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