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Table 4.9. Simulation results for biogas upgrading using ILs [hmim][Tf2N] [bmim][Tf2N] [bmim][PF6] 24.45 23.64 23.97 Diameter of absorber, m Make-up solvent, t/h 0.53 0.46 0.66 0.360 0.365 Recirculated solvent, t/h Power, kW COMP 1 COMP 2 13.205 13.205 13.205 15.945 13.546 13.410 PUMP 7.744 6.884 9.444 VACUUM PUMP 8.454 7.447 8.453 total 0.372 45.348 41.082 44.512 For the novel ILs, the processes of biogas upgrading with both aqueous ChCl/Urea and aqueous [Amim][HCOO] were simulated. The effect of water content on the process performance was studied. The results for aqueous ChCl/Urea are shown in Figure 4.17. The amount of aqueous ChCl/Urea decreases and the amount of air increases with increasing of ChCl/Urea content. When the content of ChCl/Urea is higher than 50 wt%, the amount of air increases sharply due to the difficulty in desorption. The total electrical power of biogas upgrading decreases when the percentage of ChCl/Urea changes from 0 to 50 wt%. When the content of ChCl/Urea is more than 50 wt%, the total electrical power decreases but not so obvious. Therefore, 50 wt% aqueous ChCl/Urea can be a recommended solvent. Figure 4.17. Effect of water content on the solvent recirculation, air flow rate and total electrical power demand of biogas upgrading. 42PDF Image | CO2 Separation with Ionic Liquids
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