Appendix 8.5
Equipment Summary & Specification Sheets
59
REACTORS, COLUMNS & VESSELS
EQUIPMENT NR. :
NAME
:
Pressure [bara]
Temp.
[oC]
Volume [m3]
Diameter [m]
L or H [m]
:
:
:
:
:
R101
Monolith
Reactor
1.9 / 2
596 / 600
71
3
10
R102
Riser
Regenerator
1/2
84 / 682 (2)
3.0
0.9
15
–
SUMMARY
C101
Depropanizer
C104
De-ethanizer
C105
P-P splitter
Tray Column
16.8 / 16.7
47.4 / 89.2
Tray Column
24.2 / 24
- 62.1 / 60.9
Tray Column
10.0 / 11.0
19.0 / 30.4
0.9
18.0
1.0
19.8
1.98+1.98
(3)
39.6+36.6
(3)
Internals
Sieve Trays
Sieve Trays
Sieve Trays
n.a.
- Tray Type
: n.a.
119
29
26
n.a.
- Tray Number : n.a.
Monolith
n.a.
- Fixed Packing
n.a.
n.a.
n.a.
Type
: Honeycomb
n.a.
n.a.
n.a.
Shape
: 400 cpsi
n.a.
- Catalyst
n.a.
n.a.
n.a.
Type
: Pt-Sn-K/γAl2O3
n.a.
n.a.
n.a.
Shape
:
Number
2 (3)
1
1
- Series
:
- Parallel
:
Trays: SS314
Trays: SS314 Trays: SS314
Materials of
Column: CS
Column: CS
Column: CS
Construction (1) :
Remarks:
(1) SS = Stainless Steel; CS = Carbon Steel
(2) Temperatures of incoming air and outgoing effluent. The temperature of incoming solids is 596oC.
(3) The P-P splitter is split in two towers
Project ID-Number :
Date
:
CPD3300
January 12th 2004
60
REACTORS, COLUMNS & VESSELS
EQUIPMENT NR. :
NAME
:
Pressure [bara]
Temp.
[oC]
Volume [m3]
Diameter [m]
L or H [m]
Internals
:
:
:
:
:
V101
Reflux
accumulator
C101
Horizontal
16.2
47.4
63.62 (1)
3.0
9.0
V102
Flash vessel
for water
separation
Horizontal
12.0
30
5.18 (1)
1.3
3.9
n.a.
- Tray Type
: n.a.
n.a.
- Tray Number : n.a.
- Fixed Packing
n.a.
Type
: n.a.
n.a.
Shape
: n.a.
- Catalyst
n.a.
Type
: n.a.
n.a.
Shape
: n.a.
Number
1
1
- Series
:
- Parallel
:
CS
SS
Materials of
Construction (2) :
Remarks:
(1) Effective volume for residence time of 10 minutes.
(2) SS = Stainless Steel; CS = Carbon Steel
–
SUMMARY
V103
Reflux
accumulator
of C104
Horizontal
23.8
-62
49.1 (1)
2.5
10.0
V104
Reflux
accumulator
of C105
Horizontal
10.0
19
341.0 (1)
5.3
15.8
n.a.
n.a.
n.a.
n.a.
n.a.
n.a.
n.a.
n.a.
n.a.
n.a.
n.a.
n.a.
1
CS
1
CS
Project ID-Number :
Date
:
CPD3300
January 12th 2004
61
HEAT EXCHANGERS
SUMMARY
E-101
E-102
E-103
E-104
E-105
C101
Condenser
Heat
exchanger
Heat
exchanger
Heat
exchanger
C101
Reboiler
Floating Head
Floating Head
Floating Head
Floating Head
Floating Head
Cooling W.
n-C3
4617
Exhaust air
n-C3
7022
n-C3/C3=/H2O
n-C3
4898
n-C3/C3=
n-C3
3050
n-C3/C3=/H2O
n-C4/n-C3
10607
921
1419
424
2262
1184
1
-
2
-
1
-
3
-
1
-
16.7
3.0
2.2
1.0
2.2
1.55
2.2
25.0
1.55
16.8
20.0/37.0
47.0/47.0
Tubes : Brass
Shell : CS
Praat geen
poep
682.2/70.9
60.9/248.2
Tubes : Brass
Shell : CS
595.9/498.3
248.2/378.9
Tubes : Brass
Shell : CS
70.9/46.6
-20.4/60.9
Tubes : Brass
Shell : CS
394.5/183.3
89.2/89.2
Tubes : Brass
Shell : CS
EQUIPMENT NR. :
NAME
:
Substance
- Tubes
:
- Shell
:
Duty
[kW] :
Heat Exchange
area
[m2] :
Number
- Series
:
:
- Parallel
Pressure
[bara]
- Tubes
:
- Shell
:
Temperature
In / Out
[oC]
- Tubes
:
- Shell
:
Special Materials of
Construction (2) :
Other
:
–
Remarks:
(1) Bare tube surface.
(2) SS = Stainless Steel;
CS = Carbon Steel.
Project ID-Number :
Date
:
CPD3300
January 12st 2004
62
HEAT EXCHANGERS
SUMMARY
E-106
E-107
E-108
E-109
E-110
Heat
exchanger
C104
Reboiler
C104
Reboiler
Heat
exchanger
R101 effluent
cooler
Floating Head
Floating Head
Floating Head
Floating Head
Floating Head
n-C3/C3=/H2O
n-C3/C3=
5212
n-C3/C3=/H2O n-C3/C3=/H2O
n-C3/C3=
n-C3/C3=
4191
12611
n-C3/C3=/H2O
Light ends
89
n-C3/C3=/H2O
Cooling W.
3271
288
1151
4619
20
668
1
-
1
-
5
-
1
-
1
-
1.55
25
1.55
25.0
12.2
25.0
12.2
2.2
12.2
3.0
498.3/394.5
60.9/100.0
Tubes : Brass
Shell : CS
183.3/100.0
60.9/60.9
Tubes : Brass
Shell : CS
225.0/70.9
60.9/60.9
Tubes : Brass
Shell : CS
70.9/69.8
-62.5/15.0
Tubes : Brass
Shell : CS
69.8/29.9
20/40
Tubes : Brass
Shell : CS
EQUIPMENT NR. :
NAME
:
Substance
- Tubes
:
- Shell
:
Duty
[kW] :
Heat Exchange
area
[m2] :
Number
- Series
:
- Parallel
:
Pressure
[bara]
- Tubes
:
- Shell
:
Temperature
In / Out
[oC]
- Tubes
:
- Shell
:
Special Materials of
Construction (2) :
Other
:
Remarks:
–
(3) Bare tube surface.
(4) SS = Stainless Steel;
CS = Carbon Steel.
Project ID-Number :
Date
:
CPD3300
January 12st 2004
63
HEAT EXCHANGERS
SUMMARY
E-111
E-112
E-113
E-114
E-115
C104
Reboiler
C104 feed
cooler
C104
Condenser
Heat pump
Reboiler
Heat pump
trim cooler
Floating Head
Floating Head
Floating Head
Floating Head
Floating Head
n-C3/C3=
n-C3/C3=
456
n-C3/C3=
Cooling W.
2073
Refrig. (N2)
Light ends
5135 (3)
n-C3/C3=
n-C3/C3=/C4+
39702
C3=
Cooling W.
8871
927
736
?
4393
3088
1
-
1
-
?
5
-
3
-
25.2
25.0
46.6/30.0
20.0/37.0
?
24.0
18.0
11.0
17.0
3.0
74.5/69.0
60.9/60.9
Tubes : Brass
Shell : CS
25.2
3.0
Tubes : Brass
Shell : SS
<-72.0
-62.0/-62.0
Tubes : Brass
Shell : CS
54.0/43.0
11.0/11.0
Tubes : Brass
Shell : CS
43.0/29.5
19.5/33.0
Tubes : Brass
Shell : CS
EQUIPMENT NR. :
NAME
:
Substance
- Tubes
:
- Shell
:
Duty
[kW] :
Heat Exchange
area
[m2] :
Number
- Series
:
:
- Parallel
Pressure
[bara]
- Tubes
:
- Shell
:
Temperature
In / Out
[oC]
- Tubes
:
- Shell
:
Special Materials of
Construction (2) :
Other
:
Remarks:
–
1. Bare tube surface.
2. SS = Stainless Steel;
CS = Carbon Steel.
3. Cost estimation based on energy consumption ($/MJ)
Project ID-Number :
Date
:
CPD3300
January 12st 2004
64
HEAT EXCHANGERS
SUMMARY
E-116
E-117
E-118
Exhaust air
cooler
C4+ cooler
C104 Reboiler
Floating Head
Floating Head
Thermosyphon
Exhaust Air
Cooling W.
357
C4+
Cooling W.
? (Small)
n-C3/C3=
L.P.
5349
50
? (Small)
183
1
-
1
-
1
-
1.2
3.0
16.8
3.0
25.0
3.0
70.9/39.9
20.0/40.0
Tubes : Brass
Shell : CS
89.0/15.0
?
Tubes : Brass
Shell : CS
60.9/60.9
190.0/133.5
Tubes : Brass
Shell : CS
EQUIPMENT NR. :
NAME
:
Substance
- Tubes
:
- Shell
(1) :
Duty
[kW] :
Heat Exchange
area
[m2] :
Number
- Series
:
:
- Parallel
Pressure
[bara]
- Tubes
:
- Shell
:
Temperature
In / Out
[oC]
- Tubes
:
- Shell
:
Special Materials of
Construction (2) :
Other
:
Remarks:
–
1. L.P. = Low pressure steam
2. SS = Stainless Steel;
CS = Carbon Steel.
Project ID-Number :
Date
:
CPD3300
January 12st 2004
65
PUMPS & COMPRESSORS
P-101
P-102
C101 Reflux
pump
Centrifugal
2
Bottom C102
n-C3
TEG/water
EQUIPMENT NR. :
NAME
:
Type
:
Number
:
Medium
transferred
:
Capacity
[kg/s]
:
[m3/s]
:
Density [kg/m3] :
Pressure [bara]
Suct. / Disch.
:
Temperature
In / Out [oC]
:
Power
[kW]
- Theor.
:
- Actual
:
Number
- Theor.
:
- Actual
:
Special Materials of
Construction
:
Other
:
–
SUMMARY
P104
P-103
Bottom C103 Bottom C105
Centrifugal
2
n-C3
C104 Reflux
pump
Centrifugal
2
n-C3 / Light
ends
Centrifugal
2
TEG
P106
Centrifugal
2
133.4
427
?
?
?
?
6.67
0.014
469
10.4
?
?
16.2/18.0
?
?
11.0/20.0
24.8/25.0
47.0/47.0
?
?
30.0/30.0
-62.0/-62.0
6.81
?
?
?
?
13.52
3.46
(1)
2
2
(1)
MS casing
Double
mechanical
seals
2
(1)
MS casing
Double
mechanical
seals
2
MS casing
Double
mechanical
seals
(1)
MS casing
Double
mechanical
seals
2
(1)
MS casing
Double
mechanical
seals
Remarks:
(1) One installed spare included.
Project ID-Number :
Date
:
CPD3300
January 12st 2004
66
PUMPS & COMPRESSORS
EQUIPMENT NR. :
NAME
:
Type
:
Number
:
Medium
transferred
:
Capacity
[kg/s]
:
[m3/s]
:
Density [kg/m3] :
Pressure [bara]
Suct. / Disch.
:
Temperature
In / Out [oC]
:
Power
[kW]
- Theor.
:
- Actual
:
Number
- Theor.
:
- Actual
:
Special Materials of
Construction
:
Other
:
LPG feed
pump
Centrifugal
2
Discharge
V102 pump
Centrifugal
2
C3=
SUMMARY
P110
P-109
P-108
P-107
C105 Reflux
pump
Centrifugal
2
–
Water
K101
Bottom C101 R101effluent
compressor
Centrifugal
Centrifugal
2
1
LPG
C4+
n-C3/C3=/H2O
9.71
0.019
502
0.39
0.0007
579
19.0
8.8/1.9
2.2/9.9
123
0.25
501
3.29
0.0038
980
10.0/10.5
12.0/15.0
17.0/20.0
16.8/20.0
1.55/12.2
19.0/19.0
30.0/30.0
15.0/15.0
89.0/89.0
100.0/225.0
14.43
0.17
1.68
0.23
4857
2
(1)
MS casing
Double
mechanical
seals
2
(1)
MS casing
Double
mechanical
seals
2
(1)
MS casing
Double
mechanical
seals
2
(1)
MS casing
Double
mechanical
seals
1
MS casing
Double
mechanical
seals
Remarks:
(1) One installed spare included.
Project ID-Number :
Date
:
CPD3300
January 12st 2004
67
PUMPS & COMPRESSORS
SUMMARY
K102
K103
K104
T101
T102
C102
Overhead
compressor
Centrifugal
1
C105
Overhead
compressor
Centrifugal
1
Air
compressor
Expander
overhead
C101
Expander
Bottom C104
n-C3/C3=
C3=
Air
n-C3
n-C3/C3=
13.55
11.25/7.33
1.205/1.85
16.0
0.44/3.64
36.8/4.39
15.35
0.37/0.69
44.51/22.12
EQUIPMENT NR. :
NAME
:
Type
:
Number
:
Medium
transferred
:
Capacity
[kg/s]
:
3
[m /s]
:
3
Density [kg/m ] :
Pressure [bara]
Suct. / Disch.
:
Temperature
In / Out [oC]
:
Power
[kW]
- Theor.
:
- Actual
:
Number
- Theor.
:
- Actual
:
Special Materials of
Construction
:
Other
:
–
Centrifugal
1
15.66
0.68/0.35
22.9/44.5
134.0
6.45/3.75
20.77/35.78
11.8/25.2
10.0/18.0
1.0/2.35
16.2/2.2
24.0/13.0
30.0/75.0
19.0/54.0
15.0/102.0
47.0/-20.0
100.0/75.0
873
5301
1197
-1101
-391
1
1
1
1
1
MS casing
Double
mechanical
seals
MS casing
Double
mechanical
seals
MS casing
Double
mechanical
seals
MS casing
Double
mechanical
seals
MS casing
Double
mechanical
seals
Remarks:
Project ID-Number :
Date
:
CPD3300
January 12st 2004
68
PUMPS & COMPRESSORS
EQUIPMENT NR. :
NAME
:
Type
:
Number
:
Medium
transferred
:
Capacity
[kg/s]
:
[m3/s]
:
Density [kg/m3] :
Pressure [bara]
Suct. / Disch.
:
Temperature
In / Out [oC]
:
Power
[kW]
- Theor.
:
- Actual
:
Number
- Theor.
:
- Actual
:
Special Materials of
Construction
:
Other
:
–
SUMMARY
T103
Expander
propylene
product
Centrifugal
1
C3=
8.68
0.42/0.46
20.7/18.7
10.0/9.0
19.0/15.0
-32
1
MS casing
Double
mechanical
seals
Remarks:
Project ID-Number :
Date
:
CPD3300
January 12st 2004
69
DISTILLATION COLUMN – SPECIFICATION SHEET
EQUIPMENT NUMBER :
NAME
:
Service
Column Type
Tray Type
Tray Number (1)
- Theoretical
- Actual
- Feed (actual)
Tray Distance (HETP) [m]
Column Diameter
[m]
Column Height
[m]
Heating
Stream Details
Temp.
[oC]
Pressure
[bara]
Density
[kg/m3]
Mass Flow [kg/s]
Composition
Propylene
Propane
Ethane
1-Butene
Butane
C101
Depropanizer
General Data
: - distillation
: - tray
: - sieve
:
:
:
:
:
:
:
12
26
14
0.6
Tray Material
0.9
Column Material
18
- reboiler (3)
Process Conditions
:
:
SS314
CS
(2)
(2)
Feed
:
21.7
:
17
: 489
:
16.4
mol% wt%
0.6
0.6
96.2
96.0
1.2
1.8
0.2
0.2
1.8
1.4
Trays
(4)
Number of sieve holes
Active Tray Area
Weir Length
Diameter of
chute pipe / hole /
Top
Bottom
Reflux
:
47.4
:
89.2
:
47.4
:
16.7
:
16.8
:
16.7
:
37
: 436
:
37
: 15.8
:
0.4
:
16.0
mol% wt% mol% wt% mol% wt%
0.0
0.0
0.6
0.6
16.2
20.2
97.6 98.1
0.0
0.0
1.3
1.8
9.0
8.8
0.0
0.0
74.8
71.0
0.0
0.0
Column Internals
Packing
Not Applicable
: …
Type
:
2
[m ] : …
Material
:
[mm] : 0.77
Volume [m3] :
Length [m] :
Width
[m] :
[mm] : …
Height [m] :
Remarks:
(1) Tray numbering from top to bottom.
(2) SS = Stainless Steel;
CS = Carbon Steel.
(3) Reboiler is E105; can operate with LP steam but also as heat exchanger.
(4) Tray layout valid for whole column.
Project ID-Number :
Date
:
CPD3300
January 12th 2004
70
HEAT EXCHANGER – SPECIFICATION SHEET
EQUIPMENT NUMBER :
NAME
:
Service
E-101
C-101 Overhead Condenser
General Data
: Condenser
Type
:
Floating Head
Position
:
Horizontal
Capacity
Heat Exchange Area
Overall Heat Transfer Coefficient
Log. Mean Temperature Diff. (LMTD)
[kW]
[m2]
[W/m2⋅oC]
[oC]
Passes Tube Side
Passes Shell Side
Correction Factor LMTD (min. 0.75)
Corrected LMTD
In Series
In Parallel
:
:
:
:
4617
921
300
16.9
:
:
4
2
:
:
1
none
: 0.99
[oC]
: 16.7
Process Conditions
Medium
:
Shell Side
Propane/Ethane
Tube Side
Water
Mass Stream
Mass Stream to
- Condense
Average Specific Heat
Heat of Evap. / Condensation
[kg/s]
:
31.81
63.62
[kg/s]
[kJ/kg⋅oC]
[kJ/kg]
:
:
:
15.81
-
3.279
-
Temperature IN
Temperature OUT
[oC]
[oC]
:
:
47
47
20.0
37.0
Pressure
Material
[bara]
:
:
16.2
CS (1)
3.0
SS (1)
292
Remarks:
1. SS = Stainless Steel;
CS = Carbon Steel.
Project ID-Number :
Date
:
CPD3300
January 12th 2004
71
HEAT EXCHANGER – SPECIFICATION SHEET
EQUIPMENT NUMBER :
NAME
:
Service
E-118
C-104 Reboiler
General Data
: Reboiler
Type
:
Thermosyphon
Position
:
Vertical
Capacity
Heat Exchange Area
Overall Heat Transfer Coefficient
Log. Mean Temperature Diff. (LMTD)
[kW]
[m2]
[W/m2⋅oC]
[oC]
Passes Tube Side
Passes Shell Side
Correction Factor LMTD (min. 0.75)
Corrected LMTD
:
:
:
:
:
:
In Series
In Parallel
:
:
1
none
5349
183
300
97.3
-
:
1.0
[ C]
:
97.3
Process Conditions
o
Medium
:
Shell Side
LP steam
Tube Side
Propane / Propylene
Mass Stream
Mass Stream to
- Evaporize
- Condense
[kg/s]
:
5.34
24.71
[kg/s]
[kg/s]
:
:
5.34
24.71
-
Average Specific Heat
Heat of Evap. / Condensation
[kJ/kg⋅oC]
[kJ/kg]
:
:
1.88
2200
798.0
Temperature IN
Temperature OUT
[oC]
[oC]
:
:
190.0
133.5
61.7 (2)
61.9 (2)
Pressure
Material
Remarks:
[bara]
:
:
4.0
SS (1)
25
CS (1)
(1) SS = Stainless Steel;
CS = Carbon Steel.
(2) Actual temperature change is zero since propane/propylene evaporates
Project ID-Number :
Date
:
CPD3300
January 12th 2004
72
HEAT EXCHANGER – SPECIFICATION SHEET
EQUIPMENT NUMBER :
NAME
:
Service
E-115
Heat pump trim cooler
General Data
: Heat Exchanger
Type
:
Floating Head
Position
:
- Horizontal
Capacity
Heat Exchange Area
Overall Heat Transfer Coefficient
Log. Mean Temperature Diff. (LMTD)
[kW]
[m2]
[W/m2⋅oC]
[oC]
Passes Tube Side
Passes Shell Side
Correction Factor LMTD (min. 0.75)
Corrected LMTD
In Series
In Parallel
:
:
:
:
8871
3088
300
10.2
:
:
4
2
:
:
1
none
:
0.94
[oC]
:
9.59
Process Conditions
Medium
:
Shell Side
Cooling water
Tube Side
Propylene
Mass Stream
Mass Stream to
- Evaporize
- Condense
[kg/s]
:
156.62
156.62
[kg/s]
[kg/s]
:
:
-
Average Specific Heat
Heat of Evap. / Condensation
[kJ/kg⋅oC]
[kJ/kg]
:
:
4.18
-
4.75
-
Temperature IN
Temperature OUT
[oC]
[oC]
:
:
19.5
33.0
Pressure
Material
[bara]
:
:
3.0
SS (1)
(1)
43.0
30.0
17.0
SS (1)
Remarks:
(1) SS = Stainless Steel;
CS = Carbon Steel.
Project ID-Number :
Date
:
CPD3300
January 12st 2004
73
CENTRIFUGAL PUMP – SPECIFICATION SHEET
EQUIPMENT NUMBER : P109
Operating : 1
NAME
: C101 LPG Pump
Installed Spare : 1
Service : LPG Transfer pump
Type
: Centrifugal
Number : 1
Operating Conditions & Physical Data
Pumped liquid
: LPG
Temperature
(T)
[oC]
:
15
3
[kg/m ] : 502
Density
( ρ)
[N⋅s/m2] : 2*10-8
Viscosity
(η)
Vapour Pressure
(pv) [bara]
:
17
at Temperature [oC] : 15
Power
Capacity
(Φv) [m3/s]
: 0.019
Suction Pressure
(ps) [bara]
: 17
Discharge Pressure
(pd) [bara]
: 19.7
Theoretical Power
[kW]
Pump Efficiency
Power at Shaft
[-]
[kW]
RPM
Drive
Type electrical motor
Tension
Rotational direction
Foundation Plate
[V]
Flexible Coupling
Pressure Gauge Suction
Pressure Gauge Discharge
Min. Overpressure above
pv/pm
[bar]
Pump House
Pump Rotor
Shaft
Special provisions
:
5.13
{ = Φv⋅( pd - ps)⋅102 }
: 0.71
: 1.7
Construction Details (1)
: 3500
Nominal diameter
: Electrical
Suction Nozzle
[…]
Discharge Nozzle […]
:
: 380
Cooled Bearings
: Clock
Cooled Stuffing Box
Smothering Gland
: Combined /
If yes
: Yes
- Seal Liquid
: No
- Splash Rings
: Yes
- Packing Type
- Mechanical Seal
: 0.1
- N.P.S.H.
[m]
Construction Materials (2)
: MS
Wear Rings
: HT Steel
Shaft Box
: HT Steel
: none
Operating Pressure
[bara] : 17.3
Test Pressure
Remarks:
(1) Double mechanical seals required to prevent any leakage; single-stage pump
(2) MS = Mild Steel; HT Steel = High Tensile Steel
Project ID-Number :
Date
:
:
:
:
:
:
:
:
:
:
:
No
No
Yes
Yes
Yes / No
Yes
3.7
:
:
[bara] :
CPD3300
January 12th 2004
74
COMPRESSOR
– SPECIFICATION SHEET
EQUIPMENT NUMBER : K103
NAME
: C105 Overhead compressor
Service : Heat pump gas compressor
Type
: Centrifugal, polytropic
Number : 1
Operating Conditions & Physical Data
Pumped liquid
: Propylene
Temperature In / Out (T)
[oC]
:
19.0 / 54
Capacity
Pressure In
Discharge Pressure
(Φv)
(pd)
3
[m /s]
[bara]
[bara]
:
:
:
Operating : 1
Installed Spare : 1
Power
6.45
10
18
Actual Power
[kW]
: 5301
Efficiency
[-]
: 0.73
Construction Material
Construction material
:
CS
Remarks:
Project ID-Number :
Date
:
CPD3300
January 12th 2004
75
VESSEL – SPECIFICATION SHEET
EQUIPMENT NUMBER :
NAME
:
R101
Reactor
In Series
In Parallel
:
Type
: Monolith
Position
: Vertical
Internals
Heating/Cooling medium
- Type
- Quantity
- Press./Temp.’s
Vessel Diameter (ID)
Vessel Height
Vessel Tot. Volume
Vessel Material
Other
:
:
:
:
:
:
:
:
:
:
Honeycomb monolith
none
n.a.
n.a.
n.a.
3
10
71
SS
(2)
Downward solid and gas flow through honeycomb
monolith
Process Conditions
Gas Feed
Stream Data
1
none
General Data
Reaction
Service
[kg/s]
[bara/oC]
[m]
[m]
[m3]
:
:
Temperature
[oC]
Pressure
[bara]
3
Solid Feed
Bottom
Effluent
378.9
676
596
2
-
1.9
Density
[kg/m ]
1.62
6689
98.9
Mass Flow
[kg/s]
16.0
2179
2195
Composition
mol%
wt%
mol%
wt%
mol%
wt%
0.46
0.36
0.00
0.00
0.00
0.00
Propylene
0.35
0.26
0.00
0.00
0.98
0.98
Propane
0.01
0.04
0.00
0.00
0.00
0.00
Hydrogen
0.17
0.32
0.00
0.00
0.00
0.00
Water
0.00
0.00
0.00
0.00
0.00
0.00
Methane
0.01
0.01
0.00
0.00
0.02
0.02
Ethane
0.00
0.00
0.00
0.00
0.00
0.00
Ethylene
0.00
0.00
0.00
0.00
0.00
0.00
1-Butene
0.00
0.00
0.00
0.00
0.00
0.00
Butane
0.00
0.01
0.00
0.00
0.00
0.00
Carbon monoxide
1.00
1.00
0.00
0.00
SOC
(1)
0.93
0.92
0.00
0.00
0.00
0.00
Spent SOC
(1)
0.07
0.08
Remarks: (1) SOC and Spent SOC fractions are solid phase fractions
(2) SS = Stainless Steel
Project ID-Number : CPD3300
Date
: January 12st 2004
76
VESSEL – SPECIFICATION SHEET
EQUIPMENT NUMBER :
NAME
:
Service
R102
Riser regenerator
General Data
: Reaction
Type
: Riser reactor
Position
: Vertical
Internals
Heating/Cooling medium
- Type
- Quantity
- Press./Temp.’s
Vessel Diameter (ID)
Vessel Height
Vessel Tot. Volume
Vessel Material
Other
:
:
:
:
:
:
:
:
:
:
[kg/s]
[bara/oC]
[m]
[m]
[m3]
In Series
In Parallel
1
none
Open
none
n.a.
n.a.
n.a.
0.9
15
9.53
SS
(2)
Upward bound solid and gas flow.
Process Conditions
Gas Feed
Stream Data
:
:
Solid Feed
Top Effluent
Temperature
[oC]
102
593
682
Pressure
[bara]
2.35
-
1.35
Density
[kg/m3]
0.064
6689
72.52
Mass Flow
[kg/s]
14
2176
2190
Composition
mol%
wt%
mol%
wt%
mol%
wt%
0.00
0.00
0.00
0.00
0.00
0.00
Propylene
0.00
0.00
0.00
0.00
0.00
0.00
Propane
0.00
0.00
0.00
0.00
0.00
0.00
Hydrogen
0.00
0.00
0.00
0.00
0.00
0.00
Water
0.01
0.01
0.00
0.00
0.23
0.21
Oxygen
0.99
0.99
0.00
0.00
0.77
0.79
Nitrogen
0.00
0.00
0.00
0.00
0.00
0.00
Butane
0.00
0.00
0.00
0.00
0.00
0.00
Carbon monoxide
SOC
(1)
1.00
1.00
0.93
0.92
0.00
0.00
Spent SOC
(1)
0.00
0.00
0.07
0.08
0.00
0.00
Remarks: (1) SOC and Spent SOC fractions are solid phase fractions
(2) SS = Stainless Steel
Project ID-Number : CPD3300
Date
: January 12st 2004
77
CYCLONE – SPECIFICATION SHEET
EQUIPMENT NUMBER : S101
NAME
: Reactor effluent separator
Service : Gas-Solid separation
Type
: High Flowrate Stairmand cyclone
Number : 2
Operating Conditions & Physical Data
Gas
Solid
Gas flowrate
Particle size
:
:
:
:
:
:
19.0
21.9
0.866
2176
0.279
60
Design pressure drop
Characteristic velocity
[Pa]
[m/s]
:
:
1500
8.47
Temperature
Operation pressure
Cyclone diameter
Cyclone height
Particle cut size
[oC]
[bara]
[m]
[m]
[µm]
:
:
:
:
:
596
1.9
1.01
4.04
6.21
:
0.99 (1)
Efficiency
2
1
: Propane/Propylene/Water/Carbonmonoxide
: SOC/ Spent SOC
[kg/s]
[m3/s]
[kg/m3]
[kg/s]
[m3/s]
[µm]
Gas density
Solid flowrate
Operating
:
Installed Spare :
Construction Material
Construction material
:
CS
Remarks:
(1) Remaining solids separated by additional filter
Project ID-Number :
Date
:
CPD3300
January 12th 2004
78