Source: UNIV OF IDAHO submitted to NRP
EFFICIENT PRODUCTION OF GREEN NITROGEN FERTILIZER FROM AIR AND WATER BY A LIQUID-PHASE PLASMA PROCESS
Sponsoring Institution
National Institute of Food and Agriculture
Project Status
COMPLETE
Funding Source
Reporting Frequency
Annual
Accession No.
1023208
Grant No.
2020-67022-31699
Cumulative Award Amt.
$199,923.00
Proposal No.
2019-06440
Multistate No.
(N/A)
Project Start Date
Jul 1, 2020
Project End Date
Jun 30, 2024
Grant Year
2020
Program Code
[A1521]- Agricultural Engineering
Recipient Organization
UNIV OF IDAHO
875 PERIMETER DRIVE
MOSCOW,ID 83844-9803
Performing Department
Biological Engineering
Non Technical Summary
Despite the remarkable success in nitrogen fertilizer synthesis which has increased agricultural productivity to sustain half of the world population by the 21st century, significant environmental consequences exist for the current nitrogen fertilizer manufacturing system such as the Haber-Bosch (HB) process involving high temperature, high pressure, catalysts and a huge amount of natural gas as substrate. The long-term goal of this proposal is to reduce our reliance on fossil fuels and associated environmental issues (i.e., greenhouse gas emissions) in nitrogen fertilizer production by developing a transformative liquid-phase plasma discharge technology for efficiently manufacturing nitrogen fertilizer using only air and water as substrates without catalysts. Such technology will move the US to a leading position in renewable fertilizer production by minimizing resource consumption and improving the overall US agricultural economy. This seed grant will help PD collect preliminary evidence to show the promise of this new endeavor, and be prepared to compete for larger federal funding in this topical area. The specific objectives of this seed project are to 1) study the technical feasibility of nitrogen fixation (convert N2 to nitrogen oxide or ammonia) in water treated by liquid-phase plasma discharge with air (or pure N2) in a novel plasma reactor designed and developed by the PD equipped with an inexpensive AC power supply; 2) determine significant factors that influence nitrogen fixation by the liquid-plasma discharge process, and evaluate the liquid plasma reactor to determine the optimal operating conditions for efficient production of nitrogen fertilizer from air and water.Despite the remarkable success in nitrogen fertilizer synthesis which has increased agricultural productivity to sustain half of world population by the 21st century, significant environmental consequences exist for the current nitrogen fertilizer manufacturing system such as the Haber-Bosch (HB) process involving high temperature, high pressure, catalysts and huge amount of natural gas as substrate. The long-term goal of this proposal is to reduce our reliance on fossil fuels and associated environmental issues (i.e., greenhouse gas emissions) in nitrogen fertilizer production by developing a transformative liquid-phase plasma discharge technology for efficiently manufaturing nitrogen fertilizer using only air and water as substrates without catalysts. Such a technology will move the US to a leading position in renewable fertilizer production by minimizing the resource consumption and improving the overall US agricultural economy. This seed grant will help PD collect preliminary evidence to show the promise of this new endeavor, and be prepared to compete for larger federal funding in this topical area.The specific objectives of this seed project are to 1) study the technical feasibility of nitrogen fixation (convert N2 to nitrogen oxide or ammonia) in water treated by liquid-phase plasma discharge with air (or pure N2) in a novel plasma reactor designed and developed by the PD equipped with an inexpensive AC power supply; 2) determine significant factors that influence nitrogen fixation by the liquid-plasma discharge process, and evaluate the liquid plasma reactor to determine the optimal operating conditions for efficient production of nitrogen fertilizer from air and water.
Animal Health Component
80%
Research Effort Categories
Basic
20%
Applied
80%
Developmental
(N/A)
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
10252102020100%
Knowledge Area
102 - Soil, Plant, Water, Nutrient Relationships;

Subject Of Investigation
5210 - Fertilizers;

Field Of Science
2020 - Engineering;
Goals / Objectives
The long-term goal of this proposal is to reduce our reliance on fossil fuels and the associated environmental issues (i.e., greenhouse gas emissions) in producing nitrogen fertilizer. A green technology to manufacture nitrogen fertilizer at high efficiency without using fossil fuels as raw substrates or catalysts will be developed in this study. Such technology will move the US to a leading position in renewable fertilizer production in the world by minimizing resource consumption and improving the overall US agricultural economy. The specific objectives of this project are to 1) study the technical feasibility of nitrogen fixation (convert N2 to nitrogen oxide or ammonia) in water treated by liquid-phase plasma discharge with air (or pure N2) in a novel plasma reactor designed and developed by the PD equipped with an inexpensive AC power supply; 2) determine significant factors that influence nitrogen fixation by the liquid-plasma discharge process, and evaluate the liquid plasma reactor to determine the optimal operating conditions for efficient production of nitrogen fertilizer from air and water.
Project Methods
1. Methods for specific objective 1: study the technical feasibility of nitrogen fixation (convert N2 to nitrogen oxide or ammonia) in water treated by liquid-phase plasma discharge with air (or pure N2) in a novel plasma reactor designed and developed by the PD equipped with an inexpensive AC power supply.Experimental apparatus: The plasma reactor designed in the preliminary study will be built with a controlling module for better monitoring and control of the nitrogen fixation processes. The key dimensions of the plasma reactor are:diameter of the reactor body D = 12.7 mm, thickness of dielectric plate δ = 3.2 mm, and the diameter of the dielectric plate opening ? = 0.75 mm.Experimental design: Experiments with the operating parameters defined in the preliminary study will be performed to diagnose plasma generation and verify the mechanism for nitrogen fixation by LPPD. Two operational modes (circulation and one pass) for the LPPD process will be analyzed. Technically, important plasma properties during electric discharge will be studied with three techniques commonly used in the literature [26] for characterizing the discharge breakdown moment of plasma in flowing water and air (or N2). The first technique is to interpret the driving current and voltage waveforms by measuring the electric parameters, such as breakdown voltage, current, and power, and their mean values, using two types of electric devices. Standard multi-meters will be used to estimate mean voltage and current values to produce current-voltage (A-V) characteristics of the discharge under the specified experimental conditions. Time-resolved records of voltage and current will be measured using an oscilloscope (Tektronix TBS1052B) operating up to 50 MHz with a high voltage probe (Tektronix P6015A, attenuation 1:1000) and AC Current Probe probe (Tektronix P6021). Experiments with air (or N2) and water will be repeatedly run for at least 10 times and the mean values will be used for analysis. The second technique to be used in this study is the intensified Charge Coupled Device (ICCD) imaging using cameras to acquire images at very low light levels over a wide light spectrum and at high speeds to observe formation and propagation of plasma streamers happening in the air and water. The ICCD camera will be connected to a PC with the software to process the images. The third technique for specific plasma monitoring and quantification is to use optical emission spectroscopy (OES, Ocean- QEPro Spectrometer, Ocean Optics Inc.) to record the spectrum of plasma emission at nano-second scale and analyze the concentrations of reactive species generated with plasma discharge.Sampling and analysis: For static A-V characteristics, mean values of voltage and current obtained from the multi-meter measurements will be used to construct the static current-voltage characteristics and reveal breakpoints related to the LPPD processes occurring before, during, and after the discharge breakdown moment. The A-V characteristics and their breakpoints allow the determination of plasma generation. Time-resolved characteristics observed by the oscilloscope will show a true evaluation of the parameters during the processes. Combined with the static current-voltage characteristics, the determination of the occurrence of plasma reaction can be obtained in a relatively precise way. The images captured by the ICCD camera will provide visual observation of plasma discharge type such as pulsed corona and arc to further evidence the happening of the plasma process. Concentrations of •OH, •N2O, O•, N•, O3, and other radicals will be analyzed by OES with software (OceanView, Ocean Optics Inc.) and compared for different operational modes to verify the mechanism of continuous nitrogen fixation process by LPPD.Expected outcomes: The plasma discharge type and formation of the reactive species in water and air (or N2) for instant nitrogen fixation and feasibility for NOx and NH3 production in this particular process will be verified after completion of the experiments in this section.2. Methods for specific objective 2: determine significant factors that influence nitrogen fixation by the liquid-plasma discharge process and evaluate the liquid plasma reactor to determine the optimal operating conditions for efficient production of NOx/NH3 in water.Experimental apparatus: The same plasma reactor and measuring equipment for Specific Objective 1 will be used. Experimental design: The performance of the plasma reactor in nitrogen fixation in terms of quantity and efficiency will be evaluated with respect to air (or N2) flow rate (LPM), liquid flow rate (ml/min), power input (watt) and the reactor dimensions (by changing the dielectric plate opening ?). All these variables will be tested at five scattered levels to determine if they are significant factors for the response variables (i.e, NOx/NH3 production rate and power efficiency) by statistical analysis. The optimization of significant variables will be conducted using the Central Composite Design (CCD) with Response Surface Methodology (RSM). The ranges of each variable and the center values (zero level) in the CCD design are chosen based on the results from the significance test and will be adjusted if necessary (Table 1). According to this CCD design, 18 experiments will be performed for the three variables each being tested at five levels with four replicates of the center values for NOx and NH3 production, respectively. A second-order quadratic model will be used to fit the data set of different responses with the operational parameters, and the corresponding results will be subjected to regression analysis using the least square approach to generate the respective quadratic equations using statistical software (Design Expert). After that, volume ratios of N2 to O2 by mixing pure N2 and O2 will be investigated for four more levels (2:1, 1:1, 0.5:1, 0.3:1 as compared to 3.7:1 in ambient air) to determine the effect of gas composition on the NOx production rate and power efficiency. Other properties of treated water will also be analyzed and discussed, include applied voltage needed to induce plasma discharge, change of pH and conductivity, and H2O2 production rate, etc.Sampling and analysis: For each experimental run, water samples of 20 ml each will be taken at predetermined time intervals for analysis of pH, conductivity, NO2-, NO3-, NH4+ and H2O2. The NOx (NH3) production rate will be determined by dividing concentration of NOx (NO2-+NO3- or NH4+) by treatment time, and the power efficiency for nitrogen fixation (mg N/kWh) is obtained by dividing the amount of N fixed (based on NOx (NH3) production) by the power consumed.Expected outcomes: The optimal operating conditions of the plasma reactor and optimized productivity of NOx/NH3 from air and water by LPPD process will be determined.

Progress 07/01/20 to 06/30/24

Outputs
Target Audience:Research institutions and companies engaged in fertilizer research and production; Researchers in nonthermal plasma technology and nitrogen fixation;Nationally and internationally professional communities of fertilizer and soil health Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?One graduate student hasbeen hired and one other undergraduate student have been trained and involved to conduct the project and related research work. How have the results been disseminated to communities of interest?Journal articles and conference presentations/papers What do you plan to do during the next reporting period to accomplish the goals? Nothing Reported

Impacts
What was accomplished under these goals? Mechanism ofammonia oxidation by liquid-phase plasma Nitrogen fixation to ammoniawas not successfully achieved using our liquid-phase plasma process, the ammonia oxidation instead was accomplished with very encouraging results. As reported in the last year's results,98.91% of NH3- N could be removed with a N2 selectivity of 92.91% in a one-hour treatment. Our research thenwasfocused on elucidating the mechanism forliquid phase plasma discharge to accelerate the ammonia oxidation reaction.First,free electrons gain energy from the electric field generated between the discharge and ground electrodes, resulting in high-energy electrons. These high-energy electrons can interact with oxygen, water molecules, and other ionic compounds in the aqueous phase to initiate various physical and chemical reactions. These processes may generate shock waves, reactive chemical species such as •OH, ?O, ?H, H2, O2, H2O2 and intense ultraviolet (UV) radiation which can be detected as a spectrum of emitted light photons by optical emission spectroscopy (OES). This spectrum of plasma-emitted radiation is grated, and the intensity is measured as a function of the wavelength. The spectra obtained in this study were analyzed using the National Institute of Standards and Technology atomic spectra databaseto identify the various active chemical species present in the reactor during operation.The relative intensity of the optical emission spectra observed in our CLPPD system from oxygen gas (flow rate = 2.5 L/min) at different power input levels (300 W and 225 W, respectively). The magnitude of the emission intensity lines provides a qualitative indicator of chemical species concentration in the optical emission. The results showed that the relative intensity of OES was strongly influenced by the magnitude of the discharge voltage. For example, an increase in power input from 225W (Vrms = 9.2 kV, Irms = 9.08 mA) to 300W (Vrms = 10.4 kV, Irms = 11.2 mA) resulted in a significant increase in the density/intensity of the transition lines of all active radicals and ionic species. This observation could be ascribed to the fact that stronger electric fields are produced when the power is increased, and as a result, collisions of high-energy electron with oxygen molecules accelerates the generation of active radicals through ionization, resulting in more light emissions. The discharge produced a significant UV radiation that was clearly visible to the naked eye and was dominated by atomic oxygen lines at 777.04 and 844.14 nm, which correspond to atomic transition 3p5P-3s5S and 3p3P-3s3S, respectively. These transitions arise from the decay of various excited states of oxygen atoms. In addition, molecular bands corresponding to transitions in the first negative system of the ?O2+ ions (b4Σg−- a4Πu), as well as hydrogen atoms, (3s→2p), were found at 559.6 and 659 nm, respectively. The ?OH emission from the electronic transition of A2Σ+ → X2Π with a band-head at 310.2 nm was also visible for the oxygen plasma discharge. These excited states can be generated due to both energetic electron impact excitation of oxygen atoms and energetic electron impact dissociation or Penning ionization of O2, NH3, ?OH, H2O2, and H2O molecules. The emission spectra obtained from this study are consistent with the results from other studies conducted by different research groups. ?O2+ and ?OH molecules are the most important reactive species that are frequently generated by the plasma treatment of aqueous solutions. They can oxidize most organic and inorganic compounds they come in contact with and are the primary source of hydrogen peroxide in plasma systems. During plasma treatment, NH3-N is mainly oxidized to NO3-, NO2-, and nitrogen gas, which are inactive. Based on data from the OES, theconceptual reaction pathways for NH3-N removal by the CLPD system are proposed.

Publications

  • Type: Journal Articles Status: Published Year Published: 2024 Citation: D. Mohotti, MM. Hossain, R. Ndeddy Aka, A. Mukhtar, N. Holloway, *S. Wu. 2024. Evaluating a green liquid phase plasma discharge process and working mechanism for remediating cobalt contamination in water. Separation and Purification Technology, 354(3):128940. https://doi.org/10.1016/j.seppur.2024.128940.
  • Type: Conference Papers and Presentations Status: Published Year Published: 2024 Citation: D. Mohotti, MM. Hossain, Y. Yuan, R. Robi, S. Wu. Evaluating a Green Liquid Phase Plasma Discharge Process and The Mechanism for Remediating Cobalt Contamination in Water. University of Idaho Institute for Health in the Human Ecosystem Annual Research Symposium, April 8, 2024.
  • Type: Conference Papers and Presentations Status: Published Year Published: 2024 Citation: Mohotti, D., MM. Hossain, R. Ndeddy Aka, A. Mukhtar, *S. Wu. Efficient Cobalt Removal and Synthesis of Cobalt Oxide Particles from Wastewater by A Continuous Liquid Phase Plasma Discharge Process, ACS Fall 2024 Conference, Denver, CO. August 18-22, 2024.
  • Type: Conference Papers and Presentations Status: Published Year Published: 2024 Citation: T. Booker, MM. Hossain, Y. Yuan, S. Asghar, S. Wu. Investigating Early Growth Characteristics of Nonthermal Plasma Treated Wheat Seeds. University of Idaho Institute for Health in the Human Ecosystem Annual Research Symposium, April 8, 2024.


Progress 07/01/22 to 06/30/23

Outputs
Target Audience: Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided? One graduate student and one undergraduate student have been hired and one other undergraduate student have been trained and involved to conduct the project and related research work. How have the results been disseminated to communities of interest? What do you plan to do during the next reporting period to accomplish the goals?Nitrogen fixation to produce ammonia is not yet achievedwith only water and air or water with nitrogen gas by the CLPD process. Our plan for the next period will be to test if a hybrid of plasma with a catalyst is able to make the reaction of synthesis of ammonia from air (or nitrogen) and water as we have achieved the opposite reaction very successfully.

Impacts
What was accomplished under these goals? To understand the effect of plasma assisted reactions on nitrogen cycle, our novel continuous liquid plasma process (CLPD) was evaluated to remove and convert NH3- N from synthetic wastewater, which is usually very hard to achieve by other chemical/physical processes. The Box-Behnken experimental design was used to optimize the main process parameters, including the initial NH3- N concentration (50-200 mg/L), power input (150-300 W), and gas-flow rate (1.5-2.5 L/min), for efficient NH3- N removal from wastewater. The gas-flow rate and power input were found to be significant factors affecting the removal efficiency of NH3- N, whereas the initial concentration of NH3- N played a vital role in determining the energy efficiency of the process. Under the optimal conditions of an initial NH3- N concen- tration of 200 mg/L, applied power of 223 W, and gas-flow rate of 2.4 L/min, 98.91% of NH3- N could be removed with a N2 selectivity of 92.91%, and the corresponding energy efficiency was 0.527 g/kWh after 2 hrs of treatment. A small fraction of undesirable NO−3 -N (7.05 mg/L) and NO−2 -N (2.83 mg/L) were also produced. Kinetic modeling revealed that NH3- N degradation by the CLPD followed a pseudo-first-order reaction model, with a rate constant (k) of 0.03522 min− 1. Optical emission spectroscopy (OES) was used to gather information about the active chemical species produced during the plasma discharge. The obtained spectra revealed the presence of several highly oxidative radicals, including ?OH, ?O, and ?O+2 . These results demonstrate the potential of liquid phase plasma discharge as a highly efficient technology for removing ammonia from aqueous solutions.

Publications

  • Type: Journal Articles Status: Published Year Published: 2022 Citation: Ndeddy Aka, RJ., S. Wu, #D. Mohotti, MA. Bashir, A. Nasir. 2022. Evaluation of a liquid-phase plasma discharge process for ammonia oxidation in wastewater: process optimization and kinetic modeling. Water Research, 224: 119107. https://doi.org/10.1016/j.watres.2022.119107.
  • Type: Conference Papers and Presentations Status: Published Year Published: 2022 Citation: Wu, S., B. Thapa, Yuan, Y., R. Ndeddy Aka, A. Nasir. 2022. Optimization of a green plasma process for nitrogen fixation in water. ASABE 115th Annual International Meeting. Paper#: 2200908. Houston, TX. July 17-20, 2022.
  • Type: Conference Papers and Presentations Status: Published Year Published: 2023 Citation: Booker, T., S. Wu, Y. Yuan. Evaluating a green nitrogen fertilizer produced by plasma discharge of air and water. University of Idaho Undergraduate Research Symposium, April 24, 2023.
  • Type: Conference Papers and Presentations Status: Published Year Published: 2022 Citation: Booker, T., S. Wu, Y. Yuan. Evaluating a green nitrogen fertilizer produced by plasma discharge of air and water. 2022 Idaho Conference on Undergraduate Research (ICUR). Online. July 20-21, 2022.


Progress 07/01/21 to 06/30/22

Outputs
Target Audience: Research institutions and companies engaged in fertilizer research and production; Nationally and internationally professional communities of fertilizer and soil health Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided? One graduate student and one undergraduate student have been hired and one other undergraduate studenthave been trained and involved to conduct the project and related research work How have the results been disseminated to communities of interest?Journal articles and conference presentations/papers What do you plan to do during the next reporting period to accomplish the goals?Our next reporting period is going to focus on further optimization of the plasma process for nitrogen fixation and ammonia removal.

Impacts
What was accomplished under these goals? Factorial design is used to find out significant process factors for NOx production using NOx concentration and energy efficiency for nitrogen fixation as the responses. The summary of analysis of variance settled the model a second-order polynomial equation. The ANOVA analysis for NOx Model with F-value of 231.51 implies the model is significant at 95% confidence level. Applied power, water volume, and air flow rate had positive effects on NOx with power as a factor with the most significant positive effect while water flow rate was the only factor with a negative effect on NOx production. Water volume and air flow rate had a positive effect on N-efficiency with the volume being the most significant positive factor. And water flow rate is the only factor with a negative effect on N-efficiency. The response surface contour plot by a central composite designrevealed that the maximum production of NOx that can be achieved 284mg/Lat the center of the circle with2.2 standard liter per minutefor air flow rate and 310 W for appliedpower.Similar observation was made on effects of independent variables on N-efficiency. The maximum efficiency was achieved as 259.1mg/kWh when power is in the range of 245 W and air flow rate in the range of 2.25 standard liter per minute.

Publications


    Progress 07/01/20 to 06/30/21

    Outputs
    Target Audience: 1. Research institutions and companies engaged in fertilizer research and production 2. Ordinary citizens who are interested in green nitrogen fertilizer production technologies 3. Nationally and internationally professional communities of fertilizer and soil health Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided?One graduatestudent and one undergraduate studenthavebeen hired and three otherundergraduate and graduate students havebeen trained and involved to conduct the project and related research work, which has been resulted in one peer-reviewed journal article and four conference paper/presentations. This project has provided opportunities forundergraduate and graduate students toprepare them for their career development in the academic and industrial comminities. How have the results been disseminated to communities of interest?The results have been disseminated as published peer-reviewed papers, conference papers, and conference and on-campus presentations. The results are also shared with the interested industry for potential collaboration for the scale-up and commercialization of the proposed technology. What do you plan to do during the next reporting period to accomplish the goals?In the next year, our work will be focused onevaluating and optimizing the liquid plasma reactor to determine the optimal operating conditions for efficient production of nitrogen fertilizer from air and water, in terms of process parameters including airflow rate, liquid flow rate, power, N2 and O2 ratio, as well as design parameters. The mechanism and reaction pathways of nitrogen fixation by CFLPPD will be determined.

    Impacts
    What was accomplished under these goals? Technical feasibility of nitrate and nitrite production by the continuous flow liquid-phase plasma discharge and influence of operating factors Variations of NO2 and NO3 (NOx, ditto) produced from air and water by the continuous flow liquid-phase plasma discharge (CFLPPD) system have been studied, based on which the technical feasibility was confirmed, and a few comments can be made for the influence of operating factors. First, the production of NOx increased with increasing power usage under all tested airflow rates in a largely linear manner. This was expected because increasing power supply would normally provide more energy to the plasma system, thus leading to increased reaction rates and improved product yields or treatment effects. Second, it was interesting to note that the CFLPPD system produced more NO3 than NO2 (the amount of the former was greater than about 2 times the latter). When the nitrogen gas in the air was oxidized by the strong oxidizing species, such as the hydroxyl radicals and H2O2 generated in large quantities by the plasma discharge, nitrite was expected to be formed in the first step of N2 oxidation. However, the existence of nitrite was transient, and as soon as it was generated, it would be immediately subjected to oxidation to nitrate by the abundant oxidizing species provided by the plasma discharge. It was reported that when O2 was copiously present, the formation of NO3 in water could proceed at a significantly higher rate. Since crops are in favor of nitrate as nitrogen fertilizer and nitrate is also considered a nutrient to improve soil quality, it is desirable to produce more nitrate than nitrite in the final effluent. That said, since nitrite can be further oxidized in the soil by soil microorganisms, a small amount of nitrite in the liquid should not pose a concern when the plasma-treated liquid is used as fertilizer. As a matter of fact, the nitrite to nitrate transformation in soils could take place without involving microorganisms. An early study revealed that when reactive manganese oxides were present, nitrite could be oxidized to nitrate in the presence or absence of atmospheric O2, which explained the seldom accumulation of nitrite in soils even when nitrifying bacterial numbers were low and the conditions for their growth were unfavorable. Third, the product yields of NOx apparently increased with the increase in air flow rate. And this increase showed a trend of continuing beyond the highest air flow rate examined in this study (2.0 L/min) because no slowdown or turning point was observed. This implies that the current experimental settings in terms of power and treatment times may be able to accommodate higher airflow rates than 2.0 L/min to produce more NOx. Further studies should be planned on increasing the airflow rate without increasing the power and treatment times to ascertain the maximal NOx yields for the CFLPPD system. Finally, it seemed that treatment times played a profound role in producing the NOx species by the CFLPPD system. As shown in Figure 2, as the treatment time increased from 20 min to 60 min, almost all treatments showed significant increases in NOx yields, regardless of airflow rate and power applied. The highest yields of NO3 and NO2 were observed for air flow rate at 2.0 L/min and power consumption at 300 W, which was 49.5, 75.8, and 97.5 mg/L for the former and 23.5, 35.0, and 38.7 mg/L for the latter under 20, 40, and 60 min treatments, respectively. However, the percent increases in yields were found to be reduced with the increases in treatment time. For instance, calculations of percent increases in yields using the same data showed that the NO3 yield increased by 53.13% and 28.63% corresponding to the treatment time increases from 20 to 40 min and from 40 to 60 min. This calculation can be performed on all the other experimental conditions with similar results achieved. It may therefore be concluded that increasing treatment time may not be as effective as increasing airflow rate with respect to increasing the NOx yields by the CFLPPD system examined in this study. Feasibility of nitrogen fixation to ammonium by CFLPPD As pure nitrogen gas was used as the gas reactant instead of air, it was expected that the product species in the solution will consist of ammonium ions besides nitrate and nitrite, based on the hypothesis that hydrogen ions and radicals from water ionization can react with nitrogen radicals by ionization of molecular nitrogen to produce ammonium. However, the actual results showed almost no ammonium ions in the treated solution from nitrogen gas and water, while the NOx ions are still dominant. In CFLPPD, the plasma discharge ionizes water to produce a high concentration of hydroxyl radical which possesses the highest oxidation capability. The existence of ammonium ions can be transient, and as soon as it was generated, it would be immediately subjected to oxidation to nitrate by the abundant oxidizing species provided by the plasma discharge in water. The commonly reported information in the literature on nonthermal plasma discharge for ammonia synthesis is from N2 and H2 with the assistance of catalysts by gas-phase plasma discharge. Given the current knowledge and level of development thus far, such a system is expected to be complex and requires the availability of expensive H2 in addition to readily available N2, which is unrealistic for most farms and can even pose a safety hazard due to the on-site storage of H2. Furthermore, the use of catalysts and the ability to recycle them constitute another hurdle to on-farm applications of the NTP process for ammonia synthesis. Therefore, it is concluded that the CFLPPD system is more suitable and economical for nitrogen fixation to NOx as fertilizer products.

    Publications

    • Type: Journal Articles Status: Published Year Published: 2021 Citation: Wu, S., B. Thapa, C. Rivera, Y. Yuan. 2021. Nitrate and nitrite fertilizer production using a continuous flow liquid-phase plasma discharge process. Journal of Environmental Chemical Engineering, 9(2): 104761. https://doi.org/10.1016/j.jece.2020.104761.
    • Type: Conference Papers and Presentations Status: Published Year Published: 2021 Citation: Wu, S., B. Thapa, R. Ndeddy Aka, Y. Yuan, C. Rivera, 2021. Production of Liquid Nitrogen Fertilizer by Air Activated Plasma Discharge in Water. ASABE 114th Annual International Meeting. Paper#: 2100284. Online. July 11-14, 2021.
    • Type: Conference Papers and Presentations Status: Published Year Published: 2021 Citation: Booker, T., S. Wu, B. Thapa, R. Ndeddy Aka. 2021. Liquid-phase Plasma Discharge Process for Green Nitrogen Fixation. University of Idaho Undergraduate Research Symposium, April 26, 2021.
    • Type: Conference Papers and Presentations Status: Published Year Published: 2020 Citation: Wu, S., B. Thapa, C. Rivera, Y. Yuan. 2020. Liquid-Phase Plasma Discharge for Producing Green Nitrogen Fertilizer from Air and Water. Nutrient Cycling, Soil Health, and Food Safety Conference Online. October 27-28, 2020.
    • Type: Conference Papers and Presentations Status: Published Year Published: 2020 Citation: Wu, S., B. Thapa. 2020. Liquid-Phase Plasma Discharge for Producing Green Nitrogen Fertilizer from Air and Water. ASABE 113th Annual International Meeting. Paper#: 2000940. Online. July 12-15, 2020.