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15 3.0 / 9.0 150 30 3.0 / 10.0 140 45 3.0 / 10.0 140 60 3.0 / 11.0 140 75 3.0 / 12.0 140 90 2.0 / 9.0 140 105 1.0 / 6.0 140 120 0.5 / 4.0 140 135 0.25 / 3.0 140 150 0.0 / 0.0 140 165 0.0 / 0.0 140 80 2.08 77 - 75 2.15 75 2.10 144 - 140 2.19 140 2.70 140 3.61 140 5.88 140 - 140 8.76 12.69 - 12.63 12.49 - 12.13 12.00 11.41 11.26 - 10.41 Table 3. Test 1: Acidification of IO-1 seawater at 140 mL/min Time, min Amp/V olt Influent Seawater Flow Rate, mL min-1 Influent DI Flow Rate, mL min-1 Effluent Acidified Seawater pH Effluent DI Cathode pH In the second test, a similar IO synthetic formulation was made (IO-2) and used to determine the effect that flow rate through the IX compartment had on the performance of the Nalco cell. Initially IO-2 was pumped at 900 mL/min before a flow of 860 mL/min was established and maintained after 90 minutes. The results summarized in Table 4 establish that at higher flow rates the pH of the effluent seawater can be lowered using the acidification cell. Higher influent seawater flow rates increase the percent recovery from 50% to 86%. In addition the results suggest that the flow rate to current ratio was improved from 560 to 716 (860 mL/min/1.20 amps). Table 4. Test 2: Acidification of IO-2 seawater at 900 mL/min Time, min Amp/V olt Influent Seawater Flow Rate, mL min-1 Influent DI Flow Rate, mL min-1 Effluent Acidified Seawater pH Effluent DI Cathode pH 15 1.0 / 5.0 900 30 1.5 / 7.0 900 45 1.5 / 7.0 864 60 1.5 / 7.0 870 75 1.5 / 7.0 864 90 1.5 / 7.0 868 105 1.5 / 7.0 860 120 1.5 / 7.0 860 135 1.0 / 6.0 860 150 1.0 / 6.0 860 165 1.0 / 6.0 860 180 1.2 / 6.5 860 140 7.31 140 6.13 140 5.95 140 4.63 140 4.41 140 4.30 140 4.18 140 4.05 140 6.31 140 6.20 140 6.27 140 6.17 11.79 12.06 12.04 11.90 11.89 11.75 11.76 11.74 11.12 11.42 11.52 11.20 12PDF Image | CO2 from Seawater
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