Statoil Revision A Econamine FG Plus SM Contract: A0NL Overall Heat and Material Balance March 31, 2005 Stream Description Flue Gas to Direct Contact Cooler Absorber Overhead to Atmosphere Make-Up Wash Water to Absorber Excess Water from DCC Carbon Dioxide Product Compressed CO2 Product Stream Numbers Temperature, °C Pressure, kg/cm² (a) 1 (Note 2) 80.0 1.03 2 (Note 2) 36.9 1.03 3 (Note 2) 40.0 1.03 4 (Note 2) 41.7 3.53 5 25.0 1.65 6 124.0 103.43 Component Flows <strong>MW</strong> kgmol/hr mol% kgmol/hr mol% kgmol/hr mol% kgmol/hr mol% kgmol/hr mol% kgmol/hr mol% H 2 O 18.02 13,782 7.8% 10,332 6.2% 3,072 100.0% 6,402 100.0% 120 2.0% 0 0.0% CO 2 44.01 6,873 3.9% 1,032 0.6% 0 0.0% 0 0.0% 5,841 98.0% 5,841 100.0% MEA 61.08 0 0.0% Trace 0.0% 0 0.0% 0 0.0% Trace 0.0% 0 0.0% N 2 + Ar 28.02 132,801 75.5% 132,801 79.8% 0 0.0% 0 0.0% 0 0.0% 0 0.0% O 2 32.00 22,323 12.7% 22,323 13.4% 0 0.0% 0 0.0% 0 0.0% 0 0.0% HSS - 0 0.0% 0 0.0% 0 0.0% 0 0.0% 0 0.0% 0 0.0% Total kgmol/hr Total kg/hr Molecular Weight Density, kg/m³ Liquid Flow, m³/hr Vapor Flow, m³/hr 175,779 4,985,400 28.4 0.980 1,696,580 166,488 4,665,900 28.0 1.103 1,410,319 3,072 55,200 18.0 992 18.5 6,402 115,500 18.0 992 38.8 5,961 259,200 43.5 2.869 90,361 5,841 257,000 44.0 720 356.9 NOTES: 1) Stream in<strong>for</strong>mation corresponds to Process Flow Diagram PFD-001. 2) Stream flow rate listed is <strong>the</strong> total flow to/from all three absorption trains of <strong>the</strong> Econamine FG Plus plant. Flow to/from each absorption train is one-third of <strong>the</strong> indicated flow.
CO 2 Capture Study For <strong>800</strong> <strong>MW</strong> <strong>Power</strong> <strong>Plant</strong> – Tjeldbergodden 4.5 UFD Cooling Water CB2005-0022_Final Report.Doc