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65,115 x 1.20
10 Vapor
(in/out)
kg/h 17,406 x 1.20
65,115 x 1.20
65,115 x 1.20
49,551 x 1.20
11 Liquid
kg/h 47,709 x 1.20
15,564 x 1.20
12 Steam
kg/h
13 Water
kg/h
1
of
7
1 Customer
Shandong Yuhuang Chemical Co. Ltd.
Equipment Tag No.
E-3201
2 Plant Location
Dongming County, Shandong, China
Manufacturer
3 Service of Unit
OCT Reactor Feed/Effluent Exchanger
Rev
0
1
2
3
4
5
Date/ By
10/01/10
MS 11/26/10 MS
Chkd/Appr
SSAX
JLH/RIH SSAX JLH/RIH
CONFIDENTIAL
Lummus Technology Bloomfield, NJ USA
Always Refer To This Number
21250A
3.75 (Note 3)
3.75 (Note 3)
32 Design Temperature, Min./Max.
°C
375 (Note 3)
375 (Note 3)
33 No. of Passes Per Shell
34 Corrosion Allowance
mm
1.5
1.5
35 Connections,
SI3
Sheet
4
of
7
1 Customer
Shandong Yuhuang Chemical Co. Ltd.
Equipment Tag No.
E-3201
2 Plant Location Dongming County, Shandong, China
3 Service of Unit OCT Reactor Feed/Effluent Exchanger 4 NOTES (CONTINUED):
5 10. TUBE SIDE cooling curve at the inlet pressure for the End-of-Life case is below:
6
7
Enthalpies
Crit Temp - TC
Crit Press - PC
8
Temp Pr
OCT Reactor Feed/Effluent Exchanger
NOTES:
SI3 Equipment Tag No.
Sheet
3 of
7
E-3201
9. Diagram for the exchanger layout is as follows:
Rev
0
1
2
3
4
5
Date/ By
10/01/10
MS 11/26/10 MS
Chkd/Appr
SSAX
JLH/RIH SSAX JLH/RIH
CONFIDENTIAL
Lummus Technology Bloomfield, NJ USA
Always Refer To This Number
21250A
Div.
Job
PO/Req.
Sup.
DATA SHEET - SHELL AND TUBE HEAT EXCHANGER
Gaskets
48 Expansion Joint
Type
49 Code Requirements
ASME-VIII
Code Stamp (Yes/No)
TEMA Class
R
50 Weights/Shell - Shipping
kg , Filled W/ Water
kg ,Bundle
kg
51 REMARKS:
14 Noncondensable
kg/h
15 Temperature
(in/out)
°C
49.8
281.7
345.5
69.1
16 Density (Liquid/Vapor)
kg/m³ 481.0
57.11
31.02
23.94
469.3
54.09
17 Viscosity, (Liquid/Vapor)
52
53 Rev
0
1
2
3
4
5
54 Date/ By
10/01/10
MS
11/26/10
MS
55 Chkd/Appr
SSAX
JLH/RIH
SSAX
JLH/RIH
CONFIDENTIAL
A109 06 1282-TP2.1-1 (SI) Rev. 4A
Lummus Technology Bloomfield, NJ USA
Div.
Job PO/Req.
Sup.
DATA SHEET - SHELL AND TUBE HEAT EXCHANGER
Customer
Shandong Yuhuang Chemical Co. Ltd.
Plant Location
Dongming County, Shandong, China
Service of Unit
Type
CES (Note 6,8)
Horizontal
Vertical
4 Size
Connected In
Parallel
Series
5 Surface/Unit
Gros s
Eff.
m²
Shell/Unit 1 (Note 6) Surface/Shell (Gross)(Eff),
m²
6
PERFORMANCE OF ONE UNIT
Water
Total
Vapor
Liquid
Vapor
Liquid
9
°C MPa abs MkJ/h
MkJ/h
MkJ/h
MkJ/h
°C
°C MPa Abs. MPa Abs.
10
345.5
2.96
70.58
0.00
0.00
0.00
75.6
4.60
11
315.8
2.96
65.33
0.00
0.00
5.25
In
36 Size &
Out
37 Rating
Intermediate
38 Tube No.
O.D.
mm
Thk (Min/Avg)
mm Length
m Pitch, mm
39 Tube Type
Welded
Seamless
Material CS (Note 5)
40 Shell
CS (Note 5)
Lummus Technology Bloomfield, NJ USA
Always Refer To This Number
21250A
Div.
Job
PO/Req.
Sup.
DATA SHEET - SHELL AND TUBE HEAT EXCHANGER
SI3
CASE - DESIGN EOL
Sheet
Case Description: DESIGN EOL
7 Fluid Allocation
Shell Side
Tube Side
8 Fluid Circulated
REACTOR FEED
REACTOR EFFLUENT
9 Fluid Quantity Total
kg/h
65,115 x 1.20
8. Helical baffle-type exchanger by Lummus Heat Transfer Inc. preferred. Helixchanger heat exchangers can be obtained directly from the global network of qualified licensee fabricators.
4.60
16
152.0
2.96
39.08
0.00
0.00
31.50
75.6
4.60
17
116.1
2.96
33.83
0.00
0.00
36.75
3. Dry-out conditions are 80 °C and 0.7 MPaG.
4. Insulation required is:
Shell – “Hot”
Tube– “Hot”
5. The requirements of paragraph UCS-66 of ASME Section VIII Division I shall apply for all carbon steel materials.
pV²
44 Baffles (Cross)
Type
%Cut
(Dia./Area) SPACING
c/c
45 Baffles (Long)
Seal Type
46 Supports - Tube
U-Bend
Type
47 Bypass Seal Arrangement
Tube/Tubesheet Joint
mPa·s 0.084
0.012
0.017
0.018
0.078
0.012
18 Molecular Weight,
Vapor
33.04
40.74
40.90
39.07
19 Molecular Weight,
Noncondensable
20 Specific Heat,(Liquid/Vapor)
kJ/kg·°C 3.010
6. TEMA Type and number of shell indicated is preliminary. Final selection to be confirmed during detailed engineering.
7. For removable bundles, the maximum bundle weight to be no more than 50 tons with maximum shell diameter of 1800 mm and tube length no more than 9000 mm.
75.6
4.60
12
285.2
2.96
60.08
0.00
0.00
10.50
75.6
4.60
13
253.6
2.96
54.83
0.00
0.00
15.75
75.6
4.60
14
220.9
2.96
49.58
0.00
0.00
21.00
75.6
4.60
15
187.0
2.96
44.33
0.00
0.00
26.25
75.6
I.D.
O.D.
Shell Cover
(Integ.)(Remov.)
41 Channel or Bonnet
Channel Cover
42 Tubesheet - Stationary
Tubesheet - Floating
43 Floating Head Cover
Impingement Protection
Always Refer To This Number
21250A
Div.
Job PO/Req.
Sup.
DATA SHEET - SHELL AND TUBE HEAT EXCHANGER
SI3
Customer Plant Location
Shandong Yuhuang Chemical Co. Ltd. Dongming County, Shandong, China
2.283
2.594
2.752
3.191
2.298
21 Thermal Conductivity, (Liq/Vap)
W/m·°C 0.0910 0.0225
0.0533
0.0629 0.0886
0.0233
22 Latent Heat
kJ/kg @
°C
23 Inlet Pressure
MPa Ga (MPaa)
Equipment Tag No.
Service of Unit
OCT Reactor Feed/Effluent Exchanger
NOTES:
1. Flows and duties are specified for the End-of-Life Case.
Sheet
2 of
7
E-3201
2. Provide 20% overdesign on flows and 20% overdesign on duties specified on data sheet.
3.35
2.86
24 Velocity,
m/s
25 Press. Drop (Allow./Calc.)
MPa
0.07/
0.07/
26 Fouling Resist. (Min.)
m²·°C·/W
0.00027
0.00027
27 Heat Exchanged
MkJ/h
47.25 x 1.20
MTD Corrected
°C
28 Transfer Rate
W/m²·°C
Service
Clean
Design
29
CONSTRUCTION OF ONE SHELL
Sketch
30
Shell Side
Tube Side
(Bundle/Nozzle Orientation)
31 Design Pressure,
MPa Ga (MPaa)