Bio-electrochemical sensor, system and method for monitoring and controlling organic carbon levels in a wastewater treatment process
The present disclosure generally relates to a system for monitoring and/or controlling the delivery of one or more organic carbon compounds to a wastewater treatment system. The system comprises a bio-electrochemical sensor to monitor metabolic activity of a population of exo-electrogenic bacteria and provide an electrical output corresponding with the metabolic activity, the bio-electrochemical sensor comprising an electrode pair and a power source to deliver a voltage across the electrode pair, and an electrical output analyzer to analyze the electrical output and correlate the electrical output with a value representing the amount of the one or more organic carbon compounds in the wastewater treatment system. A method and sensor for monitoring and/or controlling the delivery of one or more organic carbon compounds to a wastewater treatment system are also provided.
1. A method of monitoring one or more organic carbon compounds in a wastewater treatment system, the method comprising:
applying power to a bio-electrochemical sensor comprising an anode electrode and a cathode electrode, the cathode being in electrical communication with a non-dioxygen terminal acceptor, wherein each of the anode and cathode electrodes is within one chamber of the treatment system;
measuring an electrical output of the bio-electrochemical sensor and correlating the electrical output with metabolic activity of exo-electrogenic bacteria present in the chamber; and
correlating the electrical output with the one or more organic carbon compounds in the wastewater treatment system,
wherein the wastewater treatment system is an anaerobic digestion system, an anoxic digestion system, a denitrifying system, or a phosphorous removal system.
2. The method of claim 1 , wherein the one chamber is a denitrifying tank or a phosphorous removal tank.
3. The method of claim 1 , wherein the one chamber comprises oxygen at a concentration of about 2 mg/L and: (i) nitrate at a concentration from about 5 mg/L to about 100 mg/L; (ii) bio-available carbon at a concentration from 0 mg/L to about 100 mg/L; or a combination of (i) and (ii).
4. The method of claim 1 , wherein the one chamber comprises nitrate at a concentration from about 5 mg/L to about 100 mg/L; bio-available carbon at a concentration from 0 mg/L to about 100 mg/L; oxygen at a concentration of about 2 mg/L; or any combination thereof.
5. The method of claim 3 , wherein the one or more organic carbon compounds comprises a volatile fatty acid, an organic acid, a complex organic compound, acetic acid, propionic acid, butyric acids, or any combination thereof.
6. The method of claim 3 for controlling delivery of one or more organic carbon compounds in the wastewater treatment system, comprising:
delivering one or more organic carbon compounds into the wastewater treatment system;
monitoring a change in the electrical output in response to the one or more organic carbon compounds; and
adjusting the delivery of one or more organic carbon compounds in response to a change in the electrical output.
7. The method of claim 6 , wherein the adjusting step comprises real time adjustments in the delivery of the one or more organic carbon compounds, wherein the delivery of the one or more organic carbon compounds is adjusted in response to a change in electrical output beyond a threshold.
8. The method of claim 6 for controlling a nitrogen removal process and/or a phosphorous removal process in a wastewater treatment system.
9. The method of claim 7 , wherein the threshold represents a change in a ratio of the value representing the amount of the one or more organic carbon compounds to a value representing the amount of nitrogen and/or phosphorous in the wastewater treatment system, and wherein the delivery of the one or more organic carbon compounds initiates, adjusts, maintains, or stops a nitrification process, a simultaneous nitrification and denitrification process, a denitrification process, and/or a carbon addition process.
10. The method of claim 9 , wherein:
the ratio of the value representing the amount of the one or more organic carbon compounds to a value representing the amount of nitrogen is: about 0:1; about 1:1, about 2:1; about 3:1; about 4:1; about 5:1; about 6:1; about 7:1; about 8:1; about 9:1; or about 10:1, or greater than about 4:1; greater than about 5:1; greater than about 6:1; greater than about 7:1; greater than about 8:1; greater than about 9:1; greater than about 10:1; greater than about 11:1; or greater than about 12:1; and
the ratio of the value representing the amount of the one or more organic carbon compounds to a value representing the amount of the phosphorous is less than about 10:1; less than about 15:1; less than about 20:1; less than about 25:1; less than about 30:1; less than about 35:1; less than about 40:1; less than about 45:1; or less than about 50:1.
11. The method of claim 6 further comprising adjusting delivery of nitrogen and/or phosphorous to the wastewater treatment system in response to the change in the electrical output.
12. The method of claim 1 wherein the one chamber is a chamber within a reactor of the wastewater treatment system.