AR2 data - Solution [molal] Actual pH Exp pH 0.01 12.00...

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Solution [molal] Actual pH Exp pH 0.01 12.00 12.26 0.01 11.70 12.03 0 11.40 11.69 0 11.10 11.42 0 10.80 11.18 0 9 9.04 9.00 9.50 10.00 10.50 11.00 11.50 12.00 9 9.5 10 10.5 11 11.5 12 12.5 f(x) = 1.08x - 0.66 R² = 1 pH Calibration Actual pH Measured pH
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CO2 Flow Rate CO2 Flow Rate L/min N2 Flow Rate LN2 Flow Rat%CO2 ExpIR %CO2 25 0.45 10.1 12.793 3.4 19.2 54 0.97 9.8 12.413 7.3 35 89 1.6 9.7 12.287 11.5 45.6 17 0.31 7.5 9.500 3.1 17.6 24 0.43 8.5 10.767 3.9 21.7 16 0.29 9.5 12.033 2.3 13 15 0.27 10 12.667 2.1 11.6 0.0 2.0 4.0 6.0 8.0 10.0 12.0 14.0 0 5 10 15 20 25 30 35 40 45 50 f(x) = 3.59x + 6.17 R² = 0.98 IR Calibration IR %CO2 Linear Re- gression for IR %CO2 %CO2 Exp. %CO2 IR
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Reading Actual Values CO2 Flow [L/min] 40 0.72 N2 Flow Rate [L/min] 5 6.33 CO2 in [mol/min] CO2 liq out [mol/min] NaOH Flow [mL/min] 91 295.75 0.03 0 RH% - 37.7 Temperature [C] - 20.8 Level [cm] - 12.5 D [cm] - 15 k2 exp dG exp [kJ/mol] Liquid Volume [L] - 2.21 4.80E+03 -20.705 IR %CO2 28.2 6.14 Tacometer Reading [rpm] - 415 Power 3.5 k23 equilibrium 4.80E-11 k2 equilibrium 5.30E+03 kw 1.00E-14 Time [sec] pH [Na+] [HCO3 -] 0 12.12 1.318E-02 7.586E-13 1.318E-02 5.95E-15 0.5 11.78 6.026E-03 1.660E-12 1.318E-02 1.22E-04 1 11.78 6.026E-03 1.660E-12 1.318E-02 1.22E-04 1.5 11.77 5.888E-03 1.698E-12 1.318E-02 1.27E-04 2 11.76 5.754E-03 1.738E-12 1.318E-02 1.32E-04 2.5 11.74 5.495E-03 1.820E-12 1.318E-02 1.43E-04 3 11.72 5.248E-03 1.905E-12 1.318E-02 1.54E-04 3.5 11.7 5.012E-03 1.995E-12 1.318E-02 1.66E-04 4 11.69 4.898E-03 2.042E-12 1.318E-02 1.73E-04 4.5 11.67 4.677E-03 2.138E-12 1.318E-02 1.85E-04 5 11.66 4.571E-03 2.188E-12 1.318E-02 1.92E-04 5.5 11.63 4.266E-03 2.344E-12 1.318E-02 2.13E-04 6 11.62 4.169E-03 2.399E-12 1.318E-02 2.20E-04 6.5 11.6 3.981E-03 2.512E-12 1.318E-02 2.35E-04 7 11.6 3.981E-03 2.512E-12 1.318E-02 2.35E-04 7.5 11.59 3.890E-03 2.570E-12 1.318E-02 2.42E-04 8 11.58 3.802E-03 2.630E-12 1.318E-02 2.50E-04 8.5 11.57 3.715E-03 2.692E-12 1.318E-02 2.58E-04 9 11.56 3.631E-03 2.754E-12 1.318E-02 2.66E-04 9.5 11.56 3.631E-03 2.754E-12 1.318E-02 2.66E-04 10 11.55 3.548E-03 2.818E-12 1.318E-02 2.75E-04 15 11.53 3.388E-03 2.951E-12 1.318E-02 2.92E-04 20 11.51 3.236E-03 3.090E-12 1.318E-02 3.10E-04 25 11.5 3.162E-03 3.162E-12 1.318E-02 3.20E-04 [OH - [H 3 O + ]
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Mass Balance CO2 gas out [mol/min] CO2 out [mol/min] OUT/IN Yin Yout 0.02 0.02 0.65 0.11 0.07 Yout * 0 dG Table 1 Deviation -20.93 1.1% Experiment Yin Gas 0.17 Yin liq 0 Yout gas 0.14 Yout liq 0.13 mC out 0.03 mC in 0 [CO3 2-] 3.763E-13 3.518E-03 3.518E-03 3.584E-03 3.648E-03 3.772E-03 3.890E-03 4.002E-03 4.056E-03 4.160E-03 4.210E-03 4.352E-03 4.397E-03 4.483E-03 4.483E-03 4.525E-03 4.565E-03 4.605E-03 4.643E-03 4.643E-03 4.680E-03 4.751E-03 4.818E-03 4.850E-03 11.5 11.7 11.9 12.1 0.000E+00 1.000E-03 2.000E-03 3.000E-03 4.000E-03 5.000E-03 6.000E-03 Na+ = 0.01 mol/kg [HCO3 -] [CO3 2-] pH Concentration [mol/L] C
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Murphee Tray Efficiency 43.1% Theory mC Y 0 0.17 0.01 0.17 0.01 0.17 0.01 0.17 0.02 0.17 0.03 0.17 0.03 0.17 0 0.02 0 0.05
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AR2 data - Solution [molal] Actual pH Exp pH 0.01 12.00...

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