Systems and methods for producing ammonium nitrate
Systems and methods for producing ammonium nitrate are disclosed herein. Exemplary systems can comprise a bioreactor positioned to receive a feed including ammonia. The bioreactor can hold a liquid solution including (i) an ammonia oxidizing bacteria (AOB) and (ii) a nitrite oxidizing bacteria (NOB). The AOB can facilitate oxidation of the ammonia to produce a nitrite at a nitritation rate and the NOB can facilitate oxidation of the nitrite at a nitratation rate. Thus, the bioreactor can produce a mixed liquor comprising a nitrate biologically. The system can further comprise a filter positioned to receive the mixed liquor and produce a permeate and a sludge. A sensor can measure the concentration of the liquid solution of the bioreactor, and a controller coupled to the sensor can regulate the mass flow of nitrogen and/or phosphorus of the bioreactor feed based on the measured concentration of the liquid solution.
1 . An industrial system for producing ammonium nitrate using biological activity, the system comprising:
a bioreactor positioned to receive a feed comprising ammonia, wherein the bioreactor is configured to hold a liquid solution including (i) an ammonia oxidizing bacteria (AOB) and (ii) a nitrite oxidizing bacteria (NOB);
a sensor positioned to measure a concentration of the liquid solution of the bioreactor; and
a controller operably coupled to the sensor, wherein the controller is configured to control biological activity within the bioreactor based on the measured concentration of the liquid solution to produce ammonium nitrate.
2 . The system of claim 1 , wherein the bioreactor is configured to produce a mixed liquor comprising a nitrate.
3 . The system of claim 1 , wherein the controller is configured to control the biological activity by regulating a wasting rate of a sludge produced from one or more outputs of the bioreactor.
4 . The system of claim 1 , wherein the controller is configured to control the biological activity by regulating a mass flow of nitrogen and/or phosphorus of the feed.
5 . The system of claim 1 , wherein the sensor is a pH sensor positioned to measure a pH of the liquid solution, and wherein the controller is configured to regulate a mass flow of nitrogen and/or phosphorus of the feed to the bioreactor based on the measured pH of the liquid solution.
6 . The system of claim 1 , further comprising a return line positioned to direct a first portion of a sludge produced from one or more outputs of the bioreactor into the bioreactor as return sludge, wherein:
the controller is configured to regulate a return rate of the return sludge based on a sludge retention time of at least 15 days, and
the sludge retention time equals a volume of the liquid solution divided by a remaining portion of the sludge that is not the return sludge, wherein the sludge retention time is based on a thickening of the sludge.
7 . The system of claim 1 , further comprising (i) a return line positioned to direct a first portion of a sludge produced from one or more outputs of the bioreactor into the bioreactor as return sludge, and (ii) a waste line positioned to direct a second portion of the sludge away from the bioreactor as waste sludge, wherein the controller is configured to regulate a return rate of the return sludge and/or a waste rate of the waste sludge based on a measured pH.
8 . The system of claim 1 , further comprising:
a return line positioned to direct a portion of a sludge produced from one or more outputs of the bioreactor into the bioreactor as return sludge;
a heat exchanger positioned to increase and/or decrease a temperature of the return sludge; and
a temperature sensor positioned to measure a temperature of the liquid solution in the bioreactor,
wherein the controller is operably coupled to the temperature sensor and the heat exchanger, and is configured to adjust operation of the heat exchanger based on the measured temperature.
9 . A method for producing ammonium nitrate via a bioreactor, the method comprising:
receiving, at the bioreactor, a feed comprising ammonia;
producing a mixed liquor via the bioreactor, wherein the bioreactor holds a liquid solution having (i) an ammonia oxidizing bacteria (AOB) configured to facilitate oxidation of the ammonia to produce a nitrite, and (ii) a nitrite oxidizing bacteria (NOB) configured to facilitate oxidation of the nitrite; and
controlling biological activity within the bioreactor based on a concentration of the liquid solution to produce ammonium nitrate.
10 . The method of claim 9 , further comprising:
controlling a mass flow of nitrogen and/or phosphorus of the feed to be mixed with the liquid solution held by the bioreactor, wherein the feed comprises the ammonia, and wherein the liquid solution comprises the AOB and the NOB;
obtaining a return rate of a return sludge to be mixed with the liquid solution;
obtaining the concentration of the liquid solution; and
adjusting the mass flow of nitrogen and/or phosphorus of the feed based at least in part on the obtained concentration of the liquid solution.
11 . The method of claim 9 , further comprising controlling biological activity by regulating a wasting rate of a sludge produced from outputs of the bioreactor.
12 . The method of claim 9 , further comprising controlling biological activity by regulating a mass flow of nitrogen and/or phosphorous of the feed.
13 . The method of claim 9 , further comprising measuring a pH of the liquid solution; and regulating a mass flow of nitrogen and/or phosphorus of the feed to the bioreactor based on the measured pH to maintain the pH of the liquid solution within a range of 4.0-7.0.
14 . The method of claim 9 , further comprising directing a first portion of a sludge produced from outputs of the bioreactor into the bioreactor as return sludge; and regulating a return rate of the return sludge based on a sludge retention time of at least 15 days.
15 . The method of claim 9 , further comprising:
directing a first portion of a sludge produced from outputs of the bioreactor into the bioreactor as return sludge;
directing a second portion of the sludge away from the bioreactor as waste sludge; and
regulating a return rate of the return sludge and a waste rate of the waste sludge such that a sum of one or more outputs of the bioreactor is less than a sum of one or more inputs of the bioreactor.
16 . An industrial system for producing ammonium nitrate using biological activity, the system comprising:
a bioreactor configured to receive a feed comprising ammonia and hold a liquid solution including a nitrifier;
a sensor positioned to measure a condition of the liquid solution within the bioreactor; and
a controller operably coupled to the sensor, wherein the controller is configured to control biological activity within the bioreactor based on the measured condition of the liquid solution to produce ammonium nitrate.
17 . The system of claim 16 , wherein the nitrifier includes an ammonia oxidizing bacteria (AOB) and/or a nitrite oxidizing bacteria (NOB).
18 . The system of claim 16 , wherein the nitrifier includes an ammonia oxidizing bacteria (AOB) and a nitrite oxidizing bacteria (NOB).
19 . The system of claim 16 , wherein the bioreactor is a first bioreactor and the liquid solution is a first liquid solution, the system further comprising a second bioreactor positioned downstream from the first bioreactor and configured to hold a second liquid solution including at least a portion of the first liquid solution.
20 . The system of claim 19 , wherein the nitrifier is a first nitrifier and the first liquid solution includes the first nitrifier, and wherein the second liquid solution includes a second nitrifier different than the first nitrifier.
21 . The system of claim 16 , wherein the controller is configured to automatically control biological activity in the bioreactor based on the condition measured by the sensor.
22 . The system of claim 16 , wherein the sensor is a pH sensor positioned to measure a pH of the liquid solution.
23 . The system of claim 16 , wherein the sensor is a temperature sensor positioned to measure a temperature of the liquid solution.
24 . The system of claim 16 , wherein the sensor is a concentration sensor positioned to measure a concentration of at least one of oxygen, phosphorus, carbon, calcium, or magnesium in the liquid solution.
25 . The system of claim 16 , wherein the bioreactor is positioned to receive the feed at a continuous flow rate.
26 . The system of claim 16 , wherein the bioreactor is configured to produce a mixed liquor, the system further comprising a unit positioned downstream of the bioreactor and configured to separate solids from liquid and soluble constituents of the mixed liquor.
27 . The system of claim 16 , wherein the bioreactor is configured to produce a sludge, and wherein at least a portion of the sludge remains in the bioreactor for a sludge retention time of at least 15 days.
28 . The system of claim 16 , wherein the liquid solution of the bioreactor has a nitrite concentration of at least 100 parts per billion (ppb).
29 . The system of claim 16 , wherein the bioreactor is configured to receive sodium bicarbonate prior to receiving the feed comprising ammonia.
30 . A method for producing ammonium nitrate via a bioreactor, the method comprising:
receiving, at the bioreactor, a feed comprising ammonia;
mixing the feed with a liquid solution within the bioreactor, the liquid solution comprising a nitrifier;
measuring a condition of the liquid solution; and
based in part on the measured condition of the liquid solution, adjusting biological activity within the bioreactor to produce ammonium nitrate.