.033
13.133
13.133
13.233
13.233
13.333
13.333
Vapor
Heat
Capacity
kcal/kg-C
2.2440
2.2620
2.2780
2.2940
2.3100
2.3260
2.3410
2.3560
2.3720
2.3860
2.4010
2.4160
2.4300
2.4450
2.4600
2.4740
2.4880
2.5030
2.5180
2.5320
Liquid
Density
kg/m3
697.80
702.10
706.40
710.70
714.80
718.90
723.00
727.00
731.00
734.90
738.70
742.50
746.30
750.00
753.70
757.30
760.90
764.40
767.90
771.40
Liquid
Dynamic
Viscosity
cP
0.6540
0.6840
0.7160
0.7500
0.7860
0.8250
0.8660
0.9110
0.9590
1.0110
1.0680
1.1290
1.1960
1.2680
1.3470
1.4340
1.5300
1.6370
1.7550
1.8880
Input Reprint
Page 19
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Hot Fluid Physical Property Data
2 Pressure Set, 161.23 kgf/cm2A
3
Liquid
Liquid
4
Thermal
Heat
5
Temp.
Cond.
Capacity
6
C
kcal/hr-m-C kcal/kg-C
7
140.00
0.1170
0.6120
8
135.00
0.1170
0.6060
9
129.00
0.1180
0.6010
10
11 Pressure Set, 159.93 kgf/cm2A
12
Vapor
13
Mass
14
Temp.
Enthalpy Fraction
15
C
kcal/kg
16
232.00
167.60
0.0886
17
227.00
163.00
0.0876
18
221.00
158.40
0.0867
19
216.00
153.90
0.0858
20
210.00
149.40
0.0850
21
205.00
144.90
0.0842
22
200.00
140.50
0.0834
23
194.00
136.10
0.0827
24
189.00
131.70
0.0820
25
183.00
127.30
0.0813
26
178.00
123.00
0.0806
27
173.00
118.70
0.0799
28
167.00
114.50
0.0793
29
162.00
110.20
0.0787
30
156.00
106.00
0.0781
31
151.00
101.80
0.0775
32
146.00
97.700
0.0769
33
140.00
93.500
0.0763
34
135.00
89.400
0.0758
35
129.00
85.400
0.0752
36
37 Pressure Set, 159.93 kgf/cm2A
38
Liquid
Liquid
39
Thermal
Heat
40
Temp.
Cond.
Capacity
41
C
kcal/hr-m-C kcal/kg-C
42
232.00
0.1010
0.7090
43
227.00
0.1020
0.7030
44
221.00
0.1030
0.6980
45
216.00
0.1040
0.6920
46
210.00
0.1050
0.6860
47
205.00
0.1060
0.6800
48
200.00
0.1070
0.6750
49
194.00
0.1080
0.6690
50
Liquid
Surface
Tension
dyne/cm
13.000
13.000
13.000
Liquid
Critical
Pressure
kgf/cm2A
13.433
13.433
13.533
Vapor
Density
kg/m3
12.010
12.000
11.990
12.000
12.010
12.020
12.040
12.060
12.090
12.120
12.150
12.190
12.230
12.280
12.320
12.380
12.430
12.490
12.560
12.620
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0140
0.2460
0.0140
0.2440
0.0140
0.2420
0.0140
0.2400
0.0140
0.2380
0.0140
0.2360
0.0140
0.2350
0.0130
0.2330
0.0130
0.2310
0.0130
0.2290
0.0130
0.2270
0.0130
0.2250
0.0130
0.2230
0.0130
0.2210
0.0130
0.2190
0.0130
0.2170
0.0130
0.2150
0.0130
0.2130
0.0120
0.2110
0.0120
0.2090
Liquid
Surface
Tension
dyne/cm
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
Liquid
Critical
Pressure
kgf/cm2A
12.733
12.733
12.833
12.833
12.833
12.933
12.933
12.933
Vapor
Heat
Capacity
kcal/kg-C
2.2430
2.2600
2.2770
2.2930
2.3090
2.3250
2.3400
2.3550
2.3700
2.3850
2.4000
2.4150
2.4300
2.4440
2.4590
2.4730
2.4880
2.5020
2.5170
2.5310
Liquid
Density
kg/m3
698.10
702.40
706.70
710.90
715.10
719.20
723.20
727.20
731.20
735.10
738.90
742.70
746.40
750.20
753.80
757.40
761.00
764.50
768.00
771.50
Liquid
Dynamic
Viscosity
cP
0.6540
0.6840
0.7150
0.7490
0.7850
0.8240
0.8650
0.9100
0.9580
1.0100
1.0660
1.1270
1.1940
1.2660
1.3450
1.4320
1.5280
1.6340
1.7520
1.8950
Input Reprint
Page 20
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Hot Fluid Physical Property Data
2 Pressure Set, 159.93 kgf/cm2A
3
Liquid
Liquid
4
Thermal
Heat
5
Temp.
Cond.
Capacity
6
C
kcal/hr-m-C kcal/kg-C
7
189.00
0.1090
0.6630
8
183.00
0.1100
0.6580
9
178.00
0.1110
0.6520
10
173.00
0.1120
0.6460
11
167.00
0.1120
0.6410
12
162.00
0.1130
0.6350
13
156.00
0.1140
0.6290
14
151.00
0.1150
0.6240
15
146.00
0.1160
0.6180
16
140.00
0.1170
0.6120
17
135.00
0.1170
0.6060
18
129.00
0.1180
0.6010
19
20 Cold Fluid Property Data
21 Fluid name
22 Physical property method
23 Temperature interpolation option
24 Flash type
25 Quantity units
26 Heat release type
27 Cold Fluid Physical Property Data
28 Pressure Set, 14.233 kgf/cm2A
29
Vapor
30
Mass
31
Temp.
Enthalpy Fraction
32
C
kcal/kg
33
60.00
24.900
0.0023
34
68.00
29.000
0.0024
35
76.00
33.100
0.0026
36
84.00
37.300
0.0028
37
92.00
41.600
0.0029
38
99.00
46.000
0.0032
39
107.00
50.400
0.0034
40
115.00
54.900
0.0036
41
123.00
59.400
0.0038
42
131.00
64.000
0.0040
43
139.00
68.700
0.0043
44
147.00
73.400
0.0045
45
155.00
78.200
0.0048
46
163.00
83.100
0.0051
47
171.00
88.000
0.0054
48
178.00
92.900
0.0057
49
186.00
97.900
0.0060
50
Liquid
Surface
Tension
dyne/cm
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
13.000
Liquid
Critical
Pressure
kgf/cm2A
13.033
13.033
13.033
13.133
13.133
13.233
13.233
13.333
13.333
13.433
13.433
13.533
CHPS Liquid
Property tables
Program
Integral
Moles
Specific enthalpy
Vapor
Density
kg/m3
2.6400
2.7400
2.8500
2.9500
3.0700
3.1800
3.3000
3.4200
3.5400
3.6600
3.7900
3.9100
4.0400
4.1700
4.3100
4.4500
4.6000
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0110
0.0830
0.0120
0.0820
0.0120
0.0810
0.0120
0.0810
0.0130
0.0800
0.0130
0.0800
0.0130
0.0800
0.0140
0.0800
0.0140
0.0790
0.0140
0.0790
0.0150
0.0790
0.0150
0.0800
0.0150
0.0800
0.0150
0.0800
0.0160
0.0810
0.0160
0.0810
0.0160
0.0820
Vapor
Heat
Capacity
kcal/kg-C
1.4710
1.4110
1.3540
1.3020
1.2540
1.2110
1.1710
1.1350
1.1020
1.0710
1.0440
1.0200
0.9970
0.9760
0.9570
0.9390
0.9230
Liquid
Density
kg/m3
803.20
798.70
794.30
789.80
785.40
780.90
776.50
772.00
767.50
763.00
758.40
753.80
749.20
744.60
739.80
735.10
730.30
Liquid
Dynamic
Viscosity
cP
5.5770
4.5800
3.8230
3.2370
2.7770
2.4090
2.1120
1.8670
1.6650
1.4950
1.3510
1.2270
1.1210
1.0280
0.9470
0.8750
0.8110
Input Reprint
Page 21
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Cold Fluid Physical Property Data
2 Pressure Set, 14.233 kgf/cm2A
3
Vapor
4
Mass
5
Temp.
Enthalpy Fraction
6
C
kcal/kg
7
194.00
103.00
0.0064
8
202.00
108.10
0.0068
9
210.00
113.30
0.0072
10
11 Pressure Set, 14.233 kgf/cm2A
12
Liquid
Liquid
13
Thermal
Heat
14
Temp.
Cond.
Capacity
15
C
kcal/hr-m-C kcal/kg-C
16
60.00
0.0840
0.5060
17
68.00
0.0830
0.5150
18
76.00
0.0820
0.5250
19
84.00
0.0810
0.5330
20
92.00
0.0810
0.5420
21
99.00
0.0800
0.5510
22
107.00
0.0790
0.5590
23
115.00
0.0780
0.5670
24
123.00
0.0770
0.5750
25
131.00
0.0760
0.5830
26
139.00
0.0760
0.5900
27
147.00
0.0750
0.5980
28
155.00
0.0740
0.6050
29
163.00
0.0730
0.6120
30
171.00
0.0720
0.6190
31
178.00
0.0710
0.6260
32
186.00
0.0700
0.6330
33
194.00
0.0690
0.6400
34
202.00
0.0690
0.6470
35
210.00
0.0680
0.6530
36
37 Pressure Set, 13.033 kgf/cm2A
38
Vapor
39
Mass
40
Temp.
Enthalpy Fraction
41
C
kcal/kg
42
60.00
24.800
0.0024
43
68.00
28.900
0.0026
44
76.00
33.100
0.0027
45
84.00
37.300
0.0029
46
92.00
41.600
0.0031
47
99.00
45.900
0.0033
48
107.00
50.300
0.0036
49
115.00
54.800
0.0038
50
Vapor
Density
kg/m3
4.7500
4.9000
5.0600
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0160
0.0820
0.0170
0.0830
0.0170
0.0840
Liquid
Surface
Tension
dyne/cm
27.000
26.000
25.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
Liquid
Critical
Pressure
kgf/cm2A
14.033
13.933
13.933
13.933
13.833
13.833
13.733
13.733
13.733
13.633
13.633
13.633
13.533
13.533
13.533
13.433
13.433
13.433
13.333
13.333
Vapor
Density
kg/m3
2.5100
2.6100
2.7100
2.8100
2.9200
3.0300
3.1500
3.2600
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0110
0.0810
0.0120
0.0800
0.0120
0.0800
0.0120
0.0790
0.0130
0.0790
0.0130
0.0780
0.0130
0.0780
0.0140
0.0780
Vapor
Heat
Capacity
kcal/kg-C
0.9080
0.8950
0.8820
Liquid
Density
kg/m3
725.40
720.50
715.50
Liquid
Dynamic
Viscosity
cP
0.7540
0.7030
0.6560
Vapor
Heat
Capacity
kcal/kg-C
1.4310
1.3710
1.3160
1.2650
1.2190
1.1770
1.1390
1.1040
Liquid
Density
kg/m3
803.10
798.60
794.20
789.80
785.30
780.90
776.50
772.00
Liquid
Dynamic
Viscosity
cP
5.5680
4.5710
3.8150
3.2310
2.7710
2.4050
2.1080
1.8640
Input Reprint
Page 22
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Cold Fluid Physical Property Data
2 Pressure Set, 13.033 kgf/cm2A
3
Vapor
4
Mass
5
Temp.
Enthalpy Fraction
6
C
kcal/kg
7
123.00
59.400
0.0040
8
131.00
64.000
0.0043
9
139.00
68.700
0.0045
10
147.00
73.400
0.0048
11
155.00
78.200
0.0051
12
163.00
83.000
0.0054
13
171.00
87.900
0.0057
14
178.00
92.900
0.0061
15
186.00
97.900
0.0065
16
194.00
103.00
0.0068
17
202.00
108.10
0.0072
18
210.00
113.20
0.0076
19
20 Pressure Set, 13.033 kgf/cm2A
21
Liquid
Liquid
22
Thermal
Heat
23
Temp.
Cond.
Capacity
24
C
kcal/hr-m-C kcal/kg-C
25
60.00
0.0840
0.5060
26
68.00
0.0830
0.5150
27
76.00
0.0820
0.5250
28
84.00
0.0810
0.5330
29
92.00
0.0810
0.5420
30
99.00
0.0800
0.5510
31
107.00
0.0790
0.5590
32
115.00
0.0780
0.5670
33
123.00
0.0770
0.5750
34
131.00
0.0760
0.5830
35
139.00
0.0760
0.5910
36
147.00
0.0750
0.5980
37
155.00
0.0740
0.6050
38
163.00
0.0730
0.6120
39
171.00
0.0720
0.6190
40
178.00
0.0710
0.6260
41
186.00
0.0700
0.6330
42
194.00
0.0690
0.6400
43
202.00
0.0690
0.6470
44
210.00
0.0680
0.6530
45
46
47
48
49
50
Vapor
Density
kg/m3
3.3800
3.5000
3.6200
3.7400
3.8600
3.9900
4.1200
4.2600
4.4000
4.5400
4.6900
4.8400
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0140
0.0780
0.0140
0.0780
0.0150
0.0780
0.0150
0.0780
0.0150
0.0780
0.0150
0.0790
0.0160
0.0790
0.0160
0.0800
0.0160
0.0800
0.0160
0.0810
0.0170
0.0820
0.0170
0.0820
Liquid
Surface
Tension
dyne/cm
27.000
26.000
25.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
Liquid
Critical
Pressure
kgf/cm2A
13.933
13.933
13.933
13.833
13.833
13.733
13.733
13.733
13.633
13.633
13.533
13.533
13.533
13.433
13.433
13.433
13.333
13.333
13.233
13.233
Vapor
Heat
Capacity
kcal/kg-C
1.0730
1.0440
1.0180
0.9950
0.9730
0.9540
0.9360
0.9190
0.9040
0.8900
0.8770
0.8660
Liquid
Density
kg/m3
767.50
763.00
758.50
753.90
749.30
744.70
740.00
735.20
730.40
725.60
720.70
715.70
Liquid
Dynamic
Viscosity
cP
1.6620
1.4920
1.3490
1.2250
1.1190
1.0270
0.9450
0.8730
0.8100
0.7530
0.7020
0.6560
Input Reprint
Page 23
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Cold Fluid Physical Property Data
2 Pressure Set, 11.833 kgf/cm2A
3
Vapor
4
Mass
5
Temp.
Enthalpy Fraction
6
C
kcal/kg
7
60.00
24.800
0.0025
8
68.00
28.900
0.0027
9
76.00
33.000
0.0029
10
84.00
37.200
0.0031
11
92.00
41.500
0.0033
12
99.00
45.900
0.0035
13
107.00
50.300
0.0038
14
115.00
54.800
0.0040
15
123.00
59.300
0.0043
16
131.00
63.900
0.0046
17
139.00
68.600
0.0049
18
147.00
73.300
0.0052
19
155.00
78.100
0.0055
20
163.00
83.000
0.0058
21
171.00
87.900
0.0062
22
178.00
92.800
0.0065
23
186.00
97.800
0.0069
24
194.00
102.90
0.0073
25
202.00
108.00
0.0078
26
210.00
113.20
0.0082
27
28 Pressure Set, 11.833 kgf/cm2A
29
Liquid
Liquid
30
Thermal
Heat
31
Temp.
Cond.
Capacity
32
C
kcal/hr-m-C kcal/kg-C
33
60.00
0.0840
0.5060
34
68.00
0.0830
0.5150
35
76.00
0.0820
0.5250
36
84.00
0.0810
0.5330
37
92.00
0.0810
0.5420
38
99.00
0.0800
0.5510
39
107.00
0.0790
0.5590
40
115.00
0.0780
0.5670
41
123.00
0.0770
0.5750
42
131.00
0.0760
0.5830
43
139.00
0.0760
0.5910
44
147.00
0.0750
0.5980
45
155.00
0.0740
0.6050
46
163.00
0.0730
0.6120
47
171.00
0.0720
0.6200
48
178.00
0.0710
0.6260
49
186.00
0.0700
0.6330
50
Vapor
Density
kg/m3
2.3700
2.4600
2.5600
2.6700
2.7700
2.8800
2.9900
3.1000
3.2100
3.3300
3.4400
3.5600
3.6700
3.8000
3.9200
4.0500
4.1800
4.3200
4.4600
4.6000
Vapor
Vapor
Dynamic
Thermal
Viscosity
Cond.
cP
kcal/hr-m-C
0.0120
0.0790
0.0120
0.0790
0.0120
0.0780
0.0130
0.0780
0.0130
0.0770
0.0130
0.0770
0.0140
0.0760
0.0140
0.0760
0.0140
0.0760
0.0140
0.0760
0.0150
0.0760
0.0150
0.0770
0.0150
0.0770
0.0160
0.0770
0.0160
0.0780
0.0160
0.0780
0.0160
0.0790
0.0160
0.0790
0.0170
0.0800
0.0170
0.0810
Liquid
Surface
Tension
dyne/cm
27.000
26.000
25.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
27.000
Liquid
Critical
Pressure
kgf/cm2A
13.933
13.933
13.833
13.833
13.733
13.733
13.633
13.633
13.633
13.533
13.533
13.433
13.433
13.433
13.333
13.333
13.233
Vapor
Heat
Capacity
kcal/kg-C
1.3870
1.3290
1.2760
1.2270
1.1820
1.1420
1.1050
1.0720
1.0420
1.0150
0.9910
0.9690
0.9490
0.9310
0.9140
0.8980
0.8840
0.8710
0.8600
0.8490
Liquid
Density
kg/m3
803.00
798.60
794.10
789.70
785.30
780.90
776.40
772.00
767.50
763.00
758.50
754.00
749.40
744.80
740.10
735.40
730.60
725.80
720.90
716.00
Liquid
Dynamic
Viscosity
cP
5.5560
4.5620
3.8080
3.2250
2.7660
2.4010
2.1040
1.8610
1.6590
1.4900
1.3470
1.2240
1.1170
1.0250
0.9440
0.8720
0.8090
0.7520
0.7010
0.6550
Input Reprint
Page 24
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Summary Unit
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Cold Fluid Physical Property Data
2 Pressure Set, 11.833 kgf/cm2A
3
Liquid
Liquid
Liquid
4
Thermal
Heat
Surface
5
Temp.
Cond.
Capacity
Tension
6
C
kcal/hr-m-C kcal/kg-C
dyne/cm
7
194.00
0.0700
0.6400
27.000
8
202.00
0.0690
0.6470
27.000
9
210.00
0.0680
0.6530
27.000
10
11 Control Name Data
12 Case name
13 Item Number
14 Service
15 Customer
16 Address
17 Plant
18
19 Control Methods Data
20 Shellside friction factor method
21 Tubeside friction factor method
22 Pure longitudinal flow
23 Pure component condensation
24 Condensing correlation
25 Mole fraction inerts
26 Momentum exclusion
27 Perform shellside subcooling calculations
28 Pure component boiling
29 Check film boiling
30 Nucleate boiling method
31 Component boiling method
32 Reduced pressure calculation method
33 Increments per baffle
34
35 Control User-Defined Methods Data
36 Add non-nucleate boiling
37
38 Control Shells-in-Series
39 Maximum rigorous trials
40 Overdesign range
41 Series starting unit
42 Minimum allowable temperature approach
43 Maxumum duty tolerance
44 Simulation mode starting trial
45 Minimum Alpha
46 Maximum Alpha
47 Alpha adjustment
48 Starting adjustment trial
49
50
Liquid
Critical
Pressure
kgf/cm2A
13.233
13.233
13.133
70N-SOR
1837-E-003A-B
Reactor Effluent / CHPS Liquid Exchanger
Gujarat Refinery, IOCL
Vadodara, Gujarat
Lupech Project
Commercial
Commercial
No
No
HTRI Proration
0.0000
0.0000 %
No
No
Yes
Physical property/theoretical boiling range
Convective
Program decides
Calculated
Yes
25
2.0000 %
Program decides
1.00e-3 C
2.00e-5
13
1.0000
8.0000
1.0000
6
Output Summary
Page 25
Released to the following HTRI Member Company:
TEMA INDIA
MKH Units
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 See Data Check Messages Report for Warning Messages.
2 See Runtime Message Report for Warning Messages.
3
Process Conditions
4 Fluid name
5 Total flow rate
6 Inlet/Outlet Y
7 Inlet/Outlet T
8 Inlet P/Avg
9 dP/Allow.
10 Fouling
Cold Shellside
(1000-kg/hr)
(Wt. frac vap.)
(Deg C)
(kgf/cm2A)
(kgf/cm2)
(m2-hr-C/kcal)
11
CHPS Liquid
33.906
0.0076
210.00
13.385
2.100
0.000400
0.0889
232.00
162.63
0.725
HDF RX Effluent
36.403
0.0823
191.93
162.27
2.100
0.000300
Exchanger Performance
12 Shell h
13 Tube h
14 Hot regime
15 Cold regime
16 EMTD
17
(kcal/m2-hr-C)
(kcal/m2-hr-C)
(--)
(--)
(Deg C)
816.88
2291.7
Shear
Conv
27.9
Actual U
Required U
Unit Duty
Eff. area
Overdesign
(kcal/m2-hr-C)
(kcal/m2-hr-C)
(MM kcal/hr)
(m2)
(%)
Shell Geometry
18 TEMA type
19 Shell ID
20 Series
21 Parallel
22 Orientation
23
DFU
710.00
1
1
0.00
(--)
(mm)
(--)
(--)
(deg)
Baffle type
Baffle cut
Baffle orientation
Central spacing
Crosspasses
32 Shell
33 Tube
34 Fouling
35 Metal
36
(Pct Dia.)
(--)
(mm)
(--)
Single-Seg.
27.23
Parallel
198.00
27
Nozzles
(--)
(mm)
(mm)
(--)
(deg)
(--)
(--)
Thermal Resistance, %
305.34
294.14
1.2080
146.97
3.81
Baffle Geometry
Tube Geometry
24 Tube type
25 Tube OD
26 Length
27 Pitch ratio
28 Layout
29 Tubecount
30 Tube Pass
31
0.0049
154.02
13.668
0.566
Hot Tubeside
Plain
19.050
6086.
1.3333
45
418
2
Shell inlet
Shell outlet
Inlet height
Outlet height
Tube inlet
Tube outlet
(mm)
(mm)
(mm)
(mm)
(mm)
(mm)
Velocities, m/s
37.38
26.21 Tubeside
30.24 Crossflow
6.17 Longitudinal
Min
5.26
0.35
0.27
101.60
131.78
54.980
91.849
131.78
131.78
Flow Fractions
Max
5.64
1.10
0.44
A
B
C
E
F
0.226
0.555
0.055
0.165
0.000
Runtime Messages
Page 26
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Unit ID 101 - WARNING MESSAGES (CALCULATIONS CONTINUE)
2
3 Thermal & Hydraulic
4 Based on input property curves, your apparent boiling range is 2561.92 C ( 4611 F). The apparent boiling range was
5 used to calculate the mixture correction factors of nucleate and convective boiling coefficients. If the apparent boiling
6 range is incorrect, specify the correct value on the Cold Fluid Properties input panel and rerun the case.
(MN
7 6028)
8
9 At least one incremental pressure has exceeded 95% of the boiling fluid critical pressure. This is an upper limit in the
10 selected boiling method. The program assumed a ratio of incremental to critical pressure of 0.95 for the affected
11 increments. HTRI methods require the true-critical pressure as opposed to the pseudo-critical pressure. If the
12 true-critical pressure has been specified, check the specified process conditions and physical properties. (MN 6002)
13
14 Phase separation in the headers is possible for this design. Methods do not exist for rigorously predicting the extent of
15 phase separation in the headers, but the thermal performance may be overpredicted for such cases. (MN 2008)
16
17 Geometry, Mechanical Design, and Vibration
18 The design has parallel-cut baffles and the reported height under the nozzle lowers the bundle below the baffle cut.
19 Unrestricted longitudinal flow can bypass the bundle. This bypass region can be reduced by decreasing the height under
20 the nozzle, changing the baffle cut, or adding sealing arrangements. (MN 3505)
21
22 WARNING-prevention of tube ends erosion at the inlet needs to be considered in accordance with TEMA
23 recommendation when an axial inlet nozzle is used, when liquid Rho-V-squared exceeds 6000 lb/ft s2 (8928 kg/m s2) or
24 when there is two-phase flow at the inlet. (MN 3205)
25
26 The outlet nozzle velocity is greater than the tube exit velocity where momentum pressure drop between the tube exit
27 and the outlet nozzle is not included in the calculations. This pressure drop can be significant in a vacuum condenser.
28 Ensure you have margin for this additional pressure loss. (MN 3224)
29
30 A tubecount has been specified and the program has generated a tube layout that tries to matches the specified
31 tubecount. The user should review the tube layout drawing to assure that it is valid and as intended by the user. If the
32 generated tube layout drawing in not as intended, the user should make geometry changes, use the inputs provided on
33 the Tube Layout input panel or use the "Use tube layout drawing as input" option until the tube layout drawing better
34 matches the actual tubecount. (MN 3018)
35
36 The outlet baffle spacing is less than the calculated minimum outlet spacing 10.875 in. ( 276 mm) using estimated
37 nozzle clearance requirements. This could result in the last baffle being placed beneath or beyond the outlet nozzle. This
38 geometry is not recommended. (MN 3037)
39
40 ASME Section VIII Div. 1 Code was used to ESTIMATE all pressure vessel dimensions and weights. The dimensions in
41 this report cannot be used to fabricate the vessel. (MN 10170)
42
43 Shell inlet nozzle wall thickness may be too small for design conditions (MN 10017)
44
45 Specified inlet shell nozzle thickness does not meet internal pressure thickness requirements - reinforcement
46 calculations aborted. (MN 10120)
47
48 Specified inlet channel nozzle thickness does not meet internal pressure thickness requirements - reinforcement
49 calculations aborted. (MN 10122)
50
Runtime Messages
Page 27
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Unit ID 101 - WARNING MESSAGES (CALCULATIONS CONTINUE)
2
3 Geometry, Mechanical Design, and Vibration (cont.)
4 Specified outlet channel nozzle thickness does not meet internal pressure thickness requirements - reinforcement
5 calculations aborted. (MN 10123)
6
7 Tube-to-Baffle Clearance = 0.8 mm (0.03150 in) Exceeds TEMA Recommended 0.8 mm (0.03125 in). (MN 10042)
8
9 Fluid Properties
10 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the hot fluid at isobar no. 1 around increment
11 no. 13. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty,
12 and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100 Btu/lb). Check
13 the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
(MN 5091)
14
15 A negative latent heat has been calculated for the hot fluid at isobar no. 1 around increment no. 17. Using specific
16 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
17 the total incremental duty. These operations produced a negative value. Check the specified heat release curve, liquid
18 and vapor specific heats, and enthalpy values; rerun the case. (MN 5010)
19
20 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the hot fluid at isobar no. 2 around increment
21 no. 10. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty,
22 and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100 Btu/lb). Check
23 the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
(MN 5091)
24
25 A negative latent heat has been calculated for the hot fluid at isobar no. 2 around increment no. 17. Using specific
26 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
27 the total incremental duty. These operations produced a negative value. Check the specified heat release curve, liquid
28 and vapor specific heats, and enthalpy values; rerun the case. (MN 5010)
29
30 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the hot fluid at isobar no. 3 around increment
31 no. 10. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty,
32 and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100 Btu/lb). Check
33 the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
(MN 5091)
34
35 A negative latent heat has been calculated for the hot fluid at isobar no. 3 around increment no. 17. Using specific
36 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
37 the total incremental duty. These operations produced a negative value. Check the specified heat release curve, liquid
38 and vapor specific heats, and enthalpy values; rerun the case. (MN 5010)
39
40 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the cold fluid at isobar no. 1 around
41 increment no. 16. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible
42 liquid duty, and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100
43 Btu/lb). Check the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
44 (MN 5090)
45
46 A negative latent heat has been calculated for the cold fluid at isobar no. 1 around increment no. 3. Using specific
47 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
48 the total incremental duty. These calculations produced a negative value. Check the specified heat release curve, liquid
49 and vapor specific heat, and enthalpy values; rerun the case. (MN 5051)
50
Runtime Messages
Page 28
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Unit ID 101 - WARNING MESSAGES (CALCULATIONS CONTINUE)
2
3 Fluid Properties (cont.)
4 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the cold fluid at isobar no. 2 around
5 increment no. 16. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible
6 liquid duty, and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100
7 Btu/lb). Check the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
8 (MN 5090)
9
10 A negative latent heat has been calculated for the cold fluid at isobar no. 2 around increment no. 3. Using specific
11 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
12 the total incremental duty. These calculations produced a negative value. Check the specified heat release curve, liquid
13 and vapor specific heat, and enthalpy values; rerun the case. (MN 5051)
14
15 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the cold fluid at isobar no. 3 around
16 increment no. 16. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible
17 liquid duty, and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100
18 Btu/lb). Check the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
19 (MN 5090)
20
21 A negative latent heat has been calculated for the cold fluid at isobar no. 3 around increment no. 3. Using specific
22 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
23 the total incremental duty. These calculations produced a negative value. Check the specified heat release curve, liquid
24 and vapor specific heat, and enthalpy values; rerun the case. (MN 5051)
25
26 The physical properties of the cold fluid have been extrapolated beyond the valid temperature range. Check the
27 calculated values. The thermal analysis requires properties at bulk and skin/wall temperatures. (MN 5033)
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
Final Results
Page 29
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
Process Data
Cold Shellside
Hot Tubeside
2 Fluid name
3 Fluid condition
4 Total flow rate
5 Weight fraction vapor, In/Out
6 Temperature, In/Out
7 Skin temperature, Min/Max
8 Wall temperature, Min/Max
9 Pressure, In/Average
10 Pressure drop, Total/Allowed
11 Velocity, Mid/Max allow
12 Boiling range/Mole fraction inert
13 Average film coef.
14 Heat transfer safety factor
15 Fouling resistance
CHPS Liquid
Boil. Liquid
33.906
0.0076
210.00
219.25
221.69
13.385
2.100
HDF RX Effluent
Cond. Vapor
36.403
0.0889
0.0823
232.00
191.93
182.74
226.52
176.08
222.93
162.63
162.27
0.725
2.100
5.47
0.0000
2291.7
1.0000
0.000300
(1000-kg/hr)
(--)
(Deg C)
(Deg C)
(Deg C)
(kgf/cm2A)
(kgf/cm2)
(m/s)
(Deg C)
(kcal/m2-hr-C)
(--)
(m2-hr-C/kcal)
16
(kcal/m2-hr-C)
(MM kcal/hr)
(Deg C)
(Deg C)
39 Type
40 Crosspasses/shellpass
41 Central spacing
42 Inlet/Outlet Spacing
43 Turn Spacing
44 Baffle thickness
45 Insulated long baffle
46 Use deresonating baffles
47
48 Tube type
49 Length to tangent
50 Effective length
51 Total tubesheet
52 Area ratio
53 Tube metal
294.14 /
1.2080 /
27.9
29.4 *
437.67
0.9953
/
305.34
* 0.9564
1731.6
330.0
Shell Construction Information
30 TEMA shell type
DFU
31 Shells Series
1 Parallel
32 Passes Shell
2 Tube
33 Shell orientation angle (deg)
0.00
34 Impingement present
Rods
35 Pairs seal strips
3
36 Shell expansion joint
No
37 Weight estimation Wet/Dry/Bundle
38
2566.2
816.88
1.0000
0.000400
Overall Performance Data
17 Overall coef., Reqd/Clean/Actual
18 Heat duty, Calculated/Specified
19 Effective overall temperature difference
20 EMTD = (MTD) * (DELTA) * (F/G/H)
21
22
23 See Runtime Messages Report for
24 warnings.
25
26
Exchanger Fluid Volumes
27 Approximate shellside (L)
28 Approximate tubeside (L)
29
0.0049
154.02
169.23
173.78
13.668
0.566
0.91
1
2
Shell ID
Total area
Eff. area
(mm)
(m2)
(m2/shell)
710.00
152.25
146.97
Impingement rod rows
2
Passlane seal rods (mm) 0.000 No. 0
UBend tangent to Support Dist. (mm) 40.000
14064 /
12004 /
5713.5 (kg/shell)
Baffle Information
Parallel Single-Seg.
27
(mm)
198.00
(mm)
727.00
(mm)
198.00
(mm)
4.762
No
No
Baffle cut (% dia) 27.23
No. (Pct Area)
(mm) to C.L
1
21.72
161.67
2
0.00
0.000
Long. baffle length
(mm)
5677.
Tube Information
Plain
(mm)
6086.
(mm)
5875.
(mm)
171.00
(out/in)
1.9676
SA-213 T22
Tubecount per shell
Pct tubes removed (both)
Outside diameter
(mm)
Wall thickness
(mm)
Pitch (mm)
25.400 Ratio
Tube pattern (deg)
418
7.52
19.050
4.684
1.3333
45
Final Results
Page 30
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
Shellside Performance
2 Nom vel, X-flow/window
0.96 / 0.88
3
4 Flow fractions for vapor phase
5
A=0.2263 B=0.5546 C=0.0545 E=0.1646
6
7
Shellside Heat Transfer Corrections
8
9
Total
0.987
Beta
0.920
Cross
77.96
MOMENTUM
Window
13.10
10
11
12
13
Gamma
1.072
Fin
1.000
Ends
6.13
0.10
Nozzle
Inlet
Outlet
Shell
2.02
0.70
Tube
3.66
2.17
Two-Phase Parameters
Method
RPM
PP/TBR
18
Inlet
Shear
Conv
Center
Shear
Conv
H. T. Parameters
19 Overall wall correction
20 Midpoint
Prandtl no.
21 Midpoint
Reynolds no.
22 Bundle inlet
Reynolds no.
23 Bundle outlet
Reynolds no.
24 Fouling layer
(mm)
25
50
Outlet
Shear
Conv
Mix F
0.7326
Shell
Tube
7452
2304
8774
8946
10374
7476
Thermal Resistance, %
26
Shell
Tube
Fouling
27
37.38
26.21
30.24
28 Total fouling resistance
(m2-hr-C/kcal)
29 Differential resistance
(m2-hr-C/kcal)
30
Shell Nozzles
31 Inlet at channel end
32 Nozzle location at U-bend
33
34
35 Number at each position
36 Diameter
(mm)
37 Velocity
(m/s)
38 Pressure drop
(kgf/cm2)
39 Height under nozzle
(mm)
40 Nozzle R-V-SQ
(kg/m-s2)
41 Shell ent.
(kg/m-s2)
42
43
44
Tube Nozzle
45 Diameter
(mm)
46 Velocity
(m/s)
47 Pressure drop
(kgf/cm2)
48 Nozzle R-V-SQ
(kg/m-s2)
49
Annular Distributor
51 Length
52 Height
53 Slot area
Metal
6.17
Over Des
3.81
9.90e-4
1.25e-4
Yes
After U-bend
Inlet
1
101.60
2.99
0.011
54.980
3471.0
539.85
Outlet
1
131.78
2.04
3.94e-3
91.849
1410.1
151.79
Inlet
RADIAL
131.78
6.38
0.027
4729.8
Outlet
RADIAL
131.78
5.94
0.016
4401.8
Inlet
Outlet
Liquid
Outlet
0
Liquid
Outlet
(mm)
(mm)
(mm2)
54
55
56
End
0.949
Pressure Drops (Percent of Total)
14
15
16
17
F=0.0000
Diametral Clearances (mm)
Baffle-to-shell
4.8000
Bundle-to-shell
20.194
Tube-to-baffle
0.8000
Supplementary Results
Page 31
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
Externally Enhanced Tube Geometry
2 Type
3 Fin density
4 Fin height
5 Fin thickness
6 Root diameter
7 Area/length
8
Plain
None
(mm)
(L/D)
Mean Metal Temperatures
10 Mean shell temperature
11 Tubesheet temperature
12
13
14
15
16
Type
Thickness
Pitch
(fin/meter)
(mm)
(mm)
(mm)
(m2/m)
9
Internally Enhanced Tube Geometry
183.92 (C)
343.00 (C)
Mean tube metal temperature in each tubepass, (C)
Tube Pass
1
2
Inside
212.33
188.54
Outside
210.71
186.54
Radial
211.34
187.32
Vibration Analysis
Page 32
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Shellside condition
Boil. Liquid
2 Axial stress loading
(kg/mm2)
0.000
Added mass factor
3 Beta
4.217
4
Position In The Bundle
Inlet
Center
5 Length for natural frequency
(mm)
925.
396.
6 Length/TEMA maximum span
(--)
0.607
0.260
7 Number of spans
(--)
14
14
8 Tube natural frequency
(Hz)
88.6 +
262.9
9 Shell acoustic frequency
(Hz)
10
Flow Velocities
Inlet
Center
11 Window parallel velocity
(m/s)
0.63
0.68
12 Bundle crossflow velocity
(m/s)
0.17
0.71
13 Bundle/shell velocity
(m/s)
0.68
0.73
14
Fluidelastic Instability Check
Inlet
Center
15 Log decrement
HTRI
0.091
0.088
16 Critical velocity
(m/s)
7.67
42.43
17 Baffle tip cross velocity ratio
(--)
0.0242
0.0177
18 Average crossflow velocity ratio
(--)
0.0303
0.0221
19
Acoustic Vibration Check
Inlet
Center
20 Vortex shedding ratio
(--)
21 Chen number
(--)
22 Turbulent buffeting ratio
(--)
23
Tube Vibration Check
Inlet
Center
24 Vortex shedding ratio
(--)
0.062
0.250
25 Parallel flow amplitude
(mm)
0.000
0.000
26 Crossflow amplitude
(mm)
0.001
0.000
27 Tube gap
(mm)
6.350
6.350
28 Crossflow amplitude/tube gap
(--)
1.44e-4
7.79e-5
29 Crossflow RHO-V-SQ
(kg/m-s2)
20.96
318.67
30
Bundle Entrance/Exit
31
(analysis at first tube row)
Entrance
32 Fluidelastic instability ratio
(--)
0.024
33 Vortex shedding ratio
(--)
0.065
34 Crossflow amplitude
(mm)
0.00101
35 Crossflow velocity
(m/s)
0.18
36 Tubesheet to inlet/outlet support
(mm)
None
37
Shell Entrance/Exit Parameters
Entrance
38 Impingement device
Rods
39 Flow area
(m2)
0.021
40 Velocity
(m/s)
1.18
41 Critical velocity
(m/s)
7.67
42 RHO-V-SQ
(kg/m-s2)
539.85
43 Shell type
DFU
Baffle type
44 Tube type
Plain
Baffle layout
45 Pitch ratio
1.3333
Tube diameter, (mm)
46 Layout angle
45
Tube material
47 Number U-Bend supports
2
Elastic modulus, (kg/mm2)
48 Use deresonating baffles
No
Supports/baffle space
49
Program Messages
50 + Natural or acoustic frequency used in vibration analysis.
51 See help for additional information.
52 * Items with asterisk exceed a conservative lower limit for vibration-free design.
53 Review your case using the procedure described in Online Help;
54 You may find that a vibration problem is unlikely.
55
56
MKH Units
1.394
Outlet
925.
0.607
14
89.1
Outlet
0.73
0.20
0.21
Outlet
0.087
7.99
0.0267
0.0334
Outlet
Outlet
0.071
0.000
0.001
6.350
1.65e-4
24.10
Exit
0.027
0.075
0.00117
0.21
None
Exit
-0.042
0.67
7.99
151.79
Single-Seg.
Parallel
19.050
SA-213 T22
20072
HEAT EXCHANGER RATING DATA SHEET
Page 33
1
Released to the following HTRI Member Company:
2
MKH Units
TEMA INDIA
3
4
5 Service of Unit Reactor Effluent / CHPS Liquid Exchanger
Item No.
6 Type
DFU
Orientation Horizontal
Connected In
1 Parallel
1 Series
7 Surf/Unit (Gross/Eff)
152.25 / 146.97 m2
Shell/Unit 1
Surf/Shell (Gross/Eff)
152.25 / 146.97 m2
8
PERFORMANCE OF ONE UNIT
9 Fluid Allocation
Shell Side
Tube Side
10 Fluid Name
CHPS Liquid
HDF RX Effluent
11 Fluid Quantity, Total
1000-kg/hr
33.906
36.403
12 Vapor (In/Out)
wt%
0.49
0.76
8.89
8.23
13 Liquid
wt%
99.51
99.24
91.11
91.77
14 Temperature (In/Out)
C
154.02
210.00
232.00
191.93
kg/m3
15 Density
3.9413 V/L 749.82 4.8526 V/L 715.69 12.180 V/L 697.50 12.198 V/L 728.46
cP
16 Viscosity
0.0150 V/L 1.1347 0.0170 V/L 0.6560 0.0140 V/L 0.6550 0.0133 V/L 0.9301
kcal/kg-C
17 Specific Heat
0.9883 V/L 0.6041 0.8669 V/L 0.6530 2.2460 V/L 0.7090 2.3625 V/L 0.6667
kcal/hr-m-C
18 Thermal Conductivity
0.0791 V/L 0.0741 0.0821 V/L 0.0680 0.2460 V/L 0.1010 0.2322 V/L 0.1084
kgf/cm2A
19 Critical Pressure
kgf/cm2A
20 Inlet Pressure
13.668
162.63
m/s
21 Velocity
0.91
5.47
kgf/cm2
22 Pressure Drop, Allow/Calc
2.100
0.566
2.100
0.725
kcal/m2-hr-C
23 Average Film Coefficient
816.88
2291.7
m2-hr-C/kcal
24 Fouling Resistance (min)
0.000400
0.000300
1.2080 MM kcal/hr
25 Heat Exchanged
MTD (Corrected)
27.9 C
Overdesign
3.81 %
294.14 kcal/m2-hr-C
26 Transfer Rate, Service
Calculated
305.34 kcal/m2-hr-C Clean
437.67 kcal/m2-hr-C
27
CONSTRUCTION OF ONE SHELL
Sketch (Bundle/Nozzle Orientation)
28
Shell Side
Tube Side
29 Design Pressure
kgf/cm2G
130.50
169.60
30 Design Temperature
C
289.00
343.00
31 No Passes per Shell
2
2
32 Flow Direction
Upward
Downward
Connections
33
In
mm
1
@ 101.60
1
@ 131.78
Size &
34
Out
mm
1
@ 131.78
1
@ 131.78
Rating
35
Liq. Out mm
@
1
@
OD 19.050 mm
36 Tube No. 418.00
Thk(Avg) 4.684
mm
Length 6086. mm Pitch 25.400 mm
Tube pattern 45
Pairs seal strips
37 Tube Type Plain
Material SA-213 T22
3
Passlane Seal Rod No.
38 Shell ID
710.00 mm
Kettle ID
mm
0
Impingement Plate
39 Cross Baffle Type
Parallel
Single-Seg.
%Cut (Diam) 27.23
Rods
No. of Crosspasses
40 Spacing(c/c)
198.00 mm
Inlet
727.00 mm
27
Shell Exit
41 Rho-V2-Inlet Nozzle 3471.0
kg/m-s2
Shell Entrance
539.85 kg/m-s2
151.79 kg/m-s2
Bundle Exit
42
Bundle Entrance
13.22 kg/m-s2
15.21 kg/m-s2
43 Weight/Shell
12004
kg
Filled with Water
14064 kg
Bundle
5713.5 kg
44 Notes:
Thermal Resistance, %
Velocities, m/s
Flow Fractions
45
Shell
37.38 Shellside
0.91 A
0.226
46
Tube
26.21 Tubeside
5.47 B
0.555
47
Fouling
30.24 Crossflow
0.96 C
0.055
48
Metal
6.17 Window
0.88 E
0.165
0.000
F
49
HEAT EXCHANGER SPECIFICATION SHEET
Page 34
1
Released to the following HTRI Member Company:
MKH Units
2
TEMA INDIA
3
Job No.
4
Gujarat Refinery, IOCL
Reference No.
5 Customer
Vadodara, Gujarat
Proposal No.
6 Address
Lupech Project
Date
7/21/2023
Rev
7 Plant Location
Reactor Effluent / CHPS Liquid Exchanger
Item No.
8 Service of Unit
710 x 6086
mm
Type
DFU
Horizontal
Connected In
1
Parallel
1 Series
9 Size
152.25 / 146.97 m2
Shell/Unit
1
Surf/Shell (Gross/Eff)
152.25 / 146.97 m2
10 Surf/Unit (Gross/Eff)
PERFORMANCE OF ONE UNIT
11
Shell Side
Tube Side
12 Fluid Allocation
CHPS Liquid
HDF RX Effluent
13 Fluid Name
kg/hr
33906
36403
14 Fluid Quantity, Total
166.35
258.41
3236.2
2996.7
15 Vapor (In/Out)
33740
33648
33167
33406
16 Liquid
17 Steam
18 Water
19 Noncondensables
C
154.02
210.00
232.00
191.93
20 Temperature (In/Out)
0.7502
0.7160
0.6978
0.7288
21 Specific Gravity
cP
0.0150 V/L 1.1347 0.0170 V/L 0.6560 0.0140 V/L 0.6550 0.0133 V/L 0.9301
22 Viscosity
23 Molecular Weight
24 Molecular Weight, Noncondensables
kcal/kg-C
0.9883 V/L 0.6041
0.8669 V/L 0.6530 2.2460 V/L 0.7090 2.3625 V/L 0.6667
25 Specific Heat
kcal/hr-m-C
0.0791 V/L 0.0741
0.0821 V/L 0.0680 0.2460 V/L 0.1010 0.2322 V/L 0.1084
26 Thermal Conductivity
kcal/kg
320.33
611.11
265.30
535.23
27 Latent Heat
kgf/cm2A
13.668
162.63
28 Inlet Pressure
m/s
0.91
5.47
29 Velocity
kgf/cm2
2.100
0.566
2.100
0.725
30 Pressure Drop, Allow/Calc
m2-hr-C/kcal
0.000400
0.000300
31 Fouling Resistance (min)
1208044 kcal/hr
MTD (Corrected)
27.9
C
32 Heat Exchanged
294.14 kcal/m2-hr-C
Clean 437.67 kcal/m2-hr-C
Actual
305.34 kcal/m2-hr-C
33 Transfer Rate, Service
CONSTRUCTION OF ONE SHELL
Sketch (Bundle/Nozzle Orientation)
34
Shell Side
Tube Side
35
kgf/cm2G
130.50 /
169.60 /
36 Design/Test Pressure
C
289.00
343.00
37 Design Temperature
2
2
38 No Passes per Shell
mm
4.500
4.500
39 Corrosion Allowance
Connections
In
mm
1 @ 101.60
1 @ 131.78
40
Size &
Out
mm
1 @ 131.78
1 @ 131.78
41
Rating
Intermediate
@
@
42
OD 19.050 mm
Thk(Avg) 4.684 mm
Length 6086.
mm
Pitch 25.400 mm
43 Tube No. 209U
Material SA-213 T22
Tube pattern45
44 Tube Type Plain
SA-387 GR 22 CL 2
ID 710.00 OD 792.55 mm Shell Cover
SA-387 GR 22 CL 2
(Integ.)
45 Shell
SA-336 F22 CL 3
Channel Cover SA-336 F22 CL 3
46 Channel or Bonnet
SA-336 F22 CL 3
Tubesheet-Floating
47 Tubesheet-Stationary
Impingement Plate Rods
48 Floating Head Cover
SA-387 GR 22 CL 2
Type Single-Seg.
%Cut (Diam) 27.23 Spacing(c/c) 198.00
Inlet 727.00 mm
49 Baffles-Cross
Seal Type Lamiflex
50 Baffles-Long
U-Bend
Type Full support
51 Supports-Tube
3
pairs seal strips
Tube-Tubesheet Joint Expanded and strength welded
52 Bypass Seal Arrangement
Type
None
53 Expansion Joint
3471.0 kg/m-s2
Bundle Entrance
13.22 Bundle Exit
15.21
kg/m-s2
54 Rho-V2-Inlet Nozzle
Tube Side
Mach. Mtl. (Kammprofile\Flex. Face)
55 Gaskets-Shell Side Mach. Mtl. (Kammprofile\Flex. Face)
- Floating Head
56
TEMA Class
R
57 Code Requirements ASME
12004
kg
Filled with Water
14064 kg
Bundle
5713.5
kg
58 Weight/Shell
59 Remarks:
60
61
62
Reprinted with Permission
63
U-Bend Schedule
Page 35
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
Number of Straight
Bend
Total
1
Tubes
Length
Diameter Length
Row
2 (-)
(-)
mm
mm
mm
3
1
19
6086.0
76.200
12292
4
2
18
6086.0
112.12
12348
5
3
19
6086.0
148.04
12405
6
4
18
6086.0
183.96
12461
7
5
17
6086.0
219.88
12517
8
6
18
6086.0
255.81
12574
9
7
17
6086.0
291.73
12630
10
8
16
6086.0
327.65
12687
11
9
15
6086.0
363.57
12743
12 10
16
6086.0
399.49
12800
13 11
15
6086.0
435.41
12856
14 12
14
6086.0
471.33
12912
15 13
13
6086.0
507.25
12969
16 Total
215
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
MKH Units
Input Reprint
Page 39
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Exchanger Data
2 Unit identifier
3 Service type
4 TEMA type
5 Run mode
6 Hot fluid location
7 Unit orientation
8 Number of shells in series
9 Number of shells in parallel
10 Flow in 1st tubepass
11 Train flow direction
12
13 Construction Data
14 Shell material
15 Tube material
16 Shell cover material
17 Channel or bonnet material
18 Tubesheet-Stationary material
19 Baffle-Cross material
20 Shellside gasket
21 Tubeside gasket
22 Shellside design pressure
23 Tubeside design pressure
24 Shellside vacuum pressure
25 Tubeside vacuum pressure
26 Shellside design temperature
27 Tubeside design temperature
28 Shellside corrosion allowance
29 Tubeside corrosion allowance
30 Tubesheet design temperature
31 Shellside radiography
32 Tubeside radiography
33 TEMA class
34 Small exchanger
35 Shell outside diameter
36 Shell inside diameter
37 Shell wall thickness
38 Front head outside diameter
39 Front head inside diameter
40 Front head thickness
41 Rear head outside diameter
42 Rear head inside diameter
43 Rear head thickness
44 Total tubesheet thickness
45 Double tubesheet
46 Shell expansion joint
47 Suppress mechanical calculations
48
49
50
Shell 1
Generic shell and tube
DFU
Rating
Tubeside
Horizontal
1
1
Countercurrent
Countercurrent
SA-387 GR 22 CL 2
SA-213 T22
SA-387 GR 22 CL 2
SA-336 F22 CL 3
SA-336 F22 CL 3
SA-387 GR 22 CL 2
Mach. Mtl. (Kammprofile\Flex. Face)
Mach. Mtl. (Kammprofile\Flex. Face)
130.50 kgf/cm2G
169.60 kgf/cm2G
Full
Full
289.00 C
343.00 C
4.500 mm
4.500 mm
343.00 C
Full
Full
R
No
792.55 mm
710.00 mm
41.275 mm
811.60 mm
710.00 mm
50.800 mm
805.25 mm
710.00 mm
47.625 mm
171.00 mm
No
No
No
Input Reprint
Page 40
Released to the following HTRI Member Company:
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MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Tube Data
2 Tube type
3 Tube outside diameter
4 Tube wall thickness
5 Tube pitch
6 Tube pitch ratio
7 Tubepasses per shell
8 Tube pattern
9 Number of tubes per shell
10 Tube count method
11 Tube length
12 Tube material
13
14 Baffle Data
15 Baffle type
16 Baffle orientation
17 Baffle cut percent
18 Adjust baffle cut
19 Double segmental set center baffle at inlet
20 Number of crosspasses
21 Central baffle spacing
22 Inlet/outlet spacing
23 Variable baffle spacing
24 Window cut from baffles
25 Use deresonating baffles
26
27 Supports Data
28 Full support at U-Bend
29 Support distance to U-bend tangent
30 Number of U-bend supports
31 Include inlet vibration support
32 Include outlet vibration support
33
34 Longitudinal Baffle Data
35 Insulated longitudinal baffle
36 Seal type
37
38
39
40
41
42
43
44
45
46
47
48
49
50
Plain
19.050 mm
4.684 mm
25.400 mm
1.333
2
45 degrees
418.00
Rigorous
6086. mm
SA-213 T22
Single segmental
Parallel
27.230 % shell ID
No adjustment
Program set
27
198.00 mm
727.00 mm
No
No
No
Full support
40.000 mm
2
No
No
No
Lamiflex
Input Reprint
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Released to the following HTRI Member Company:
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MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Nozzle Data
2 Shellside
3 Nozzle standard
4 Shell entrance type
5 Shell exit type
6
7 Nozzle outside diameter
8 Nozzle schedule
9 Nozzle inside diameter
10 Number at this position
11 Tubeside
12 Nozzle standard
13
14 Nozzle outside diameter
15 Nozzle schedule
16 Nozzle inside diameter
17 Number at this position
18
19 Nozzle Location Data
20 Radial position on shell inlet nozzle
21 Radial position on shell outlet nozzle
22 Location of nozzle at U-bend
23 Tubeside entry type
24 Tubeside inlet position
25 Tubeside exit type
26
27 Impingement Data
28 Impingement type
29 Use tube positions to place rods
30 Impingement rod rows
31 Impingement rod diameter
32 Impingement rod pitch
33 Impingement rods on centerline
34 Impingement rod layout angle
35 Rod row width to nozzle diameter
36
37 Tube Layout Data
38 Pass partition construction
39 Force symmetric layout
40 Force continuous cleaning lanes
41 Force uniform layout
42 Align across primary passlanes
43 Fill knock out area with dummy tubes
44 Fill bundle periphery with dummy tubes
45 Fill passlanes with dummy tubes
46 Shifted staggered layout
47 Use crossed U-bends
48 Minimum U-bend diameter
49 Use tube layout drawing as input
50
01-ANSI_B36_10.TABLE
Use impingement device
Remove tubes if TEMA requires
Inlet
Outlet Liq. Outlet
114.30
168.28
-- mm
STD
STD
-101.60
131.78
-- mm
1
1
--
Inlet
168.28
STD
131.78
1
01-ANSI_B36_10.TABLE
Outlet Liq. Outlet
168.28
-- mm
STD
-131.78
-- mm
1
--
Program decides
Program decides
After U-bend
Radial
Front head
Same as inlet
Rods
No
2
20.000 mm
25.400 mm
Yes
45.00 deg
2.3180
Program set
Yes
No
No
No
Program set
Program set
Program Set
Program set
No
76.200 mm
No
Input Reprint
Page 42
Released to the following HTRI Member Company:
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Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Clearance Data
2 Number of seal strip pairs
3 Block A stream
4 Block E stream
5 Block F stream
6 Number of passlane seal rods
7 Tubes to remove for tie rods
8 Number of tie rods
9 Tie rod outside diameter
10 Tube to baffle clearance
11 Baffle to shell clearance
12 Bundle to shell clearance
13 Baffle clearance type
14
15 Process Conditions Data
16 Phase condition
17 Flow rate
18 Inlet temperature
19 Outlet temperature
20 Inlet pressure
21 Allowable pressure drop
22 Duty multiplier
23
24 Process Fouling Data
25 Fouling resistance
26
27 Control Name Data
28 Case name
29 Service
30 Customer
31 Address
32 Plant
33
34 Control Methods Data
35 Shellside friction factor method
36 Tubeside friction factor method
37 Pure longitudinal flow
38 Pure component condensation
39 Condensing correlation
40 Mole fraction inerts
41 Momentum exclusion
42 Perform shellside subcooling calculations
43 Pure component boiling
44 Check film boiling
45 Nucleate boiling method
46 Component boiling method
47 Reduced pressure calculation method
48 Increments per baffle
49
50
3
No
No
No
Calculated
1
12
12.700 mm
0.800 mm
4.800 mm
20.190 mm
TEMA
Hot Fluid
Two phase
36.403
232.00
-162.63
2.100
Cold Fluid
Two phase
33.906 1000-kg/hr
-- C
210.00 C
13.668 kgf/cm2A
2.100 kgf/cm2
1.0000
Hot Fluid
0.0003
Cold Fluid
0.0004 m2-hr-C/kcal
70N-SOR
Reactor Effluent / CHPS Liquid Exchanger
Gujarat Refinery, IOCL
Vadodara, Gujarat
Lupech Project
Commercial
Commercial
No
No
HTRI Proration
0.0000
0.0000 %
No
No
Yes
Physical property/theoretical boiling range
Convective
Program decides
Calculated
Input Reprint
Page 43
Released to the following HTRI Member Company:
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Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Control User-Defined Methods Data
2 Add non-nucleate boiling
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
Yes
Drawings
Page 36
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
710
mm
6086
mm
Unit
TEMA type
Shell diameter
Tube length
Dry weight
Wet weight
Bundle weight
Shell 1
DFU
710
6086
12004
14064
5713
mm
mm
kg/shell
kg/shell
kg/shell
Total tube inlet nozzles
Total tube outlet nozzles
Total shell inlet nozzles
Total shell outlet nozzles
1
1
1
1
Stream ID
Stream name
Flow (total), 1000-kg/hr
Pressure drop, kgf/cm2
Temperature, C
Wt. fraction vapor
Pressure, kgf/cm2A
Shellside
CHPS Liquid
33.906
0.566
154.02
210.00
0.0049
0.0076
13.668
13.102
Tubeside
HDF RX Effluent
36.403
0.725
232.00
191.93
0.0889
0.0823
162.63
161.91
Drawings
Page 37
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 1
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
Unit
TEMA type
Shell ID
Actual OTL
Height under inlet nozzle
Rows of impingement rods
Impingement rod OD
Height under outlet nozzle
Tube type
Tube OD
Tube pitch
Tube layout angle
Tubes
Tube positions available
Tie rods
Seal strip pairs
Tube Passes
Parallel passlane width
Baffle cut % diameter
131.78 mm
TUBEPASS DETAILS
Pass
Rows Tubes
1
13
215
2
13
215
SYMBOL LEGEND
Tube
Dummy Short Tube
Dummy Long Tube
Plugged Tube
Tie Rod
Seal Rod
Impingement Rod
1
101.60 mm
2
Shell 1
DFU
710.00 mm
689.81 mm
54.980 mm
2
20.000 mm
91.849 mm
Plain
19.050 mm
25.400 mm
45 deg
418
430
12
3
2
57.150 mm
27.23
Output Summary
Page 44
Released to the following HTRI Member Company:
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MKH Units
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 See Data Check Messages Report for Warning Messages.
2 See Runtime Message Report for Warning Messages.
3
Process Conditions
4 Fluid name
5 Total flow rate
6 Inlet/Outlet Y
7 Inlet/Outlet T
8 Inlet P/Avg
9 dP/Allow.
10 Fouling
Cold Shellside
(1000-kg/hr)
(Wt. frac vap.)
(Deg C)
(kgf/cm2A)
(kgf/cm2)
(m2-hr-C/kcal)
11
CHPS Liquid
33.906
0.0049
154.02
13.950
2.100
0.000400
0.0823
191.93
161.91
0.734
HDF RX Effluent
36.403
0.0752
129.00
161.54
2.100
0.000300
Exchanger Performance
12 Shell h
13 Tube h
14 Hot regime
15 Cold regime
16 EMTD
17
(kcal/m2-hr-C)
(kcal/m2-hr-C)
(--)
(--)
(Deg C)
660.10
1665.8
Shear
Conv
49.4
Actual U
Required U
Unit Duty
Eff. area
Overdesign
(kcal/m2-hr-C)
(kcal/m2-hr-C)
(MM kcal/hr)
(m2)
(%)
Shell Geometry
18 TEMA type
19 Shell ID
20 Series
21 Parallel
22 Orientation
23
DFU
710.00
1
1
0.00
(--)
(mm)
(--)
(--)
(deg)
Baffle type
Baffle cut
Baffle orientation
Central spacing
Crosspasses
32 Shell
33 Tube
34 Fouling
35 Metal
36
(Pct Dia.)
(--)
(mm)
(--)
Single-Seg.
27.23
Parallel
198.00
27
Nozzles
(--)
(mm)
(mm)
(--)
(deg)
(--)
(--)
Thermal Resistance, %
257.22
245.31
1.7820
146.97
4.85
Baffle Geometry
Tube Geometry
24 Tube type
25 Tube OD
26 Length
27 Pitch ratio
28 Layout
29 Tubecount
30 Tube Pass
31
0.0023
60.00
14.233
0.566
Hot Tubeside
Plain
19.050
6086.
1.3333
45
418
2
Shell inlet
Shell outlet
Inlet height
Outlet height
Tube inlet
Tube outlet
(mm)
(mm)
(mm)
(mm)
(mm)
(mm)
Velocities, m/s
38.97
30.38 Tubeside
25.47 Crossflow
5.18 Longitudinal
Min
4.67
0.28
0.23
131.78
131.78
54.980
91.849
131.78
131.78
Flow Fractions
Max
5.25
0.94
0.39
A
B
C
E
F
0.225
0.556
0.055
0.164
0.000
Runtime Messages
Page 45
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Unit ID 102 - WARNING MESSAGES (CALCULATIONS CONTINUE)
2
3 Thermal & Hydraulic
4 Based on input property curves, your apparent boiling range is 2566.23 C ( 4619 F). The apparent boiling range was
5 used to calculate the mixture correction factors of nucleate and convective boiling coefficients. If the apparent boiling
6 range is incorrect, specify the correct value on the Cold Fluid Properties input panel and rerun the case.
(MN
7 6028)
8
9 At least one incremental pressure has exceeded 95% of the boiling fluid critical pressure. This is an upper limit in the
10 selected boiling method. The program assumed a ratio of incremental to critical pressure of 0.95 for the affected
11 increments. HTRI methods require the true-critical pressure as opposed to the pseudo-critical pressure. If the
12 true-critical pressure has been specified, check the specified process conditions and physical properties. (MN 6002)
13
14 Phase separation in the headers is possible for this design. Methods do not exist for rigorously predicting the extent of
15 phase separation in the headers, but the thermal performance may be overpredicted for such cases. (MN 2008)
16
17 Geometry, Mechanical Design, and Vibration
18 The design has parallel-cut baffles and the reported height under the nozzle lowers the bundle below the baffle cut.
19 Unrestricted longitudinal flow can bypass the bundle. This bypass region can be reduced by decreasing the height under
20 the nozzle, changing the baffle cut, or adding sealing arrangements. (MN 3505)
21
22 WARNING-prevention of tube ends erosion at the inlet needs to be considered in accordance with TEMA
23 recommendation when an axial inlet nozzle is used, when liquid Rho-V-squared exceeds 6000 lb/ft s2 (8928 kg/m s2) or
24 when there is two-phase flow at the inlet. (MN 3205)
25
26 The outlet nozzle velocity is greater than the tube exit velocity where momentum pressure drop between the tube exit
27 and the outlet nozzle is not included in the calculations. This pressure drop can be significant in a vacuum condenser.
28 Ensure you have margin for this additional pressure loss. (MN 3224)
29
30 A tubecount has been specified and the program has generated a tube layout that tries to matches the specified
31 tubecount. The user should review the tube layout drawing to assure that it is valid and as intended by the user. If the
32 generated tube layout drawing in not as intended, the user should make geometry changes, use the inputs provided on
33 the Tube Layout input panel or use the "Use tube layout drawing as input" option until the tube layout drawing better
34 matches the actual tubecount. (MN 3018)
35
36 The outlet baffle spacing is less than the calculated minimum outlet spacing 10.875 in. ( 276 mm) using estimated
37 nozzle clearance requirements. This could result in the last baffle being placed beneath or beyond the outlet nozzle. This
38 geometry is not recommended. (MN 3037)
39
40 ASME Section VIII Div. 1 Code was used to ESTIMATE all pressure vessel dimensions and weights. The dimensions in
41 this report cannot be used to fabricate the vessel. (MN 10170)
42
43 Shell Inlet Nozzle: Outside Diameter is Less Than Inside Diameter - I.D. will be used / O.D. will be ignored (MN 10137)
44
45 Specified inlet channel nozzle thickness does not meet internal pressure thickness requirements - reinforcement
46 calculations aborted. (MN 10122)
47
48 Specified outlet channel nozzle thickness does not meet internal pressure thickness requirements - reinforcement
49 calculations aborted. (MN 10123)
50
Runtime Messages
Page 46
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Unit ID 102 - WARNING MESSAGES (CALCULATIONS CONTINUE)
2
3 Geometry, Mechanical Design, and Vibration (cont.)
4 Tube-to-Baffle Clearance = 0.8 mm (0.03150 in) Exceeds TEMA Recommended 0.8 mm (0.03125 in). (MN 10042)
5
6 Fluid Properties
7 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the hot fluid at isobar no. 1 around increment
8 no. 13. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty,
9 and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100 Btu/lb). Check
10 the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
(MN 5091)
11
12 A negative latent heat has been calculated for the hot fluid at isobar no. 1 around increment no. 17. Using specific
13 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
14 the total incremental duty. These operations produced a negative value. Check the specified heat release curve, liquid
15 and vapor specific heats, and enthalpy values; rerun the case. (MN 5010)
16
17 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the hot fluid at isobar no. 2 around increment
18 no. 10. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty,
19 and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100 Btu/lb). Check
20 the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
(MN 5091)
21
22 A negative latent heat has been calculated for the hot fluid at isobar no. 2 around increment no. 17. Using specific
23 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
24 the total incremental duty. These operations produced a negative value. Check the specified heat release curve, liquid
25 and vapor specific heats, and enthalpy values; rerun the case. (MN 5010)
26
27 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the hot fluid at isobar no. 3 around increment
28 no. 10. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty,
29 and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100 Btu/lb). Check
30 the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
(MN 5091)
31
32 A negative latent heat has been calculated for the hot fluid at isobar no. 3 around increment no. 17. Using specific
33 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
34 the total incremental duty. These operations produced a negative value. Check the specified heat release curve, liquid
35 and vapor specific heats, and enthalpy values; rerun the case. (MN 5010)
36
37 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the cold fluid at isobar no. 1 around
38 increment no. 16. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible
39 liquid duty, and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100
40 Btu/lb). Check the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
41 (MN 5090)
42
43 A negative latent heat has been calculated for the cold fluid at isobar no. 1 around increment no. 3. Using specific
44 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
45 the total incremental duty. These calculations produced a negative value. Check the specified heat release curve, liquid
46 and vapor specific heat, and enthalpy values; rerun the case. (MN 5051)
47
48 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the cold fluid at isobar no. 2 around
49 increment no. 16. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible
50 liquid duty, and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100
Runtime Messages
Page 47
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Unit ID 102 - WARNING MESSAGES (CALCULATIONS CONTINUE)
2
3 Fluid Properties (cont.)
4 Btu/lb). Check the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
5 (MN 5090)
6
7 A negative latent heat has been calculated for the cold fluid at isobar no. 2 around increment no. 3. Using specific
8 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
9 the total incremental duty. These calculations produced a negative value. Check the specified heat release curve, liquid
10 and vapor specific heat, and enthalpy values; rerun the case. (MN 5051)
11
12 An excessive latent heat >2556 kj/kg (1100 BTU/lb) has been calculated for the cold fluid at isobar no. 3 around
13 increment no. 16. Using specific heats, the program calculates the incremental sensible vapor duty and the sensible
14 liquid duty, and subtracts them from the total incremental duty. The latent heat has been limited to 2556 kj/kg (1100
15 Btu/lb). Check the specified heat release curve, liquid and vapor specific heat, and enthalpy values; rerun the case.
16 (MN 5090)
17
18 A negative latent heat has been calculated for the cold fluid at isobar no. 3 around increment no. 3. Using specific
19 heats, the program calculates the incremental sensible vapor duty and the sensible liquid duty, and subtracts them from
20 the total incremental duty. These calculations produced a negative value. Check the specified heat release curve, liquid
21 and vapor specific heat, and enthalpy values; rerun the case. (MN 5051)
22
23 The physical properties of the hot fluid have been extrapolated beyond the valid temperature range. Check the
24 calculated values. The thermal analysis requires properties at bulk and skin/wall temperatures. (MN 5033)
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
Final Results
Page 48
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
Process Data
Cold Shellside
Hot Tubeside
2 Fluid name
3 Fluid condition
4 Total flow rate
5 Weight fraction vapor, In/Out
6 Temperature, In/Out
7 Skin temperature, Min/Max
8 Wall temperature, Min/Max
9 Pressure, In/Average
10 Pressure drop, Total/Allowed
11 Velocity, Mid/Max allow
12 Boiling range/Mole fraction inert
13 Average film coef.
14 Heat transfer safety factor
15 Fouling resistance
CHPS Liquid
Boil. Liquid
33.906
0.0049
154.02
170.04
173.87
13.950
2.100
HDF RX Effluent
Cond. Vapor
36.403
0.0823
0.0752
191.93
129.00
107.79
181.44
98.42
175.79
161.91
161.54
0.734
2.100
5.00
0.0000
1665.8
1.0000
0.000300
(1000-kg/hr)
(--)
(Deg C)
(Deg C)
(Deg C)
(kgf/cm2A)
(kgf/cm2)
(m/s)
(Deg C)
(kcal/m2-hr-C)
(--)
(m2-hr-C/kcal)
16
(kcal/m2-hr-C)
(MM kcal/hr)
(Deg C)
(Deg C)
39 Type
40 Crosspasses/shellpass
41 Central spacing
42 Inlet/Outlet Spacing
43 Turn Spacing
44 Baffle thickness
45 Insulated long baffle
46 Use deresonating baffles
47
48 Tube type
49 Length to tangent
50 Effective length
51 Total tubesheet
52 Area ratio
53 Tube metal
245.31 /
1.7820 /
49.4
51.6 *
345.13
0.9956
/
257.22
* 0.9621
1734.4
330.5
Shell Construction Information
30 TEMA shell type
DFU
31 Shells Series
1 Parallel
32 Passes Shell
2 Tube
33 Shell orientation angle (deg)
0.00
34 Impingement present
Rods
35 Pairs seal strips
3
36 Shell expansion joint
No
37 Weight estimation Wet/Dry/Bundle
38
2566.2
660.10
1.0000
0.000400
Overall Performance Data
17 Overall coef., Reqd/Clean/Actual
18 Heat duty, Calculated/Specified
19 Effective overall temperature difference
20 EMTD = (MTD) * (DELTA) * (F/G/H)
21
22
23 See Runtime Messages Report for
24 warnings.
25
26
Exchanger Fluid Volumes
27 Approximate shellside (L)
28 Approximate tubeside (L)
29
0.0023
60.00
88.87
95.22
14.233
0.566
0.80
1
2
Shell ID
Total area
Eff. area
(mm)
(m2)
(m2/shell)
710.00
152.25
146.97
Impingement rod rows
2
Passlane seal rods (mm) 0.000 No. 0
UBend tangent to Support Dist. (mm) 40.000
14133 /
12069 /
5712.2 (kg/shell)
Baffle Information
Parallel Single-Seg.
27
(mm)
198.00
(mm)
727.00
(mm)
198.00
(mm)
4.762
No
No
Baffle cut (% dia) 27.23
No. (Pct Area)
(mm) to C.L
1
21.72
161.67
2
0.00
0.000
Long. baffle length
(mm)
5677.
Tube Information
Plain
(mm)
6086.
(mm)
5875.
(mm)
171.00
(out/in)
1.9676
SA-213 T22
Tubecount per shell
Pct tubes removed (both)
Outside diameter
(mm)
Wall thickness
(mm)
Pitch (mm)
25.400 Ratio
Tube pattern (deg)
418
7.52
19.050
4.684
1.3333
45
Final Results
Page 49
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
Shellside Performance
2 Nom vel, X-flow/window
0.81 / 0.74
3
4 Flow fractions for vapor phase
5
A=0.2253 B=0.5555 C=0.0554 E=0.1638
6
7
Shellside Heat Transfer Corrections
8
9
Total
0.987
Beta
0.920
Cross
78.56
MOMENTUM
Window
13.96
10
11
12
13
Gamma
1.072
Fin
1.000
Ends
5.93
0.14
Nozzle
Inlet
Outlet
Shell
0.75
0.66
Tube
3.36
1.90
Two-Phase Parameters
Method
RPM
PP/TBR
18
Inlet
Shear
Conv
Center
Shear
Conv
H. T. Parameters
19 Overall wall correction
20 Midpoint
Prandtl no.
21 Midpoint
Reynolds no.
22 Bundle inlet
Reynolds no.
23 Bundle outlet
Reynolds no.
24 Fouling layer
(mm)
25
50
Outlet
Shear
Conv
Mix F
0.7855
Shell
Tube
3044
1036
3716
5432
7277
3780
Thermal Resistance, %
26
Shell
Tube
Fouling
27
38.97
30.38
25.47
28 Total fouling resistance
(m2-hr-C/kcal)
29 Differential resistance
(m2-hr-C/kcal)
30
Shell Nozzles
31 Inlet at channel end
32 Nozzle location at U-bend
33
34
35 Number at each position
36 Diameter
(mm)
37 Velocity
(m/s)
38 Pressure drop
(kgf/cm2)
39 Height under nozzle
(mm)
40 Nozzle R-V-SQ
(kg/m-s2)
41 Shell ent.
(kg/m-s2)
42
43
44
Tube Nozzle
45 Diameter
(mm)
46 Velocity
(m/s)
47 Pressure drop
(kgf/cm2)
48 Nozzle R-V-SQ
(kg/m-s2)
49
Annular Distributor
51 Length
52 Height
53 Slot area
Metal
5.18
Over Des
4.85
9.90e-4
1.89e-4
Yes
After U-bend
Inlet
1
131.78
1.45
4.23e-3
54.980
1004.1
246.52
Outlet
1
131.78
1.78
3.76e-3
91.849
1226.5
132.02
Inlet
RADIAL
131.78
5.94
0.025
4401.8
Outlet
RADIAL
131.78
5.27
0.014
3909.3
Inlet
Outlet
Liquid
Outlet
0
Liquid
Outlet
(mm)
(mm)
(mm2)
54
55
56
End
0.949
Pressure Drops (Percent of Total)
14
15
16
17
F=0.0000
Diametral Clearances (mm)
Baffle-to-shell
4.8000
Bundle-to-shell
20.194
Tube-to-baffle
0.8000
Supplementary Results
Page 50
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
Externally Enhanced Tube Geometry
2 Type
3 Fin density
4 Fin height
5 Fin thickness
6 Root diameter
7 Area/length
8
Plain
None
(mm)
(L/D)
Mean Metal Temperatures
10 Mean shell temperature
11 Tubesheet temperature
12
13
14
15
16
Type
Thickness
Pitch
(fin/meter)
(mm)
(mm)
(mm)
(m2/m)
9
Internally Enhanced Tube Geometry
109.73 (C)
343.00 (C)
Mean tube metal temperature in each tubepass, (C)
Tube Pass
1
2
Inside
157.95
118.60
Outside
155.49
115.71
Radial
156.45
116.84
Vibration Analysis
Page 51
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Shellside condition
Boil. Liquid
2 Axial stress loading
(kg/mm2)
0.000
Added mass factor
3 Beta
4.217
4
Position In The Bundle
Inlet
Center
5 Length for natural frequency
(mm)
925.
396.
6 Length/TEMA maximum span
(--)
0.607
0.260
7 Number of spans
(--)
14
14
8 Tube natural frequency
(Hz)
89.1 +
264.9
9 Shell acoustic frequency
(Hz)
10
Flow Velocities
Inlet
Center
11 Window parallel velocity
(m/s)
0.52
0.57
12 Bundle crossflow velocity
(m/s)
0.14
0.60
13 Bundle/shell velocity
(m/s)
0.56
0.62
14
Fluidelastic Instability Check
Inlet
Center
15 Log decrement
HTRI
0.102
0.091
16 Critical velocity
(m/s)
7.49
40.34
17 Baffle tip cross velocity ratio
(--)
0.0203
0.0157
18 Average crossflow velocity ratio
(--)
0.0254
0.0196
19
Acoustic Vibration Check
Inlet
Center
20 Vortex shedding ratio
(--)
21 Chen number
(--)
22 Turbulent buffeting ratio
(--)
23
Tube Vibration Check
Inlet
Center
24 Vortex shedding ratio
(--)
0.050
0.210
25 Parallel flow amplitude
(mm)
0.000
0.000
26 Crossflow amplitude
(mm)
0.001
0.000
27 Tube gap
(mm)
6.350
6.350
28 Crossflow amplitude/tube gap
(--)
1.14e-4
6.25e-5
29 Crossflow RHO-V-SQ
(kg/m-s2)
17.22
269.68
30
Bundle Entrance/Exit
31
(analysis at first tube row)
Entrance
32 Fluidelastic instability ratio
(--)
0.020
33 Vortex shedding ratio
(--)
0.053
34 Crossflow amplitude
(mm)
0.00080
35 Crossflow velocity
(m/s)
0.15
36 Tubesheet to inlet/outlet support
(mm)
None
37
Shell Entrance/Exit Parameters
Entrance
38 Impingement device
Rods
39 Flow area
(m2)
0.028
40 Velocity
(m/s)
0.72
41 Critical velocity
(m/s)
7.49
42 RHO-V-SQ
(kg/m-s2)
246.52
43 Shell type
DFU
Baffle type
44 Tube type
Plain
Baffle layout
45 Pitch ratio
1.3333
Tube diameter, (mm)
46 Layout angle
45
Tube material
47 Number U-Bend supports
2
Elastic modulus, (kg/mm2)
48 Use deresonating baffles
No
Supports/baffle space
49
Program Messages
50 + Natural or acoustic frequency used in vibration analysis.
51 See help for additional information.
52 * Items with asterisk exceed a conservative lower limit for vibration-free design.
53 Review your case using the procedure described in Online Help;
54 You may find that a vibration problem is unlikely.
55
56
MKH Units
1.394
Outlet
925.
0.607
14
89.9
Outlet
0.63
0.18
0.18
Outlet
0.091
7.71
0.0241
0.0302
Outlet
Outlet
0.062
0.000
0.001
6.350
1.39e-4
21.04
Exit
0.024
0.065
0.00098
0.18
None
Exit
-0.042
0.58
7.71
132.02
Single-Seg.
Parallel
19.050
SA-213 T22
20770
HEAT EXCHANGER RATING DATA SHEET
Page 52
1
Released to the following HTRI Member Company:
2
MKH Units
TEMA INDIA
3
4
5 Service of Unit Reactor Effluent / CHPS Liquid Exchanger
Item No.
6 Type
DFU
Orientation Horizontal
Connected In
1 Parallel
1 Series
7 Surf/Unit (Gross/Eff)
152.25 / 146.97 m2
Shell/Unit 1
Surf/Shell (Gross/Eff)
152.25 / 146.97 m2
8
PERFORMANCE OF ONE UNIT
9 Fluid Allocation
Shell Side
Tube Side
10 Fluid Name
CHPS Liquid
HDF RX Effluent
11 Fluid Quantity, Total
1000-kg/hr
33.906
36.403
12 Vapor (In/Out)
wt%
0.23
0.49
8.23
7.52
13 Liquid
wt%
99.77
99.51
91.77
92.48
14 Temperature (In/Out)
C
60.00
154.02
191.93
129.00
kg/m3
15 Density
2.6400 V/L 803.20 3.9413 V/L 749.82 12.198 V/L 728.46 12.716 V/L 771.40
cP
16 Viscosity
0.0110 V/L 5.5770 0.0150 V/L 1.1347 0.0133 V/L 0.9301 0.0120 V/L 1.8883
kcal/kg-C
17 Specific Heat
1.4710 V/L 0.5060 0.9883 V/L 0.6041 2.3625 V/L 0.6667 2.5320 V/L 0.6010
kcal/hr-m-C
18 Thermal Conductivity
0.0830 V/L 0.0840 0.0791 V/L 0.0741 0.2322 V/L 0.1084 0.2090 V/L 0.1180
kgf/cm2A
19 Critical Pressure
kgf/cm2A
20 Inlet Pressure
14.233
161.91
m/s
21 Velocity
0.80
5.00
kgf/cm2
22 Pressure Drop, Allow/Calc
2.100
0.566
2.100
0.734
kcal/m2-hr-C
23 Average Film Coefficient
660.10
1665.8
m2-hr-C/kcal
24 Fouling Resistance (min)
0.000400
0.000300
1.7820 MM kcal/hr
25 Heat Exchanged
MTD (Corrected)
49.4 C
Overdesign
4.85 %
245.31 kcal/m2-hr-C
26 Transfer Rate, Service
Calculated
257.22 kcal/m2-hr-C Clean
345.13 kcal/m2-hr-C
27
CONSTRUCTION OF ONE SHELL
Sketch (Bundle/Nozzle Orientation)
28
Shell Side
Tube Side
29 Design Pressure
kgf/cm2G
130.50
169.60
30 Design Temperature
C
289.00
343.00
31 No Passes per Shell
2
2
32 Flow Direction
Upward
Downward
Connections
33
In
mm
1
@ 131.78
1
@ 131.78
Size &
34
Out
mm
1
@ 131.78
1
@ 131.78
Rating
35
Liq. Out mm
@
1
@
OD 19.050 mm
36 Tube No. 418.00
Thk(Avg) 4.684
mm
Length 6086. mm Pitch 25.400 mm
Tube pattern 45
Pairs seal strips
37 Tube Type Plain
Material SA-213 T22
3
Passlane Seal Rod No.
38 Shell ID
710.00 mm
Kettle ID
mm
0
Impingement Plate
39 Cross Baffle Type
Parallel
Single-Seg.
%Cut (Diam) 27.23
Rods
No. of Crosspasses
40 Spacing(c/c)
198.00 mm
Inlet
727.00 mm
27
Shell Exit
41 Rho-V2-Inlet Nozzle 1004.1
kg/m-s2
Shell Entrance
246.52 kg/m-s2
132.02 kg/m-s2
Bundle Exit
42
Bundle Entrance
10.83 kg/m-s2
13.23 kg/m-s2
43 Weight/Shell
12069
kg
Filled with Water
14133 kg
Bundle
5712.2 kg
44 Notes:
Thermal Resistance, %
Velocities, m/s
Flow Fractions
45
Shell
38.97 Shellside
0.80 A
0.225
46
Tube
30.38 Tubeside
5.00 B
0.556
47
Fouling
25.47 Crossflow
0.81 C
0.055
48
Metal
5.18 Window
0.74 E
0.164
0.000
F
49
HEAT EXCHANGER SPECIFICATION SHEET
Page 53
1
Released to the following HTRI Member Company:
MKH Units
2
TEMA INDIA
3
Job No.
4
Gujarat Refinery, IOCL
Reference No.
5 Customer
Vadodara, Gujarat
Proposal No.
6 Address
Lupech Project
Date
7/21/2023
Rev
7 Plant Location
Reactor Effluent / CHPS Liquid Exchanger
Item No.
8 Service of Unit
710 x 6086
mm
Type
DFU
Horizontal
Connected In
1
Parallel
1 Series
9 Size
152.25 / 146.97 m2
Shell/Unit
1
Surf/Shell (Gross/Eff)
152.25 / 146.97 m2
10 Surf/Unit (Gross/Eff)
PERFORMANCE OF ONE UNIT
11
Shell Side
Tube Side
12 Fluid Allocation
CHPS Liquid
HDF RX Effluent
13 Fluid Name
kg/hr
33906
36403
14 Fluid Quantity, Total
77.306
166.35
2996.7
2737.2
15 Vapor (In/Out)
33829
33740
33406
33666
16 Liquid
17 Steam
18 Water
19 Noncondensables
C
60.00
154.02
191.93
129.00
20 Temperature (In/Out)
0.8036
0.7502
0.7288
0.7718
21 Specific Gravity
cP
0.0110 V/L 5.5770 0.0150 V/L 1.1347 0.0133 V/L 0.9301 0.0120 V/L 1.8883
22 Viscosity
23 Molecular Weight
24 Molecular Weight, Noncondensables
kcal/kg-C
1.4710 V/L 0.5060
0.9883 V/L 0.6041 2.3625 V/L 0.6667 2.5320 V/L 0.6010
25 Specific Heat
kcal/hr-m-C
0.0830 V/L 0.0840
0.0791 V/L 0.0741 0.2322 V/L 0.1084 0.2090 V/L 0.1180
26 Thermal Conductivity
kcal/kg
611.11
320.33
535.23
593.29
27 Latent Heat
kgf/cm2A
14.233
161.91
28 Inlet Pressure
m/s
0.80
5.00
29 Velocity
kgf/cm2
2.100
0.566
2.100
0.734
30 Pressure Drop, Allow/Calc
m2-hr-C/kcal
0.000400
0.000300
31 Fouling Resistance (min)
1781956 kcal/hr
MTD (Corrected)
49.4
C
32 Heat Exchanged
245.31 kcal/m2-hr-C
Clean 345.13 kcal/m2-hr-C
Actual
257.22 kcal/m2-hr-C
33 Transfer Rate, Service
CONSTRUCTION OF ONE SHELL
Sketch (Bundle/Nozzle Orientation)
34
Shell Side
Tube Side
35
kgf/cm2G
130.50 /
169.60 /
36 Design/Test Pressure
C
289.00
343.00
37 Design Temperature
2
2
38 No Passes per Shell
mm
4.500
4.500
39 Corrosion Allowance
Connections
In
mm
1 @ 131.78
1 @ 131.78
40
Size &
Out
mm
1 @ 131.78
1 @ 131.78
41
Rating
Intermediate
@
@
42
OD 19.050 mm
Thk(Avg) 4.684 mm
Length 6086.
mm
Pitch 25.400 mm
43 Tube No. 209U
Material SA-213 T22
Tube pattern45
44 Tube Type Plain
SA-387 GR 22 CL 2
ID 710.00 OD 792.55 mm Shell Cover
SA-387 GR 22 CL 2
(Integ.)
45 Shell
SA-336 F22 CL 3
Channel Cover SA-336 F22 CL 3
46 Channel or Bonnet
SA-336 F22 CL 3
Tubesheet-Floating
47 Tubesheet-Stationary
Impingement Plate Rods
48 Floating Head Cover
SA-387 GR 22 CL 2
Type Single-Seg.
%Cut (Diam) 27.23 Spacing(c/c) 198.00
Inlet 727.00 mm
49 Baffles-Cross
Seal Type Lamiflex
50 Baffles-Long
U-Bend
Type Full support
51 Supports-Tube
3
pairs seal strips
Tube-Tubesheet Joint Expanded and strength welded
52 Bypass Seal Arrangement
Type
None
53 Expansion Joint
1004.1 kg/m-s2
Bundle Entrance
10.83 Bundle Exit
13.23
kg/m-s2
54 Rho-V2-Inlet Nozzle
Tube Side
Mach. Mtl. (Kammprofile\Flex. Face)
55 Gaskets-Shell Side Mach. Mtl. (Kammprofile\Flex. Face)
- Floating Head
56
TEMA Class
R
57 Code Requirements ASME
12069
kg
Filled with Water
14133 kg
Bundle
5712.2
kg
58 Weight/Shell
59 Remarks:
60
61
62
Reprinted with Permission
63
U-Bend Schedule
Page 54
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
Number of Straight
Bend
Total
1
Tubes
Length
Diameter Length
Row
2 (-)
(-)
mm
mm
mm
3
1
19
6086.0
76.200
12292
4
2
18
6086.0
112.12
12348
5
3
19
6086.0
148.04
12405
6
4
18
6086.0
183.96
12461
7
5
17
6086.0
219.88
12517
8
6
18
6086.0
255.81
12574
9
7
17
6086.0
291.73
12630
10
8
16
6086.0
327.65
12687
11
9
15
6086.0
363.57
12743
12 10
16
6086.0
399.49
12800
13 11
15
6086.0
435.41
12856
14 12
14
6086.0
471.33
12912
15 13
13
6086.0
507.25
12969
16 Total
215
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
MKH Units
Input Reprint
Page 58
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Exchanger Data
2 Unit identifier
3 Service type
4 TEMA type
5 Run mode
6 Hot fluid location
7 Unit orientation
8 Number of shells in series
9 Number of shells in parallel
10 Flow in 1st tubepass
11 Train flow direction
12
13 Construction Data
14 Shell material
15 Tube material
16 Shell cover material
17 Channel or bonnet material
18 Tubesheet-Stationary material
19 Baffle-Cross material
20 Shellside gasket
21 Tubeside gasket
22 Shellside design pressure
23 Tubeside design pressure
24 Shellside vacuum pressure
25 Tubeside vacuum pressure
26 Shellside design temperature
27 Tubeside design temperature
28 Shellside corrosion allowance
29 Tubeside corrosion allowance
30 Tubesheet design temperature
31 Shellside radiography
32 Tubeside radiography
33 TEMA class
34 Small exchanger
35 Shell outside diameter
36 Shell inside diameter
37 Shell wall thickness
38 Front head outside diameter
39 Front head inside diameter
40 Front head thickness
41 Rear head outside diameter
42 Rear head inside diameter
43 Rear head thickness
44 Total tubesheet thickness
45 Double tubesheet
46 Shell expansion joint
47 Suppress mechanical calculations
48
49
50
Shell 2
Generic shell and tube
DFU
Rating
Tubeside
Horizontal
1
1
Countercurrent
Countercurrent
SA-387 GR 22 CL 2
SA-213 T22
SA-387 GR 22 CL 2
SA-387 22 2 Pl. K21590
SA-182 F22 Forgings K21590
SA-387 GR 22 CL 2
Mach. Mtl. (Kammprofile\Flex. Face)
Mach. Mtl. (Kammprofile\Flex. Face)
130.50 kgf/cm2G
169.60 kgf/cm2G
Full
Full
289.00 C
343.00 C
4.500 mm
4.500 mm
343.00 C
Full
Full
R
No
792.55 mm
710.00 mm
41.275 mm
811.60 mm
710.00 mm
50.800 mm
805.25 mm
710.00 mm
47.625 mm
171.00 mm
No
No
No
Input Reprint
Page 59
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Tube Data
2 Tube type
3 Tube outside diameter
4 Tube wall thickness
5 Tube pitch
6 Tube pitch ratio
7 Tubepasses per shell
8 Tube pattern
9 Number of tubes per shell
10 Tube count method
11 Tube length
12 Tube material
13
14 Baffle Data
15 Baffle type
16 Baffle orientation
17 Baffle cut percent
18 Adjust baffle cut
19 Double segmental set center baffle at inlet
20 Number of crosspasses
21 Central baffle spacing
22 Inlet/outlet spacing
23 Variable baffle spacing
24 Window cut from baffles
25 Use deresonating baffles
26
27 Supports Data
28 Full support at U-Bend
29 Support distance to U-bend tangent
30 Number of U-bend supports
31 Include inlet vibration support
32 Include outlet vibration support
33
34 Longitudinal Baffle Data
35 Insulated longitudinal baffle
36 Seal type
37
38
39
40
41
42
43
44
45
46
47
48
49
50
Plain
19.050 mm
4.684 mm
25.400 mm
1.333
2
45 degrees
418.00
Rigorous
6086. mm
SA-213 T22
Single segmental
Parallel
27.230 % shell ID
No adjustment
Program set
27
198.00 mm
727.00 mm
No
No
No
Full support
40.000 mm
2
No
No
No
Lamiflex
Input Reprint
Page 60
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Nozzle Data
2 Shellside
3 Nozzle standard
4 Shell entrance type
5 Shell exit type
6
7 Nozzle outside diameter
8 Nozzle schedule
9 Nozzle inside diameter
10 Number at this position
11 Tubeside
12 Nozzle standard
13
14 Nozzle outside diameter
15 Nozzle schedule
16 Nozzle inside diameter
17 Number at this position
18
19 Nozzle Location Data
20 Radial position on shell inlet nozzle
21 Radial position on shell outlet nozzle
22 Location of nozzle at U-bend
23 Tubeside entry type
24 Tubeside inlet position
25 Tubeside exit type
26
27 Impingement Data
28 Impingement type
29 Use tube positions to place rods
30 Impingement rod rows
31 Impingement rod diameter
32 Impingement rod pitch
33 Impingement rods on centerline
34 Impingement rod layout angle
35 Rod row width to nozzle diameter
36
37 Tube Layout Data
38 Pass partition construction
39 Force symmetric layout
40 Force continuous cleaning lanes
41 Force uniform layout
42 Align across primary passlanes
43 Fill knock out area with dummy tubes
44 Fill bundle periphery with dummy tubes
45 Fill passlanes with dummy tubes
46 Shifted staggered layout
47 Use crossed U-bends
48 Minimum U-bend diameter
49 Use tube layout drawing as input
50
01-ANSI_B36_10.TABLE
Use impingement device
Remove tubes if TEMA requires
Inlet
Outlet Liq. Outlet
114.30
168.28
-- mm
STD
STD
-131.78
131.78
-- mm
1
1
--
Inlet
168.28
STD
131.78
1
01-ANSI_B36_10.TABLE
Outlet Liq. Outlet
168.28
-- mm
STD
-131.78
-- mm
1
--
Program decides
Program decides
After U-bend
Radial
Front head
Same as inlet
Rods
No
2
20.000 mm
25.400 mm
Yes
45.00 deg
1.7870
Program set
Yes
No
No
No
Program set
Program set
Program Set
Program set
No
76.200 mm
No
Input Reprint
Page 61
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Clearance Data
2 Number of seal strip pairs
3 Block A stream
4 Block E stream
5 Block F stream
6 Number of passlane seal rods
7 Tubes to remove for tie rods
8 Number of tie rods
9 Tie rod outside diameter
10 Tube to baffle clearance
11 Baffle to shell clearance
12 Bundle to shell clearance
13 Baffle clearance type
14
15 Process Conditions Data
16 Phase condition
17 Flow rate
18 Inlet temperature
19 Outlet temperature
20 Inlet pressure
21 Allowable pressure drop
22 Duty multiplier
23
24 Process Fouling Data
25 Fouling resistance
26
27 Control Name Data
28 Case name
29 Service
30 Customer
31 Address
32 Plant
33
34 Control Methods Data
35 Shellside friction factor method
36 Tubeside friction factor method
37 Pure longitudinal flow
38 Pure component condensation
39 Condensing correlation
40 Mole fraction inerts
41 Momentum exclusion
42 Perform shellside subcooling calculations
43 Pure component boiling
44 Check film boiling
45 Nucleate boiling method
46 Component boiling method
47 Reduced pressure calculation method
48 Increments per baffle
49
50
3
No
No
No
Calculated
1
12
12.700 mm
0.800 mm
4.800 mm
20.190 mm
TEMA
Hot Fluid
Two phase
36.403
-129.00
161.91
2.100
Cold Fluid
Two phase
33.906 1000-kg/hr
60.00 C
-- C
14.233 kgf/cm2A
2.100 kgf/cm2
1.0000
Hot Fluid
0.0003
Cold Fluid
0.0004 m2-hr-C/kcal
70N-SOR
Reactor Effluent / CHPS Liquid Exchanger
Gujarat Refinery, IOCL
Vadodara, Gujarat
Lupech Project
Commercial
Commercial
No
No
HTRI Proration
0.0000
0.0000 %
No
No
Yes
Physical property/theoretical boiling range
Convective
Program decides
Calculated
Input Reprint
Page 62
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1 Control User-Defined Methods Data
2 Add non-nucleate boiling
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
Yes
Drawings
Page 55
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
710
mm
6086
mm
Unit
TEMA type
Shell diameter
Tube length
Dry weight
Wet weight
Bundle weight
Shell 2
DFU
710
6086
12069
14133
5712
mm
mm
kg/shell
kg/shell
kg/shell
Total tube inlet nozzles
Total tube outlet nozzles
Total shell inlet nozzles
Total shell outlet nozzles
1
1
1
1
Stream ID
Stream name
Flow (total), 1000-kg/hr
Pressure drop, kgf/cm2
Temperature, C
Wt. fraction vapor
Pressure, kgf/cm2A
Shellside
CHPS Liquid
33.906
0.566
60.00
154.02
0.0023
0.0049
14.233
13.668
Tubeside
HDF RX Effluent
36.403
0.734
191.93
129.00
0.0823
0.0752
161.91
161.18
Drawings
Page 56
Released to the following HTRI Member Company:
TEMA INDIA
Xist 9 (64 bit) 7/21/2023 9:21 SN: 00381-1148883897
MKH Units
70N-SOR : Shell 2
Rating - Horizontal Multipass Flow TEMA DFU Shell With Single-Segmental Baffles
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
Unit
TEMA type
Shell ID
Actual OTL
Height under inlet nozzle
Rows of impingement rods
Impingement rod OD
Height under outlet nozzle
Tube type
Tube OD
Tube pitch
Tube layout angle
Tubes
Tube positions available
Tie rods
Seal strip pairs
Tube Passes
Parallel passlane width
Baffle cut % diameter
131.78 mm
TUBEPASS DETAILS
Pass
Rows Tubes
1
13
215
2
13
215
SYMBOL LEGEND
Tube
Dummy Short Tube
Dummy Long Tube
Plugged Tube
Tie Rod
Seal Rod
Impingement Rod
1
131.78 mm
2
Shell 2
DFU
710.00 mm
689.81 mm
54.980 mm
2
20.000 mm
91.849 mm
Plain
19.050 mm
25.400 mm
45 deg
418
430
12
3
2
57.150 mm
27.23