Appendix 8.5 Equipment Summary & Specification Sheets

Transcription

1 Appendix 8.5 Equipment Summary & Specification Sheets 59

2 EQUIPMENT NR. : NAME : REACTORS, COLUMNS & VESSELS SUMMARY R0 Monolith Reactor R02 Riser Regenerator C0 Depropanizer C04 Deethanizer C05 PP splitter Tray Column Tray Column Tray Column Pressure [bara] :.9 / 2 / / / /.0 Temp. [ o C] : 596 / / 682 (2) 47.4 / / / 30.4 Volume [m 3 ] : Diameter [m] : L or H [m] : Internals Tray Type : Tray Number : Fixed Packing Type : Shape : Catalyst Type : Shape : Number Series : Parallel : Materials of Construction () : Monolith Honeycomb 400 cpsi PtSnK/γAl 2 O Sieve Trays Sieve Trays (3) (3) Sieve Trays 9 2 (3) Trays: SS34 Column: CS Trays: SS34 Trays: SS34 Column: CS Column: CS () SS = Stainless Steel; CS = Carbon Steel (2) Temperatures of incoming air and outgoing effluent. The temperature of incoming solids is 596 o C. (3) The PP splitter is split in two towers Project IDNumber : CPD3300 Date : January 2th

3 EQUIPMENT NR. : NAME : REACTORS, COLUMNS & VESSELS SUMMARY V0 Reflux accumulator C0 V02 Flash vessel for water separation V03 Reflux accumulator of C04 V04 Reflux accumulator of C05 Horizontal Horizontal Horizontal Horizontal Pressure [bara] : Temp. [ o C] : Volume [m 3 ] : Diameter [m] : L or H [m] : Internals Tray Type : Tray Number : Fixed Packing Type : Shape : Catalyst Type : Shape : Number Series : Parallel : Materials of Construction (2) : () () () () CS SS CS CS () Effective volume for residence time of 0 minutes. (2) SS = Stainless Steel; CS = Carbon Steel Project IDNumber : CPD3300 Date : January 2th

4 HEAT EXCHANGERS SUMMARY EQUIPMENT NR. : NAME : E0 C0 Condenser E02 Heat exchanger E03 Heat exchanger E04 Heat exchanger E05 C0 Reboiler Substance Tubes : Shell : Floating Head Floating Head Floating Head Floating Head Floating Head Cooling W. nc 3 Exhaust air nc 3 nc 3 /C 3 =/H 2 O nc 3 nc 3 /C 3 = nc 3 Duty [kw] : Heat Exchange area [m 2 ] : Number Series : Parallel : Pressure [bara] Tubes : Shell : Temperature In / Out [ o C] Tubes : Shell : / /47.0 Special Materials of Construction (2) : Other : Praat geen poep / /248.2 () Bare tube surface. (2) SS = Stainless Steel; CS = Carbon Steel / / / /60.9 nc 3 /C 3 =/H 2 O nc 4 /nc / /89.2 Project IDNumber : CPD3300 Date : January 2 st

5 HEAT EXCHANGERS SUMMARY EQUIPMENT NR. : NAME : E06 Heat exchanger E07 C04 Reboiler E08 C04 Reboiler E09 Heat exchanger E0 R0 effluent cooler Substance Tubes : Shell : Floating Head Floating Head Floating Head Floating Head Floating Head nc 3 /C 3 =/H 2 O nc 3 /C 3 = nc 3 /C 3 =/H 2 O nc 3 /C 3 = nc 3 /C 3 =/H 2 O nc 3 /C 3 = nc 3 /C 3 =/H 2 O Light ends Duty [kw] : Heat Exchange area [m 2 ] : Number Series : Parallel : Pressure [bara] Tubes : Shell : Temperature In / Out [ o C] Tubes : Shell : Special Materials of Construction (2) : Other : / / / /60.9 (3) Bare tube surface. (4) SS = Stainless Steel; CS = Carbon Steel / / / /5.0 nc 3 /C 3 =/H 2 O Cooling W / /40 Project IDNumber : CPD3300 Date : January 2 st

6 HEAT EXCHANGERS SUMMARY EQUIPMENT NR. : NAME : E C04 Reboiler E2 C04 feed cooler E3 C04 Condenser E4 Heat pump Reboiler E5 Heat pump trim cooler Substance Tubes : Shell : Floating Head Floating Head Floating Head Floating Head Floating Head nc 3 /C 3 = nc 3 /C 3 = nc 3 /C 3 = Cooling W. Refrig. (N 2 ) Light ends nc 3 /C 3 = + nc 3 /C 3 =/C 4 Duty [kw] : (3) Heat Exchange area [m 2 ] : ? Number Series : Parallel : Pressure [bara] Tubes : Shell : Temperature In / Out [ o C] Tubes : Shell : Special Materials of Construction (2) : Other : / / / / Shell : SS?? Bare tube surface. 2. SS = Stainless Steel; CS = Carbon Steel. 3. Cost estimation based on energy consumption ($/MJ) < / /4.0/.0 C 3 = Cooling W / /3 Project IDNumber : CPD3300 Date : January 2 st

7 HEAT EXCHANGERS SUMMARY EQUIPMENT NR. : NAME : E6 Exhaust air cooler E7 C 4 + cooler E8 C04 Reboiler Substance Tubes : Shell () : Floating Head Floating Head Thermosyphon C 4 + nc 3 /C 3 = L.P. Exhaust Air Cooling W. Cooling W. Duty [kw] : 357? (Small) 5349 Heat Exchange area [m 2 ] : 50? (Small) 83 Number Series : Parallel : Pressure [bara] Tubes : Shell : Temperature In / Out [ o C] Tubes : Shell : Special Materials of Construction (2) : Other : / / /5.0? L.P. = Low pressure steam 2. SS = Stainless Steel; CS = Carbon Steel. 60.9/ /33.5 Project IDNumber : CPD3300 Date : January 2 st

8 PUMPS & COMPRESSORS SUMMARY EQUIPMENT NR. : P0 P02 P03 P04 P06 NAME : C0 Reflux pump Bottom C02 Bottom C03 Bottom C05 C04 Reflux pump Type : Centrifugal Centrifugal Centrifugal Centrifugal Centrifugal Number : Medium transferred : nc 3 TEG/water TEG nc 3 nc 3 / Light ends Capacity [kg/s] : [m 3 /s] : 33.4?? 0.04? Density [kg/m 3 ] : 427?? 469? Pressure [bara] Suct. / Disch. : 6.2/8.0??.0/ /25.0 Temperature In / Out [ o C] : 47.0/47.0?? 30.0/ /62.0 Power [kw] Theor. :?? Actual : 6.8?? Number Theor. : Actual : 2 () 2 () 2 () 2 () 2 () Special Materials of Construction : MS casing MS casing MS casing MS casing MS casing Other : () One installed spare included. Project IDNumber : CPD3300 Date : January 2 st

9 PUMPS & COMPRESSORS SUMMARY EQUIPMENT NR. : P07 P08 P09 P0 K0 NAME : C05 Reflux pump Discharge V02 pump LPG feed pump Bottom C0 R0effluent compressor Type : Centrifugal Centrifugal Centrifugal Centrifugal Centrifugal Number : Medium transferred : C 3 = Water LPG + C 4 nc 3 /C 3 =/H 2 O Capacity [kg/s] : [m 3 /s] : /.9 Density [kg/m 3 ] : /9.9 Pressure [bara] Suct. / Disch. : 0.0/ / / / /2.2 Temperature In / Out [ o C] : 9.0/ / / / /225.0 Power [kw] Theor. : Actual : Number Theor. : Actual : 2 () 2 () 2 () 2 () Special Materials of Construction : MS casing MS casing MS casing MS casing MS casing Other : () One installed spare included. Project IDNumber : CPD3300 Date : January 2 st

10 EQUIPMENT NR. : NAME : PUMPS & COMPRESSORS SUMMARY K02 C02 Overhead compressor K03 C05 Overhead compressor K04 Air compressor T0 Expander overhead C0 T02 Expander Bottom C04 Type : Centrifugal Centrifugal Centrifugal Number : Medium transferred : nc 3 /C 3 = C 3 = Air nc 3 nc 3 /C 3 = Capacity [kg/s] : [m 3 /s] : 0.68/ / / / /0.69 Density [kg/m 3 ] : 22.9/ / / / /22.2 Pressure [bara] Suct. / Disch. :.8/ /8.0.0/ / / Temperature In / Out [ o C] : 30.0/ / / / /75.0 Power [kw] Theor. : Actual : Number Theor. : Actual : Special Materials of Construction : MS casing MS casing MS casing MS casing MS casing Other : Project IDNumber : CPD3300 Date : January 2 st

11 EQUIPMENT NR. : NAME : PUMPS & COMPRESSORS SUMMARY T03 Expander propylene product Centrifugal Type : Number : Medium transferred : C 3 = Capacity [kg/s] : 8.68 [m 3 /s] : 0.42/0.46 Density [kg/m 3 ] : 20.7/8.7 Pressure [bara] Suct. / Disch. : 0.0/9.0 Temperature In / Out [ o C] : 9.0/5.0 Power [kw] Theor. : Actual : 32 Number Theor. : Actual : Special Materials of Construction : MS casing Other : Project IDNumber : CPD3300 Date : January 2 st

12 DISTILLATION COLUMN SPECIFICATION SHEET EQUIPMENT NUMBER : C0 NAME : Depropanizer General Data Service : distillation Column Type : tray Tray Type : sieve Tray Number () Theoretical : 2 Actual : 26 Feed (actual) : 4 Tray Distance (HETP) [m] : 0.6 Tray Material : SS34 (2) Column Diameter [m] : 0.9 Column Material : CS (2) Column Height [m] : 8 Heating : reboiler (3) Process Conditions Stream Details Feed Top Bottom Reflux Temp. [ o C] : 2.7 : 47.4 : 89.2 : 47.4 Pressure [bara] : 7 : 6.7 : 6.8 : 6.7 Density [kg/m 3 ] : 489 : 37 : 436 : 37 Mass Flow [kg/s] : 6.4 : 6.0 : 0.4 : 5.8 Composition mol% wt% mol% wt% mol% wt% mol% wt% Propylene Propane Ethane Butene Butane Trays (4) Number of sieve holes : Active Tray Area [m 2 ] : Weir Length [mm] : 0.77 Diameter of chute pipe / hole / [mm] : Column Internals Packing Type : Material : Volume [m 3 ] : Length [m] : Width [m] : Height [m] : () Tray numbering from top to bottom. (2) SS = Stainless Steel; CS = Carbon Steel. (3) Reboiler is E05; can operate with LP steam but also as heat exchanger. (4) Tray layout valid for whole column. Not Applicable Project IDNumber : CPD3300 Date : January 2th

13 HEAT EXCHANGER SPECIFICATION SHEET EQUIPMENT NUMBER : E0 In Series : NAME : C0 Overhead Condenser In Parallel : none General Data Service : Condenser Type : Floating Head Position : Horizontal Capacity [kw] : 467 Heat Exchange Area [m 2 ] : 92 Overall Heat Transfer Coefficient [W/m 2 o C] : 300 Log. Mean Temperature Diff. (LMTD) [ o C] : 6.9 Passes Tube Side : 4 Passes Shell Side : 2 Correction Factor LMTD (min. 0.75) : 0.99 Corrected LMTD [ o C] : 6.7 Process Conditions Shell Side Medium : Propane/Ethane Mass Stream [kg/s] : Mass Stream to Condense [kg/s] : Average Specific Heat [kj/kg o C] : Heat of Evap. / Condensation [kj/kg] : Temperature IN [ o C] : Temperature OUT [ o C] : Pressure [bara] : Material : CS () Tube Side Water SS (). SS = Stainless Steel; CS = Carbon Steel. Project IDNumber : CPD3300 Date : January 2 th

14 HEAT EXCHANGER SPECIFICATION SHEET EQUIPMENT NUMBER : E8 In Series : NAME : C04 Reboiler In Parallel : none General Data Service : Reboiler Type : Thermosyphon Position : Vertical Capacity [kw] : 5349 Heat Exchange Area [m 2 ] : 83 Overall Heat Transfer Coefficient [W/m 2 o C] : 300 Log. Mean Temperature Diff. (LMTD) [ o C] : 97.3 Passes Tube Side : Passes Shell Side : Correction Factor LMTD (min. 0.75) :.0 Corrected LMTD [ o C] : 97.3 Process Conditions Medium : Mass Stream [kg/s] : Mass Stream to Evaporize [kg/s] : Condense [kg/s] : Average Specific Heat [kj/kg o C] : Heat of Evap. / Condensation [kj/kg] : Temperature IN [ o C] : Temperature OUT [ o C] : Pressure [bara] : Material : Shell Side LP steam SS () Tube Side Propane / Propylene (2) 6.9 (2) 25 CS () () SS = Stainless Steel; CS = Carbon Steel. (2) Actual temperature change is zero since propane/propylene evaporates Project IDNumber : CPD3300 Date : January 2 th

15 HEAT EXCHANGER SPECIFICATION SHEET EQUIPMENT NUMBER : E5 In Series : NAME : Heat pump trim cooler In Parallel : none General Data Service : Heat Exchanger Type : Floating Head Position : Horizontal Capacity [kw] : 887 Heat Exchange Area [m 2 ] : 3088 Overall Heat Transfer Coefficient [W/m 2 o C] : 300 Log. Mean Temperature Diff. (LMTD) [ o C] : 0.2 Passes Tube Side : 4 Passes Shell Side : 2 Correction Factor LMTD (min. 0.75) : 0.94 Corrected LMTD [ o C] : 9.59 Process Conditions Shell Side Medium : Cooling water Mass Stream [kg/s] : Mass Stream to Evaporize [kg/s] : Condense [kg/s] : Average Specific Heat [kj/kg o C] : Heat of Evap. / Condensation [kj/kg] : Temperature IN [ o C] : Temperature OUT [ o C] : Pressure [bara] : Material () : SS () Tube Side Propylene SS () () SS = Stainless Steel; CS = Carbon Steel. Project IDNumber : CPD3300 Date : January 2 st

16 CENTRIFUGAL PUMP SPECIFICATION SHEET EQUIPMENT NUMBER : P09 Operating : NAME : C0 LPG Pump Installed Spare : Service : LPG Transfer pump Type : Centrifugal Number : Operating Conditions & Physical Data Pumped liquid : LPG Temperature (T) [ o C] : 5 Density (ρ) [kg/m 3 ] : 502 Viscosity (η) [N s/m 2 ] : 2*0 8 Vapour Pressure (p v) [bara] : 7 at Temperature [ o C] : 5 Power Capacity (Φ v ) [m 3 /s] : 0.09 Suction Pressure (p s ) [bara] : 7 Discharge Pressure (p d ) [bara] : 9.7 Theoretical Power [kw] : 5.3 { = Φ v ( p d p s ) 0 2 } Pump Efficiency [] : 0.7 Power at Shaft [kw] :.7 Construction Details () 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 p v /p m [bar] : 0. Pump House : MS Pump Rotor : HT Steel Shaft : HT Steel Special provisions : none Construction Materials (2) 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 Wear Rings : Shaft Box : Operating Pressure [bara] : 7.3 Test Pressure [bara] : () required to prevent any leakage; singlestage pump (2) MS = Mild Steel; HT Steel = High Tensile Steel Project IDNumber : CPD3300 Date : January 2th

17 COMPRESSOR SPECIFICATION SHEET EQUIPMENT NUMBER : K03 Operating : NAME : C05 Overhead compressor Installed Spare : Service : Heat pump gas compressor Type : Centrifugal, polytropic Number : Operating Conditions & Physical Data Pumped liquid : Propylene Temperature In / Out (T) [ o C] : 9.0 / 54 Power Capacity (Φ v ) [m 3 /s] : 6.45 Pressure In [bara] : 0 Discharge Pressure (p d ) [bara] : 8 Actual Power [kw] : 530 Efficiency [] : 0.73 Construction material : CS Construction Material Project IDNumber : CPD3300 Date : January 2th

18 VESSEL SPECIFICATION SHEET EQUIPMENT NUMBER : R0 In Series : NAME : Reactor In Parallel : none General Data Service : Reaction Type Position : Monolith : Vertical Internals : Honeycomb monolith Heating/Cooling medium : none Type : Quantity [kg/s] : Press./Temp. s [bara/ o C] : Vessel Diameter (ID) [m] : 3 Vessel Height [m] : 0 Vessel Tot. Volume [m 3 ] : 7 Vessel Material : SS (2) Other : Downward solid and gas flow through honeycomb monolith Process Conditions Stream Data Gas Feed Solid Feed Bottom Effluent Temperature [ o C] Pressure [bara] 2.9 Density [kg/m 3 ] Mass Flow [kg/s] Composition mol% wt% mol% wt% mol% wt% Propylene Propane Hydrogen Water Methane Ethane Ethylene Butene Butane Carbon monoxide SOC () Spent SOC () () SOC and Spent SOC fractions are solid phase fractions (2) SS = Stainless Steel Project IDNumber : CPD3300 Date : January 2 st

19 VESSEL SPECIFICATION SHEET EQUIPMENT NUMBER : R02 In Series : NAME : Riser regenerator In Parallel : none General Data Service : Reaction Type Position : Riser reactor : Vertical Internals : Open Heating/Cooling medium : none Type : Quantity [kg/s] : Press./Temp. s [bara/ o C] : Vessel Diameter (ID) [m] : 0.9 Vessel Height [m] : 5 Vessel Tot. Volume [m 3 ] : 9.53 Vessel Material : SS (2) Other : Upward bound solid and gas flow. Process Conditions Stream Data Gas Feed Solid Feed Top Effluent Temperature [ o C] Pressure [bara] Density [kg/m 3 ] Mass Flow [kg/s] Composition mol% wt% mol% wt% mol% wt% Propylene Propane Hydrogen Water Oxygen Nitrogen Butane Carbon monoxide SOC () Spent SOC () () SOC and Spent SOC fractions are solid phase fractions (2) SS = Stainless Steel Project IDNumber : CPD3300 Date : January 2 st

20 CYCLONE SPECIFICATION SHEET EQUIPMENT NUMBER : S0 Operating : 2 NAME : Reactor effluent separator Installed Spare : Service : GasSolid separation Type : High Flowrate Stairmand cyclone Number : 2 Operating Conditions & Physical Data Gas Solid : Propane/Propylene/Water/Carbonmonoxide : SOC/ Spent SOC Gas flowrate [kg/s] : 9.0 [m 3 /s] : 2.9 Gas density [kg/m 3 ] : Solid flowrate [kg/s] : 276 [m 3 /s] : Particle size [µm] : 60 Design pressure drop [Pa] : 500 Characteristic velocity [m/s] : 8.47 Temperature [ o C] : 596 Operation pressure [bara] :.9 Cyclone diameter [m] :.0 Cyclone height [m] : 4.04 Particle cut size [µm] : 6.2 Efficiency : 0.99 () Construction material : CS Construction Material () Remaining solids separated by additional filter Project IDNumber : CPD3300 Date : January 2th