Design the phase separator using the heuristics and compare with the specific values in the flowsheet ?

Stream Number 1 3 4 6 115 16.7 1.0 2191.2 100.0 Temperature (C) Pressure (bar) Vapor fraction Mass flow (kg/h) Mole flow (kmol/h) Component flowrates (kmol/h) CO CO2 H HO 320 15.2 1.0 2191.2 100.0 325 16.2 1.0 1678.3 93.2 319.7 15.2 1.0 3869,5 193.2 31.3 27.7 40.2 0.8 31.3 27.7 40.2 0.8 0,0 0,0 0.0 93.2 31.3 27.7 40.2 94.0 Stream Number 7 8 9 10 425.1 14.7 1.0 3869,5 193.2 250.1 13.8 LO 3869.5 193.2 50 12.7 10 2705.0 128.6 50 11.7 0.0 1164.5 64.6 Temperature (C) Pressure (bar) Vapor fraction Mass flow (kg/h) Mole flow (kmol/h) Component flowrates (kmol/h) CO CO, H HO 3.1 3.1 0.0 55.9 55.0 0.0 11.6 474 59.9 74.3 0.0 68.4 65.8 68.4 1.2 64.6 Table B.12.2. Utility Summary Table for Unit 1300 H-1301 Syngas Heater H-1301 First Stage WGS Reactor E-1301 Interstage Cooler H-1302 Second-Stage WGS Reactor E-1302 Low-Pressure Steam Generator -1303 Reactor Ent Cooler V-1301 Shifted Syngas Separator Steam H-1301 Shifted Syngas 50 128 Syngas V-1301 ait ng F-1301 E-1303 185 32 Condensate to Wastewater Treatment Unit E-1301 203 142 E-1302 R-1302 Teo Figure B.12.1. Unit 1300: Shift Reactor Unit Flow Diagram Table B.12.1. Stream Table for Unit 1300