The Journal of
the Korean Society on Water Environment

The Journal of
the Korean Society on Water Environment

Bimonthly
  • ISSN : 2289-0971 (Print)
  • ISSN : 2289-098X (Online)
  • KCI Accredited Journal

Editorial Office


  1. 목포대학교 환경공학과 (Dept. of Environmental Engineering, Mokpo National University)
  2. 전북대학교 정읍산학연협력지원센터, 생리활성소재과학과 (Center for Jeongeup Academy-Industry Cooperation, Dept. of Physically Active Material Science, Chonbuk National University)



Ammonium-Nitrogen, Fertilizer, Fugacity, Liquid manure, Livestock excretions.

1. Introduction

Since the ocean dumping of livestock’s excretions has been prohibited globally in 2012, many countries are concerned about resource recovery technology from livestock excretions. One of those technologies is transformation of livestock’s excretions into solid and liquid manure, which is including the same nutrients for crop production as commercial fertilizers. Before livestock manure is activated, people need to understand physical, chemical, and biological properties of manure primarily for safer and more effective management of manure. First of all, livestock manure consists of solid and liquid portions and organic and inorganic components containing feces, urine, wastewater, and runoff. For these reasons, pathogenic microorganisms and unwanted pests can live in manure environment. Common chemical compounds among 165 various compounds in manure emitted into atmosphere include Carbon dioxide (CO2), Methane (CH4), Ammonia (NH3), Hydrogen sulphide and related sulphur-containing compounds (H2S gas etc.), volatile organic acids, and nitrous oxide (N2O) depending on the type of manure and the way it's handled.

Manure has the potential to cause environmental problems such as emissions of odorous and greenhouse gases, contaminations of surface water and groundwater sources with nutrients and pathogens, contaminations of soil as loading nutrients and accumulating salt, and so on. Unlike manure contamination from manure piles as a point source, extra attention is required over application of manure as a non-point source. To minimize the environmental risks of manure, understanding fate of manure in environment is necessary. Foul-smelling odorous gases (NH3, N2O, N2, CH4, and H2S), mostly greenhouse gases (GHGs), are emitted from a spot into atmosphere and spread in broad space. Nitrogen components in manure can reduce safety and quality of environment harmfully. Nitrates in solution of manure runoff into surface water can cause excessive algae blooms and leaching into groundwater make it unable to drink as well as ammonia (NH3) in manure is toxic to aquatic organisms including fish in surface water bodies.

Fate of N components in a cycle has been investigated by many researchers in experimental studies and model simulation studies related to agriculture's role in N delivery into the environment in detailed reviews (Calderon et al., 2004; Dunn et al., 2004; Hubbard et al., 2004, Kim et al, 2009). According to previous studies mentioned above, excessive nutrients, especially nitrogen (N), can cause adverse effect on growth and production of crop in soil. N components in manure can negatively impact air, surface water, groundwater, and soil. Therefore, a study is necessary to establish fate of N components in manure related to negatively impacts on environment.

A fugacity concept has been introduced by Mackay in 1972 to understand the environmental behaviors of various chemicals in multi-media, considering terms of mass transfers including diffusion, precipitation, chemical reaction, biological decomposition, leakage, ingestion and dilution of nutrients required for the growth of plants, and water variation volume within each medium (MacKay, 1991). Also, an aqui-valence concept for non-volatile compounds and ionic chemicals is introduced by Mackay and Diamond in 1989 (MacKay et al., 1994) and recently it has been studied by many researchers (Batiha et al., 2008; Csiszar et al., 2011; Gandhi et al., 2007).

Since N-nutrient in animal liquid manure consists of high soluble, non-volatile and ionic compounds, an aquivalencebased model may be proper rather than a fugacity-based model but this study uses the fugacity-based model for simplification although it has uncertainty of model formulae, input information, and so on. Thus, this study aims at investigating the applicability of the fugacity concept originated by Mackay (1991) under a steady state condition as a tool to analyze environmental fate and transport of N components in liquid manure and to provide basis for improving management of N in the liquid manure system and for minimizing the environmental impacts of N during rice-cropping. The fugacity concept has been used in steady state condition for an air-waterrice plant-soil compartment system during rice cropping, simulated for fate of ammoniacal nitrogen (NH3-N) in manure, and evaluated its possibility during the rice cropping season. More details of model description and simulation description are in following sections.

2. Materials and Methods

2.1. Fugacity approach

The Level III fugacity model (FUGIII) includes processes of evaporation or volatilization to atmosphere, leaching via percolating water into groundwater, advection, diffusion, and degradation (or loss). The model assumes first-order kinetics for all reactions, a linear function of all movements, and local equilibrium between compartments. FUGIII will estimate concentrations (Ci) of the substance (manure NH3-N) in air, water, soil, and rice plant compartment systems as a function of fugacity fi and fugacity capacity Zi at the steady state condition of a mass balance equation given by Ci=fiZi, where Ci is the concentration of chemical substance (mol/m3), fi is the fugacity (Pa), and Zi is the capacity of fugacity or the proportionality constant (mol/m3·Pa). FUGIII deals with the distribution in a small quantity of a chemical substance between two compartments, i and j, under constant temperature and pressure, and non-equilibrium fugacity (f1 ≠ f2 ≠ f3 ≠ …… ≠ fn) in producing constant concentration ratio between two compartments, the partition coefficient kij defined as kij = Ci/Cj, where, Ci and Cj are the substance concentration in each compartment i and j respectively. The substance tends to accumulate in compartments depending upon the capacity of fugacity, which describes the affinity of the substance for the compartment. Thus, the fugacity capacity of each compartment has to be defined as considering the physicochemical properties of the substance for each compartment.

2.2. Governing equation

The rice-cropping system was modeled for air (i = a = 1), water (i = w = 2), soil (i = s = 3), and rice plant (i = r = 4) compartments. Since the model assumes the mass transfer of substance occurs from air to water and rice plants, from water to air and soil, from rice plants to air and soil and from soil to water and rice plants, governing equation for the mass balance of the substance is written by Eq.1. Table 1 presents a summary of mass balance equations in each compartment.

Table 1. Mass balance equations for each compartment in the model
Mass Balance Equations [mol/hr]

Air Compartment i = 1 Ei = Emissionrate of i compartment [mol/h]
QAiCBi = advection inflow [mol/h]
DAi = advection outflow [mol/h]
Nij = Diffusive flux between compartments i and j [mol/h]
Dij = Diffusionc oefficient between i and j [mol/h·Pa]
Fi = Fugacity of compartment i [Pa]
DRi = Reaction in compartment i [mol/h·Pa]
DLF = Litter fall [mol/h·Pa]
DGR = plant growth [mol/h·Pa]
DSF = uptake [mol/h] [mol/h·Pa]
D = total dispersion coefficient in soil [mol/h·Pa] Dothers = approximate removal by deposition and runoff (i.e.,Dothers=FiRothers)
F1DT1=E1+QA1CB1+N21+N41
DT1=(D12+D14+DA1+DR1)

Water Compartment i = 2
F2DT2=E2+QA2CB2+N12+N32+F1DA1
DT2=(D21+D23+DA2+DR2)

Soil Compartment i = 3
F3DT3=E3+QA3CB3+N23+F2DA2
DT3=(D32+DA3+DR3+DSF)

Rice Plant Compartment i = 4
F4DT4=E4+N14+F3DSF+F1DA1
DT4=(D41+DA4+DR4+DLF+DGR+Dothers)

It is assumed that rice plant growth balances litter fall, DGR = DLF.
(1)
E i + Advection i + Diffusion ij - Loss i = V i dC i dt

Considering the steady state condition,

(2)
V i dC i dt = I i + N i + i N ij - L i = 0
(3)
N i = Q 2 C i in - C i out
(4)
i N ij = i D ij f i - f j

where Input term Ii is emission Ei in each compartment i, mol/hr, Advection term Ni is mass flux by advection in compartment i, mol/hr, Diffusion term Nij is mass flux by diffusion in compartment i, mol/hr, where Dij is related to interfacial area Aij, fugacity capacity Zi and Zj, and mass transfer coefficient ki and kj in Table 2. Loss term Li is all mass fluxes by all removal processes such as reactions, deposition, runoff, leaching, uptake, litter fall, plant growth, and so on. However the removal process in this study is considered only leaching, uptake, litter fall, and plant growth, and a removal term with the approximate value, which is added instead of the deposition and runoff processes.

Table 2. Summary of Z-value and D-value used in the model
Terms Equations
Z-value Fugacity Capacity [mol/m3·Pa]
Air (i=1) Za=1/RT
Water (i=2) Zw=1/H ; H=(MwVp)/Sw
Soil (i=3) Zs=(Kpsρs)/H ; Kps=focs×0.41×Kow
Rice Plants (i=4) Zr=(Kprρr)/H ; Kpr=(Wp+Lp+Kbow)×(ρr/ρw)
R=8.314m3Pamol(-1)T(-1), T=(293+25)°K, H = Henry’s constant (Pa m3mol-1),
Mw = molar mass, Vp = vapor pressure, Sw = water solubility
Kps = partition coefficient for soil, Kpr = partition coefficient for rice plants
D-value [mol/h·Pa]
Advection outflow DAi D Ai = Z i Q Ai = Z i V i / τ i
Diffusivity in compartments between i and j, Dij D 12 = 1 k 12 × A 12 × Z 1 + 1 k 22 × A 12 × Z 2 - 1 D 23 = 1 k 23 × A 23 × Z 2 + Y 3 B 23 × A 23 × Z 2 - 1 D 14 = 1 D c + 1 D AB - F - 1
Reaction, DRi D Ri = Z i V ¯ i λ i = Z i V i ln 2 / τ 1 / 2
Litter fall, DFS-L D FS - L = k FL V F Z 4 , VF = PM F . AS / ρ F k FL = 1 / t R - F , D GR = D FS - L
Plant Growth DGR
Uptake, DSF D SF = T r A 14 L A TSCF Z 2 TSCF = 0.784 exp - log K OW 1.78 2 / 2.44
Zi = Fugacity capacity in the compartment, i [mol/m3·Pa]
QAi = Advection flow rate in the compartment, i [m3/h]
Vi = Volume of the compartment, i [m3]
τi = Residence time in the compartment, i [h]
k12 = Air-side MTC over water, [m/h]
k22 = Water-side MTC, [m/h]
Aij = Interface area between compartments i and j [m2]
DAB-F = Boundary layer diffusion ; Dc = Cuticle diffusion : kFL = the litter fall rate
VF = the volume of the foliage in vegetation compartment
PMF = a vegetation specific phyto-mass per unit ground area (kg [wet weight] /m2)
Tr = Transpiration rate = 1×10-5 [m/h]
LA = Leaf surface area = 5 [m2/m2]
TSCF = Transpiration stream cofactor (concentration)
* MTC (mass Transfer Coefficient)

The advection term considers only vertical transport in this case. The mass flux by advection in the compartment i is regarded as the linear process with a constant speed and expressed by Gi(CBi-Ci), where Gi (m3/h) is the matter flow, CBi is the concentration entering compartment i and Ci is the concentration leaving the compartment. The advection inflow (GAiCBi) is dealing with mass flow rate GAi and initial concentration in each compartment (CBi). Advection outflow (DAi) term is leaving from air and entering into water, leaving water and entering soil, and leaving from soil to groundwater. If i=2, dissolved components in water are leaving from water and entering into soil. The advection outflow (DAi) leaching from soil is expressed by vertical transport velocity U. The transfer coefficient by diffusion, D-value, (Dij, mol/h·Pa) between two compartments i and j is estimated by the expressions as shown in Table 2. In Table 2, the substance in the compartments can be also transformed by chemical reaction, biological degradation, dilution of the rice plant growth, and water variation volume in rice fields (Hu et al., 2013) and all reactions are assumed as first-order kinetics and reaction rate coefficients λi are determined by the half-life of the substance in compartment i, ti1/2; λi = ln(2)/ti1/2. The fugacity capacity and diffusivity for each one of these compartments and all removal processes are defined and summarized in Table 2. Further details for each term in Table 2 can be referred to literatures (Cousins and Mackay, 2000; Cousins and Mackay, 2001; MacKay, 1991).

2.3. Model parameters

Nitrogen components in manure includes nitrogen gas (N2), organic-nitrogen (Org-N), and inorganic-nitrogen such as ammoniacal nitrogen (NH4+-N or NH3-N), nitrite nitrogen (NO2--N), and nitrate nitrogen (NO3--N) with changing types in the nitrogen cycle process. To understand N-balance in liquid manure, N-balance model theory for Urea has been adopted from Chowdary et al. (2004) as shown in Fig. 1.

Fig. 1. Schematic representation of nitrogen balance model with reaction constants.
../../Resources/kswe/KSWE.2019.35.3.224/JKSWE-35-224_F1.jpg

For the model simulation, NH3-N among N components in manure is chosen and the mechanisms of NH3-N in manure have been applied to simulate the fate of N components in environmental media (air, water, soil, and rice plants) during rice cropping as shown in Fig. 2. As shown in Fig. 2, crops imbibe lots of nutrients from the soil. Nitrogen, mainly inorganic-N such as NH4+-N and NO3--N, is imbibed the most among those nutrients. Rice crops absorb NH4+-N well. It is not that the rice crops don't imbibe NO3--N but that NO3--N has less chance to get the effect as the manure because it is denitrified mostly in the rice field. Rice cropping occurs with water in the rice field and it provides the best advantage, productive stability by the water supply. In a submerged condition, root environment of the rice plant becomes a reduced state of soil.

Fig. 2. Schematic representation of the N-transformations in flooded rice field.
../../Resources/kswe/KSWE.2019.35.3.224/JKSWE-35-224_F2.jpg

Passing 1-2 weeks in the submerged condition, the water body in the rice field is divided into two layers, an oxidized layer or a floodwater zone with oxygen-rich water and a reduced layer or an aerobic zone with oxygen-poor water and the soil becomes an anaerobic zone saturated with water. Sometimes, the aerobic zone is thin enough to be ignored. In Fig.1, the reactions and reaction constants or their half-life in three zones are presented when applying quick-acting nitrogen liquid manure as basic manure in the rice field. In the floodwater zone and the aerobic zone, NH3-N(aq) in manure are transformed by hydrolysis to produce NH4+-N, volatilization to emit NH3(g), and nitrification to generate NO3--N. The denitrification process is very important when the soil is saturated with water because the microorganisms of the denitrification process act only in waterlogged soil without oxygen in the anaerobic layer.

The reactions progressed in the saturated anaerobic zone with water include denitrifcation of NO3--N to produce N2O and N2(g) into atmosphere and leaching of NO3--N into groundwater, mineralization to covert Organic-N into NH4+-N and immobilization to reduce NH4+-N to form Organic-N in the soil. Also, uptake of NH4+-N by rice plants roots is occurred around 30-40% of N. The losses of N are mainly caused by leaching into the groundwater and by release of N2 gas into atmosphere by the denitrification process with frequent rainfall during late springtime and early summertime. The denitrification progresses regardless of the manure and fertilizer or source of NO3--N such as degradation. Also, other factors of the denitrification acceleration includes crop residue to be used as a carbon source, warm soil, pH (neutral to alkalinity), and so on.

Table 3 contains significant parameters to calculate terms in mass balance equations as shown in Table 1 and Table 2. Values of parameters are taken from references marked in Table 3.

Table 3. Important parameters for the model calculation
Parameter Symbol Value Unit References

Phytomass in wet weight of foliage(rice plant) PMF (PMr) 1.0 kg/m2 MacKay, 1991
Density of foliage(rice plant) ρFr) 1030 kg/m3 Contreras et al., 2008
Leaf area index L 3 m2/m2 Larcher, 1995
Transpiration rate Tr 10-4 m3/m2·h Larcher, 1995
Total water flow rate transpired by rice plants Qw 8.7×10-5 m3/h Contreras et al., 2008
Average root length of rice plants δr 0.03 m Contreras et al., 2008
Volumetric fraction of water in rice plants Wp (xw) 0.80 Contreras et al., 2008
Volumetric fraction of lipids in rice plants Lp (xls) 0.02 Contreras et al., 2008
MTC for foliage air-boundary layer diffusion UAB-F 9 m/h Cousins and Mackay, 2001
Correction exponent for difference between plant lipids and octanol b 0.95
Soil density ρs 1540 kg/m3 Contreras et al., 2008
Soil organic carbon volumetric fraction ocs 0.17 Contreras et al., 2008
Water density ρw 999.5 kg/m3 Contreras et al., 2008
Height of water layer δw 0.3 m Contreras et al., 2008
Advection flow rate in water Gw 1.89×10-5 m3/h Voltolini et al., 2002
Reaction constant by Hydrology kh 0.744 h-1 Chowdary et al., 2004
Reaction constant by Volatilization kv 0.06 h-1 Chowdary et al., 2004
Reaction constant by Nitrification kn 0.08 h-1 Chowdary et al., 2004
Reaction constant by Mineralization km 0.002 h-1 Chowdary et al., 2004
Reaction constant by Immobilization kim 0.12 h-1 Chowdary et al., 2004
Reaction constant by Denitrification kd 0.18 h-1 Chowdary et al., 2004

2.4. Simulation condition

Physio-chemical properties of NH3-N in manure are important to run FUGIII and they are indicated in Table 4. Ammonia is in its pure gaseous state and also commercially or commonly available in an aqueous solution about 28– 30% NH3, which is almost saturated in water (Weast et al., 1988). Liquid manure used in this study contains 0.19% total nitrogen (TN) and 29.8% aqueous NH3-N of TN and 15.6% gaseous NH3 of TN. The temperature for simulation was 25°C (298°K). Also Table 4 and Table 5 present important input parameters for the model simulation. Table 5 includes major parameters to run the simulation.

Table 4. Physical and chemical property of NH3-N
Characteristic Information Reference

Chemical Name and synonym Ammonia, Anhydrous ammonia, AM-FOL, Ammonia gas, Liquid ammonia, Nitro-sil, R 717 Windholz et al., 1983
Chemical formular NH3
Molecular weight, MW 17.03g mol-1 LeBlanc et al., 1878
Vapor pressure, Vp 2.9 atm for Aqueous NH3 (28%) Daubert and Danner, 1989
Water solubility, Sw 0.52x106(20°C)gcm-3,mgL-1 Budavari et al., 1996
LogKOW 0.23 (estimated) USDHHS, 2004
LogKOC 0.155 (estimated) USDHHS, 2004
Table 5. Important input variables for the model simulation
Parameter Symbol Value Unit

Area of plantation Ar 100×42 m2
Amount Liquid Manure (NH3-N) Pd 1.01×102 mol m-2
Volume of Air Va 100×42×8 m3
Volume of water Vw 100×42×0.2 m3
Volume of Soil Vs 100×42×0.5 m3
Volume of Rice plants Vr 1400(A) × 0.12(H) m3
Average residence time of rice-cropping τr 240 hrs

3. Results and Discussion

After a certain amount of liquid manure (1.01×102 mol as NH3-N/m2) was sprayed under specific conditions as shown in Table 4 and 5, the model simulation was conducted for 10 days and the model results were analyzed and discussed in this section.

3.1. Fugacity Capacity

The model simulation estimated capacity of fugacity Zi, fugacity Fi for non-equilibrium each other (i.e., F1 ≠ F2 ≠ F3 ≠ F4), and concentration Ci in each compartment i (i = 1 ~ 4 for air, water, soil, and rice plants). Capacity of fugacity in each compartment, Zi, was calculated as a function of partition coefficient between compartments i and j, and physicochemical property of the substance NH3 and compartments (air, water, soil and rice plants). Zi is not time dependent so Zi of NH3 for each compartment is constant with time changes. Z1 is valued as 4.04 × 10-4 mol/m3·Pa for air, Z2 is 1.04 × 10-1 mol/m3·Pa for water, Z3 is 1.894 × 10-2 mol/m3·Pa for soil, and Z4 is 9.19 × 10-2 mol/m3·Pa for rice plants. As shown in Fig. 3, water compartment (Z2) took 48.3%, next was the rice plant compartment (Z4) with 42.7%, soil compartment had little about 8.8% (Z3), and the minimum value was found in the air compartment (Z1) less than 0.2%.

Fig. 3. Content of fugacity capacityZiin each compartment resulted from the model simulation. The values ofZiare 0.2% for air Z1, 48.3% for water Z2, 8.8% for soil Z3 and 42.7% for rice plant Z4.
../../Resources/kswe/KSWE.2019.35.3.224/JKSWE-35-224_F3.jpg

3.2. Variation of Fugacity and Concentration

During all simulations, the same amount of emission was used but emission rates were different depending upon different detention times. Fugacity and concentration for all compartments except the rice plant compartment were decreased linearly with the detention time change in the log-log graph but those for the rice plant compartment were performed nonlinearly in the log-log graph. Fig. 4 and Fig. 5 present the log-log graph between fugacity and different detention times in (a) and between concentration and different detention times in (b). The detention times were applied from 1 hour to 20 days with one time emission of manure initially. Fig. 4 is the case that the value of other removal term is same as that of uptake from soil, Rothers = RSF, and Fig. 5 is the case that the removal term for the rice plant compartment is ignored, Rothers = 0. In Fig. 4(a) and Fig. 5(a), fugacity values from the highest to the lowest were found in air, water, soil, and rice plant compartment orderly until 2 days and 1 day respectively. After that day, fugacity in soil (F3) was lower than fugacity in rice plant (F4).

Fig. 4. Changes of Fugacity and concentration in each compartment for different detention times from 1hour to 20 days.
../../Resources/kswe/KSWE.2019.35.3.224/JKSWE-35-224_F4.jpg
Fig. 5. Changes of Fugacity and concentration in each compartment for different detention times from 1hour to 20 days when the removal process in the rice plants was ignored.
../../Resources/kswe/KSWE.2019.35.3.224/JKSWE-35-224_F5.jpg

Unlike the fugacity, the highest concentration was determined in water, next was in soil and rice plant, and air detected the lowest values in Fig. 4(b) and Fig. 5(b). Concentrations between soil and rice plants were exchanged after 0.15 days and the concentration in rice plants was greater than the concentration in the soil and closed to the concentration of water with time increase, and the most concentration of NH3 was remained in the water compartment in Fig. 4(b) but in Fig. 5(b) the rice plants took NH3-N mostly after 7 days. As shown in Fig. 4 and Fig. 5, changes of fugacity and concentration in the rice plants were depending on the removal term considerably.

3.3. Mass Balance

Fig. 6 shows the mass balance with values for all processes of the model equation graphically. Units of all values in Fig. 6 were [mol/hr] and the values between gain and loss for each compartment were matched well. In the compartment of air, the gain was from emission and diffusion from water to air, and the loss was caused by the diffusion from air to water and transformation in the compartment. The water compartment was mostly affected by emission and diffusion from air to water for the gain and by transformation and diffusion from water to air for the loss. The mass in the soil compartment was balanced with the gain from diffusion from water to soil and the loss from transformation and diffusion from soil to water. The rice plants were gained by uptake of NH3-N from the soil and lost by diffusion from rice plants to air and by removal processes. The removal processes in the rice plants were not described in details but assumed the same value of uptake from soil.

Fig. 6. Graphical representation of mass balance (mol/hr) in and between compartments.
../../Resources/kswe/KSWE.2019.35.3.224/JKSWE-35-224_F6.jpg

The analysis of mass balance using Level III shown in Figure 6 can yield considerably realistic results. It can scientifically identify, quantify, and diagnose the fate of nutrients in agricultural land, the description of fate mechanism, and the analysis of mass balance, thereby preventing the excessive use of liquid manure, and inducing natural-friendly agriculture. Based on the model studying, the fate of nutrients in liquid manure in the environmental media can be understood. It can be applied to create accurate inventory for liquid manure, to control total amount of nutrients for plant growth, to quantify and minimize the nonpoint pollutants, and to quantify the pollution load affected on water quality adversely.

4. Conclusions

A series of model simulation using the fugacity concept under a steady state condition was carried out to analyze environmental fate and transport of N components in liquid manure and to provide basis for improving management of N in the liquid manure system for minimizing the environmental impacts of N during rice-cropping. Findings of the model simulation are as in the following:

  1. Model sensitivity was depending on input parameters and physicochemical properties of NH3-N in manure, which were used to calculate capacity of fugacity, Zi and partition coefficients for each compartment. Zi was not time dependent and had each constant value for each compartment. For NH3-N, most of Zi were distributed in the water body and the rice plants.

  2. Fugacity and concentration for air, water, and soil were decreased linearly with time change in the log-log graph but those in rice plants were performed nonlinearly.

  3. Most of NH3-N was remained in the water body when the removal processes (deposition and runoff) in the rice plants were considered approximately, while the rice plants took NH3-N when the removal processes are ignored.

  4. The mass balance of N or N-budget among the compartments is produced by the Level III fugacity model.

The present study has the following limitations: the model calibration by the actual observation data is not performed and the residual amount and nitrogen type change by the soil layer are not described, and the model simulation is considered as continuous emission input unlike intermittent actual emission input. Therefore, more specific and ongoing modeling and monitoring studies are required to quantify the impact of liquid manure as a non-point pollutant on water quality. Based on the simulation results, the further study is required to describe more precise removal process in the Level III fugacity model with proper values of input parameters, to simulate the model for various N-typed fertilizers, to compare simulation results between the liquid manure and various N-typed fertilizers, and to evaluate the model with observation data of N components.

요약

액비(분뇨)에 포함된 질소성분은 환경의 질을 악화시키고 안정성을 감소시킬 수 있다. 액비로 인한 환경적 위해성을 최소화하기 위해서는 환경 매체 내에서의 액비의 거동을 이 해할 필요가 있다. 액비에 포함된 암모니아성 질소(NH3-N) 의 환경 내 거동과 이송을 분석하고, 액비시스템에서 질소 (N)관리의 개선을 위한 기반을 제공하며 질소의 환경에 미치 는 악영향을 최소화하기 위해서, 본 연구는 단순화된 Level III fugacity 모델의 적용 가능성을 조사하는 것을 목적으로 하였다. 벼 재배 기간 중 4개의 환경구획(공기, 물, 토양 및 벼)에서 암모니아성 질소(NH3-N) 성분을 축적하기 위해 정 상상태의 fugacity 개념을 이용한 모델의 모의 실험을 실시 하였으며 그 결과 Level III fugacity 모델의 적용 가능성을 검증하였다. 모델 결과, 대부분의 암모니아성 질소(NH3-N)는 논물(수체)과 벼(식물)에 분포하였으며 공기와 논물 그리고 토양에 대한 로그-로그 그래프선상에서 fugacity와 농도는 시 간에 따라 선형적으로 감소한 반면에 벼(식물)에서의 변화는 비선형적으로 나타났다. 제거과정의 민감성을 살펴본 결과 제거과정(침적과 유출)이 고려된 경우 대부분의 암모니아성 질소는 논물에 분포하였으며 제거과정이 무시된 경우에는 벼(식물)가 암모니아성 질소를 흡수하는 것으로 나타났다. 또한 질소의 물질수지에 따라 각 구획별로 질소가 분포됨을 알 수 있었다. 본 연구는 실제 관측 자료에 의한 모델 보정 을 수행하지 않고 토양층에 의한 잔류량 및 질소 형태의 변 화를 기술하지 않았으며 모델 시뮬레이션은 간헐적인 실제 배출량 입력과 달리 연속 배출량으로 간주하였다 . 그러므로 수질에 대한 비점 오염원으로서의 액비의 영향을 정량화하 기 위해서는 보다 구체적이고 지속적인 모델링 및 모니터링 연구가 필요하다. 향후 연구의 Level III fugacity 모델에서는 더 정확한 제거 과정을 기술하고, 입력 변수의 적절한 값을 적용하여 다양한 N 형 비료에 대한 모델 시뮬레이션을 실시 하고, 액비와 다양한 N 형 비료를 사용하여 얻은 N 성분의 관측 자료를 이용하여 모델을 평가할 것이다.

Acknowledgement

This work was funded by the Jeonbuk Green Environment Center (JBGEC) and partly supported by the National Research Foundation of Korea (NRF: NRF-2019R1A2C1006441) with grants from the Ministry of Education in Korea.

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