Environmental Fate Tracking of Manure-borne NH3-N in Paddy Field Based on a Fugacity Model
Fugacity 모델에 기초한 논토양에서의 액비살포에 따른 암모니아성 질소 거동추적
김미숙
(Mi-Sug Kim)
1iD
곽동희
(Dong-Heui Kwak)
2†iD
-
목포대학교 환경공학과
(Dept. of Environmental Engineering, Mokpo National University)
-
전북대학교 정읍산학연협력지원센터, 생리활성소재과학과
(Center for Jeongeup Academy-Industry Cooperation, Dept. of Physically Active Material
Science, Chonbuk National University)
© Korean Society on Water Environment. All rights reserved.
Key words(Korean)
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.
|
Considering the steady state condition,
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.
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.
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)
|
ρF (ρr)
|
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.
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.
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.
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.
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:
-
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.
-
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.
-
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.
-
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.
References
Batiha M.A., Kadhum A.A.H., Mohamad A.B., Takriff M.S., Fisal Z., Daud W.R.W., Batiha
M.M., 2008, MAM-an aquivalence-based dynamic mass balance model for the fate of non-volatile
organic chemicals in the agricultural environment, American Journal of Engineering
and Applied Sciences, Vol. 1, No. 4, pp. 252-259

1996, The Merck Index, Merck & Co., Inc
Calderόn F.J., McCarty G.W., Van Kessel J.A.S., Reeves J.B., 2004, Carbon and nitrogen
dynamics during incubation of manured soil, Soil Science Society of America Journal,
Vol. 68, pp. 1592-1599

Chowdary V.M., Rao N.H., Sarma P.B.S., 2004, A Coupled soil water and nitrogen balance
model for flooded rice fields in India, Agriculture, Ecosystems and Environment, Vol.
103, pp. 425-441

Contreras W.A., Ginestar D., Paraiba L.C., Bru R., 2008, Modelling the pesticide concentration
in a rice field by a level IV fugacity model coupled with a dispersion- advection
equation, Computers and Mathematics with Applications, Vol. 56, pp. 657-669

Cousins I.T., Mackay D., 2000, Transport parameters and mass balance equations for
vegetation in Level III fugacity models, http://www.trentu.ca/academic/aminss/envmodel/CEMC200001.pdf,
Internal report published on the website of the Canadian Environmental Modeling Centre

Cousins I.T., Mackay D., 2001, Strategies for including vegetation compartments in
multimedia models, Chemosphere, Vol. 44, pp. 643-654

Csiszar S.A., Gandhi N., Alexy R., Benny D.T., Struger J., Marvin C., Diamond M.L.,
2011, Aquivalence revisited-New model formulation and application to assess environmental
fate of ionic pharmaceuticals in Hamilton harbor, Lake Ontario, Environment International,
Vol. 37, pp. 821-828

Daubert T.E., Danner R.P., 1989, Physical and thermodynamic properties of pure chemicals:
Data compilation, Taylor & Francis
Dunn S.M., Vinten A.J.A., Lilly A., DeGroote J., Sutton M.A., McGechan M., 2004, Nitrogen
risk assessment model for Scotland: I. Nitrogen leaching, Hydrology and Earth System
Sciences, Vol. 8, pp. 191-204

Gandhi N., Bhavsar S.P., Diamond M.L., Kuwabara J.S., Marvin-Dipasquale M., Krabbenhoft
D.P., 2007, Development of a mercury speciation, fate, and biotic uptake (BIOTRANSPEC)
model: application to Lahontan reservoir (Nevada, USA), Environmental Toxicology and
Chemistry, Vol. 26, No. 11, pp. 2260-2273

Hu Y., Wang D.Z., Zhang C., Wang Z.S., Chen M.H., Li Y., 2013, An interval steady-state
multimedia aquivalence (ISMA) model of the transport and fate of chloridion in a surface
flow constructed wetland system treating oil field wastewater in China, Ecological
Engineering, Vol. 51, pp. 161-168

Hubbard R., Sheridan J.M., Lowrance R., Bosch D.D., Vellidis G., 2004, Fate of nitrogen
from agriculture in the southeastern Coastal Plain, Journal of Soil and Water Conservation,
Vol. 59, pp. 72-86

Kim J., Kim B., Shin M., Kim J.K., Jung S., Lee Y., Park J.H., 2009, The distribution
of nitrogen and the decomposition rate of organic nitrogen in the Youngsan River and
the Sumjin River, Korea, Journal of Korean Society on Water Environment, Vol. 25,
pp. 135-143

Larcher W., 1995, Physiological Plant Ecology, Springer
LeBlanc J.R., Madhavan S., Porter R.E., 1978, Ammonia. In Kirk-Othmerencyclopedia
of chemical technology, John Wiley & Sons, Inc, pp. 470-516
MacKay D., 1991, Multimedia environmental models: The fugacity approach, Lewis Publishers
Mackay D., Sang S., Vlahos P., Gobas F., Diamond M., Dolan D., 1994, A rate constant
model of chemical dynamics in a Lake ecosystem: PCBs in lake Ontario, Journal of Great
Lakes Research, Vol. 20, No. 4, pp. 625-642

U.S. Department of Health and Human Services (USDHHS), 2004, http://www.atsdr.cdc.gov/toxprofiles/tp126.pdf,
Toxicological profile for ammonia, Public Health Service Agency for Toxic Substances
and Disease Registry
Voltolini J., Althoff D.A., Back A.J., 2002, Água de irrigaçao para a cultura do arrozirrigado
no Sistemaprégerminado, [in Portuguese], In: Arrozirrigado: Sistema pré-germinado,
pp. 101-112
1988, CRC Handbook of chemistry and physics, CRC Press, Inc
Windholz M., Budavari S., Blumetti R.F., Otterbein E.S., 1983, The Merck index, Merck
& Co., Inc