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IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 448
DISPERSION MODELING OF NITROUS OXIDE EMISSIONS FROM A
NITRIC ACID PLANT IN DEVNYA REGION, BULGARIA
Maya Stefanova1
, Rozalina Chuturkova2
, Evgeni Sokolovski3
, Nina Ilieva4
1
PhD Student, Department of Ecology and Environmental Protection, Technical University, Varna, Bulgaria
2
Associate Professor, Department of Ecology and Environmental Protection, Technical University, Varna, Bulgaria
3
Chief Assistant Professor, Department of Engineering Ecology, University of Chemical Technology and Metallurgy,
Sofia, Bulgaria
4
Chief Assistant Professor, Department of Engineering Ecology, University of Chemical Technology and Metallurgy,
Sofia, Bulgaria
Abstract
Within the present research a mathematical modeling is done in order to study the dispersion of nitrous oxide emissions from a single
organized source โ€“ a nitric acid plant with 363000 tons per year production capacity in the industrial region of Devnya, Bulgaria.
Separate simulations are done for the dispersion of N2O emissions without any emission reduction measures being implemented in the
plant and for N2O emission dispersion with a secondary N2O decomposing catalyst being installed under different meteorological
conditions. Results indicate that a significant decrease of N2O concentration in the ground atmospheric layer is achieved after the
implementation of the secondary decomposing catalyst โ€“ over 81 % reduction of the hourly average N2O concentration and up to 80
% reduction of the annual average N2O concentration is calculated. Dispersion models also indicate that the territorial dispersion of
N2O emissions is reduced as well โ€“ the area with N2O concentration below 200 ยตg/m3
is 15 times smaller with a secondary N2O
decomposing catalyst being installed. Research results provide a tool to assess the decomposing catalyst reduction potential and to
predict the impact of N2O emissions upon the ambient air quality in the source region. Research results prove that high temperature
catalytic reduction of N2O emissions from nitric acid production by installing secondary decomposing catalyst is an effective method
for N2O emission reduction and a tool to combat global warming effect.
Keywords: ambient air quality, air dispersion modeling, greenhouse gas, nitrous oxide, catalytic emission reduction
-----------------------------------------------------------------------***-----------------------------------------------------------------------
1. INTRODUCTION
Nitrous oxide N2O is a greenhouse gas under the Kyoto
Protocol [1] and one of the main reasons for global warming
effect [2-4]. N2O emissions from industrial installations for
nitric acid production have adverse effect upon the ambient air
quality in the surrounding area. The effect level depends on
the specific topographic and climate conditions of the source
region which also affect the dispersion of the pollutant in the
ground atmospheric layer and the processes of photo
dissociation, chemical destruction and diffusion [5, 6].
Different measures and techniques for N2O emission reduction
are developed and applied in nitric acid production plants
around the world [7-9]. Installing a non-platinum secondary
catalyst that is decomposing N2O to nitrogen and oxygen right
after its formation in the ammonia burner is a secondary
measure that provides 73 % reduction of N2O emissions [10].
The achieved N2O reduction level has a positive effect upon
the ambient air quality in the industrial source surrounding
area and is a tool to prevent adverse changes of the global
climate system.
The present research aim is to study the dispersion of N2O
emissions from a nitric acid plant with and without a
secondary decomposing catalyst being installed and to assess
their impact upon the ambient air quality in the surrounding
area having in mind the specific topographic and
meteorological conditions of the region.
2. MATERIAL AND METHODS
Within the present research a mathematical modeling is done
along with a software simulation of the dispersion of N2O
emissions from a single fixed source โ€“ a nitric acid plant with
363000 tons per year production capacity in the industrial area
of Devnya, Bulgaria. A secondary decomposing catalyst for
N2O emission reduction has been installed in the plant in
September 2005 [10]. According to the European Environment
Agency currently there is no specific software product
developed for mathematical modeling of N2O emission
dispersion due to the fact that N2O is inert in the troposphere
[11-17] and thus all dispersion models for emissions from
area, transport or point sources in urban regions can not be
applied [18, 19]. Within this research a practically approbated
software product BREEZE AERMOD is used for emission
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 449
dispersion modeling taking into account the topography of the
region. In order to ensure maximum reliability of the
meteorological conditions of the region validated data is used
in the form of hourly meteorological file containing
information on 6 parameters โ€“ wind speed and direction,
ambient air temperature, relative humidity, atmospheric
pressure, sun radiation intensity. Research period starts in
2005, due to the fact that before that year there arenโ€™t N2O
emission reduction measures applied in the nitric acid plant,
and ends in 2012.
In order to avoid obtaining of wrong results due to variation of
the meteorological conditions N2O emission dispersion
modeling is done over two main scenarios. The first scenario
presents N2O emission dispersion with no N2O reduction
measures being applied in the nitric acid plant. The other
scenario presents N2O emission dispersion with a secondary
N2O decomposing catalyst being installed in the plant.
Emission dispersion with no N2O reduction measures being
applied is simulated using data from a single N2O emission
measurement in 2005 before the implementation of the
secondary catalyst and meteorological data for 2005 and 2012.
Emission dispersion with a secondary N2O decomposing
catalyst being installed is simulated using emission data in the
form of hourly N2O concentration file for 2012 and
meteorological data for 2005 and 2012. For every of the four
simulations hourly average and annual average N2O
concentration in the ground atmospheric layer are calculated
referring to European and national standards for determination
of hourly average and annual average limit values for the
content of oxides of nitrogen in the ambient air [20, 21].
3. RESULTS AND DISCUSSION
3.1. Topographic Characteristic of the Region
The nitric acid plant is located in the east industrial area of
Devnya, Bulgaria. The terrain is mostly lowland with some
hilly areas and the elevation varies between 0 and 300 m. The
highest point in the 5 km radius area is to the north-northwest
from the source. To the south, where Beloslav Lake is
situated, the terrain is flat. The nearest settlement is
Povelyanovo, a suburb of Devnya (to the north). Other
settlements in the area are Razdelna, Beloslav and
Strashimirovo with elevation almost equal to the elevation of
the source site. Settlements to the north from the source such
as Slanchevo (elev. 145 m), Kipra (elev. 135 m) and Banovo
(elev. 340 m) can be affected by the emission dispersion.
These settlements are situated in hilly areas where
displacement is higher or almost equal to the geometric height
of the source and for that reason certain meteorological
conditions may cause increased pollutant concentrations in the
ambient air. Fig-1 presents a topographic map of the source
region.
Fig-1: Topographic map of the source region
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 450
3.2 Climate and Meteorological Conditions of the
Region
The climate of the source region is typical for its long and dry
summer with high coefficient of windless periods and small
rainfall quantity. Winter period is short and relatively soft with
greater percentage and quantity of rainfall than summer
period. There are breeze currents with east โ€“ west direction
circulating along Varna Lake and Beloslav Lake. At day time
breeze currents come from east while at night they come from
west. Moderate winds are typical for the region. The terrain
advantages the formation of inversion fog and considerable
pollution of the ambient air. Statistical data indicates that
about 60 % of calendar days are foggy.
Fig-2 and Fig-3 present wind roses built for the source region
for 2005 and 2012. Both figures indicate that most winds
come from southeast with speed varying from 1.54 to 3.09
m/s. Winds with speed over 5.14 m/s are very unusual and
mostly come from north-northeast. The percentage of windless
periods is very low.
Fig-2: Wind rose for 2005 Fig-3: Wind rose for 2012
3.3 Results
Within the present research a single organized source of N2O
emissions is studied โ€“ P1 stack at the nitric acid plant. The
height of the stack is 130 m and the diameter is 1.44 m. Due to
the fact that N2O is inert in the troposphere and emissions are
expected to expand on long distance from the source the study
area is determined with the following proportions โ€“ 20000 m
on west โ€“ east direction and 10000 m on south โ€“ north
direction. The density of the recipients with a certain N2O
concentration is 41 recipients on x (east) and 21 recipients on
y (north) with 500 m step or the total amount of the recipients
is 861.
Using BREEZE AERMOD software a simulation of N2O
emission dispersion is done. Hourly average and annual
average N2O concentration in the ground atmospheric layer
are calculated.
Table-1 indicates calculation results for peak values of hourly
average N2O concentration, recipientsโ€™ coordinates and
elevation and date/time when peak values are obtained.
ะขable-1: Peak values of hourly average N2O concentration (ฮผg/m3
)
Avg
.
Per.
Hig
h
Type Val
Date UTM Elev.
Hil
l
Ht.
Flag
Ht.
Rec.
Typ
e
Grid ID
YYMMDD
HH
East (m) North (m) (m) (m) (m)
Simulation without secondary catalyst being installed and meteorological data for 2005
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 451
1HR 1ST
Avg.
Conc.
301.96247 5/09/17/18
553291.9
5
4783610.56 0 0 2 GC R0G02000
Simulation without secondary catalyst being installed and meteorological data for 2012
1HR 1ST
Avg.
Conc.
16705.48516 12/10/28/01 553785.9 4784607.48
155.
1
209 2 GC MN101000
Simulation with secondary catalyst being installed and meteorological data for 2005
1HR 1ST
Avg.
Conc.
117.69145 5/01/19/10
554791.9
5
4783610.56 0 0 2 GC R0G02000
Simulation with secondary catalyst being installed and meteorological data for 2012
1HR 1ST
Avg.
Conc.
3126.84989 12/01/25/05 553785.9 4784607.48
155.
1
209 2 GC MN101000
As indicated in Table-1 results show a significant decrease of
hourly average N2O concentration in the ambient air after the
implementation of the secondary decomposing catalyst.
Simulation without secondary catalyst being installed and
meteorological data for 2005 indicates that the peak value of
hourly average N2O concentration is 302 ยตg/m3
while
simulation with secondary catalyst being installed and
meteorological data for the same year indicates hourly average
N2O concentration of 117.7 ยตg/m3
which is 2.5 times lower.
Simulation without secondary catalyst being installed and
meteorological data for 2012 indicates that the peak value of
hourly average N2O concentration is 16705.5 ยตg/m3
while
simulation with secondary catalyst being installed and
meteorological data for the same year indicates hourly average
N2O concentration of 3126.8 ยตg/m3
which means 81 %
reduction of N2O level in the ambient air. Specific
meteorological conditions in 2012 (e.g. ambient air
temperature, atmospheric stability class determined by the
mixing height, sun radiation, etc.) need to be emphasized
leading to higher N2O concentrations in the ground
atmospheric layer. Simulation with secondary catalyst being
installed and meteorological data for 2012 indicates that the
peak value of hourly average N2O concentration in the ground
atmospheric layer is 10 times higher than the peak value of the
simulation without secondary catalyst being installed and
meteorological data for 2005. This proves the necessity of
modeling 4 simulations for every combination of
meteorological data and process conditions.
Figures 4 โ€“ 7 present contours of hourly average N2O
concentration (ยตg/m3
) in the ground atmospheric layer for
every simulation.
Fig -4: Hourly average N2O concentration (ฮผg/m3
) without secondary catalyst being installed and meteorological data for 2005
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 452
Fig -5: Hourly average N2O concentration (ฮผg/m3
) without secondary catalyst being installed and meteorological data for 2012
Fig-6: Hourly average N2O concentration (ฮผg/m3
) with secondary catalyst being installed and meteorological data for 2005
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 453
Fig-7: Hourly average N2O concentration (ฮผg/m3
) with secondary catalyst being installed and meteorological data for 2012
The peak value of hourly average N2O concentration for
simulation without secondary catalyst being installed and
meteorological data for 2005 is obtained at 18.00 h on 17
September 2005 with southeast wind blowing with speed 2.53
m/s (Table-1 and Fig-4) while the peak value for simulation
with secondary catalyst being installed and meteorological
data for the same year is obtained in January with west-
northwest wind blowing with speed 0.5 m/s (Table-1 and Fig-
6). Logically the implementation of the secondary
decomposing catalyst leads to 61 % decrease of the hourly
average N2O concentration due to significant N2O emission
reduction at the nitric acid plant.
Peak values of hourly average N2O concentration in the
ground atmospheric layer for both simulations with
meteorological data for 2012 are obtained with south wind
blowing with speed 2 m/s โ€“ in October for simulation without
secondary catalyst being installed (Table-1 and Fig-5) and in
January for simulation with secondary catalyst being installed
(Table-1 and Fig-7). Both peak values are registered in the
same recipient with higher elevation than the source height.
Excluding the impact of the adverse meteorological conditions
in 2012 a significant decrease of hourly average N2O
concentration is calculated โ€“ over 81 % reduction for
simulation with secondary catalyst being installed compared to
simulation without secondary catalyst being installed. Beside
N2O concentration decrease a significant reduction of N2O
dispersion area in the atmosphere is observed. As indicated on
Fig-5 and Fig-7 the area with hourly average N2O
concentration below 200 ฮผg/m3
[20, 21] is 29 km2
for
simulation without secondary catalyst being installed and less
than 2 km2
for simulation with secondary catalyst being
installed.
Peak values of annual average N2O concentration and
recipientsโ€™ coordinates and elevation are presented in Table-2.
Table-2: Peak values of annual average N2O concentration (ฮผg/m3
)
High
Avg.
Conc.
UTM Elev. Hill Ht. Flag Ht. Rec.
Type
Grid ID
East (m) North (m) (m) (m) (m)
Simulation without secondary catalyst being installed and meteorological data for 2005
1ST 8.92915 553291.95 4783610.56 0 0 2 GC R0G02000
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 454
Simulation without secondary catalyst being installed and meteorological data for 2012
1ST 48.37149 551285.9 4785607.48 157.2 260 2 GC MN101000
Simulation with secondary catalyst being installed and meteorological data for 2005
1ST 2.11113 553291.95 4783610.56 0 0 2 GC R0G02000
Simulation with secondary catalyst being installed and meteorological data for 2012
1ST 9.57512 551285.9 4785607.48 157.2 260 2 GC MN101000
Results in Table-2 indicate that annual average N2O
concentration in the ground atmospheric layer is over 8.9
ฮผg/m3
for simulation without secondary catalyst being
installed and meteorological data for 2005 and 2.1 ฮผg/m3
for
simulation with secondary catalyst being installed and
meteorological data for the same year which is over 4 times
lower. For simulation with secondary catalyst being installed
and meteorological data for 2012 annual average N2O
concentration is 9.6 ฮผg/m3
which is over 5 times lower than
the peak value for simulation without secondary catalyst being
installed and meteorological data for the same year.
Comparison between simulations with and without secondary
catalyst being installed and meteorological data for 2005
indicates that 76.4 % reduction of annual average N2O
concentration has been achieved. Comparison between both
simulations with meteorological data for 2012 indicates 80.2
% reduction of annual average N2O concentration.
Figures 8 - 11 present contours of annual average N2O
concentration (ยตg/m3
) in the ground atmospheric layer for
every simulation
Fig-8: Annual average N2O concentration (ฮผg/m3
) without secondary catalyst being installed and meteorological data for 2005
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 455
Fig-9: Annual average N2O concentration (ฮผg/m3
) without secondary catalyst being installed and meteorological data for 2012
Fig-10: Annual average N2O concentration (ฮผg/m3
) with secondary catalyst being installed and meteorological data for 2005
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 456
Fig-11: Annual average N2O concentration (ฮผg/m3
) with secondary catalyst being installed and meteorological data for 2012
As indicated on Figures 8 โ€“ 11 annual average N2O
concentration in the ground atmospheric layer depends
strongly on the meteorological conditions of the region.
Adverse meteorological conditions in 2012 affect the
dispersion of N2O emissions thus causing 4 times higher
annual average N2O concentrations than peak values
calculated for simulations with meteorological data for 2005.
Although meteorological conditions have considerable
influence upon N2O emission dispersion a significant decrease
of annual average N2O concentration is registered after the
implementation of the secondary decomposing catalyst in the
nitric acid plant. By analogy with the results obtained for
hourly average N2O concentration modeling annual average
N2O concentration in the atmosphere proves significant
decrease of N2O emission dispersion area. As presented on
Fig-8 and Fig-10 the area with annual average N2O
concentration below 2 ฮผg/m3
is over 20 km2
for simulation
without secondary catalyst being installed while for simulation
with secondary catalyst being installed N2O concentration
below 2 ฮผg/m3
is registered on a small area directly next to the
emission source.
4. CONCLUSIONS
Research results indicate a significant decrease of N2O
concentration in the ground atmospheric layer after the
implementation of the secondary decomposing catalyst in the
nitric acid plant โ€“ 71 % average reduction of hourly average
N2O concentration and 78 % average reduction of annual
average N2O concentration for all the simulations done.
Beside the reduction of N2O concentration a significant
decrease of N2O emission dispersion area in the ground
atmospheric layer is observed. Research results prove the
reduction potential of the secondary decomposing catalyst and
the positive effect of N2O emission reduction upon ambient air
quality in the source region. On that basis a conclusion is
made that nitric acid plants with similar parameters can be
situated directly next to urban areas without causing adverse
effect upon ambient air quality having in mind the topography
of the region and possible cumulative effect with other air
pollutant sources [22]. High temperature catalytic reduction of
N2O emissions from nitric acid production is proved to be an
effective measure for atmospheric N2O concentration decrease
and a tool to combat adverse changes of global climate
system.
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 457
REFERENCES
[1] The Kyoto Protocol to the United Nations Framework
Convention on Climate Change, 1998
[2] Ravishankara A. R., Daniel J. S., Portmann R. W.
Nitrous Oxide: The Dominant Ozone-Depleting
Substance Emitted in the 21st Century. Science, Vol.
326 (5949), 123, 2009
[3] Petrova D., Kostadinova P., Sokolovski E., Dombalov
I. Greenhouse Gases and Environment. Journal of
Environmental Protection and Ecology, Vol. 7 (3), 679,
2006
[4] Wuebbles D. J. Nitrous Oxide: No Laughing Matter.
Science, Vol. 326 (5949), 56, 2009
[5] Chuturkova R., Stefanova M. Assessment of the Effect
of Nitrous Oxide Emissions from Nitric Acid
Production upon Ambient Air Quality in Devnya
Region. Journal Scientific and Applied Research, Vol.
4, 163, 2013
[6] McElroy M. B., McConnel J. C. Nitrous oxide โ€“ a
natural source of stratospheric NO. Journal of
Atmospheric Sciences, Vol. 28 (6), 1095, 1971
[7] European Comission, Integrated Pollution Prevention
and Control. Reference Document on BAT for the
manufacture of Large Volume Inorganic Chemicals โ€“
Ammonia, Acids and Fertilizers, 2007
[8] Agency for Energy and the Environment. Reduction of
Nitrous Oxide in the Nitric Acid Industry. The Hague,
2001
[9] Stefanova M. Industrial Methods for Nitrous Oxide
Emission Reduction. Ecological Engineering and
Environment Protection, Vol. 12 (3-4), 89, 2013 [In
Bulgarian]
[10] Stefanova M., Chuturkova R. Nitrous Oxide Catalytic
Reduction at a Nitric Acid Plant in Bulgaria. Environ.
Prot. Eng., 2014 (in press)
[11] Vallero D. A. Fundamentals of Air Pollution.
Academic Press, Burlington, MA, USA, 2007
[12] Tinsley I. J. Chemical Concepts in Pollutant Behavior.
Willey, NJ, USA, 2004
[13] Kaur H. Environmental Chemistry. Global Media,
Meerut, IND, 2010
[14] Bhagi A. K., Chatwal G. R. Environmental Chemistry.
Global Media, Mumbai, IND, 2010
[15] Bailey R. A., Clark H. M., Ferris J. P. Chemistry of the
Environment. 2nd edition. Academic Press, San Diego,
CA, USA, 2002
[16] Jadhav, H. V., Purohit S. H. Global Pollution and
Environmental Monitoring. Global Media, Mumbai,
IND, 2008
[17] P. Kudesia V., Ritu Kudesia. Air Pollution. Global
Media, Meerut, IND, 2008
[18] Borrego C., Schayes G. Air Pollution Modeling and its
Application. Kluwer Academic Publishers, Secaucus,
NJ, USA, 2002
[19] Pandurangappa C., Lakshminarayanachari K.
Mathematical Model for an Area Source and the Point
Source in an Urban Area. International Journal of
Research in Engineering and Technology, Vol. 01 (1),
20, 2012
[20] Council Directive 1999/30/EC of 22 April 1999
relating to limit values for sulphur dioxide, nitrogen
dioxide and oxides of nitrogen, particular matter and
lead in ambient air. OJ L 163, 41, 1999
[21] Regulation โ„– 12 of 15 July 2010 relating to limit
values for sulphur dioxide, nitrogen dioxide and oxides
of nitrogen, particular matter and lead in ambient air.
Governmental newspaper, Vol. 58, 27, 2010
[22] Abdel Salam H. A. Prediction of Pollutants Emission
Dispersion of Phosphate Fertilizers Production Facility.
International Journal of Research in Engineering and
Technology, Vol. 02 (11), 306, 2013

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Dispersion modeling of nitrous oxide emissions from a nitric acid plant in devnya region, bulgaria

  • 1. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 448 DISPERSION MODELING OF NITROUS OXIDE EMISSIONS FROM A NITRIC ACID PLANT IN DEVNYA REGION, BULGARIA Maya Stefanova1 , Rozalina Chuturkova2 , Evgeni Sokolovski3 , Nina Ilieva4 1 PhD Student, Department of Ecology and Environmental Protection, Technical University, Varna, Bulgaria 2 Associate Professor, Department of Ecology and Environmental Protection, Technical University, Varna, Bulgaria 3 Chief Assistant Professor, Department of Engineering Ecology, University of Chemical Technology and Metallurgy, Sofia, Bulgaria 4 Chief Assistant Professor, Department of Engineering Ecology, University of Chemical Technology and Metallurgy, Sofia, Bulgaria Abstract Within the present research a mathematical modeling is done in order to study the dispersion of nitrous oxide emissions from a single organized source โ€“ a nitric acid plant with 363000 tons per year production capacity in the industrial region of Devnya, Bulgaria. Separate simulations are done for the dispersion of N2O emissions without any emission reduction measures being implemented in the plant and for N2O emission dispersion with a secondary N2O decomposing catalyst being installed under different meteorological conditions. Results indicate that a significant decrease of N2O concentration in the ground atmospheric layer is achieved after the implementation of the secondary decomposing catalyst โ€“ over 81 % reduction of the hourly average N2O concentration and up to 80 % reduction of the annual average N2O concentration is calculated. Dispersion models also indicate that the territorial dispersion of N2O emissions is reduced as well โ€“ the area with N2O concentration below 200 ยตg/m3 is 15 times smaller with a secondary N2O decomposing catalyst being installed. Research results provide a tool to assess the decomposing catalyst reduction potential and to predict the impact of N2O emissions upon the ambient air quality in the source region. Research results prove that high temperature catalytic reduction of N2O emissions from nitric acid production by installing secondary decomposing catalyst is an effective method for N2O emission reduction and a tool to combat global warming effect. Keywords: ambient air quality, air dispersion modeling, greenhouse gas, nitrous oxide, catalytic emission reduction -----------------------------------------------------------------------***----------------------------------------------------------------------- 1. INTRODUCTION Nitrous oxide N2O is a greenhouse gas under the Kyoto Protocol [1] and one of the main reasons for global warming effect [2-4]. N2O emissions from industrial installations for nitric acid production have adverse effect upon the ambient air quality in the surrounding area. The effect level depends on the specific topographic and climate conditions of the source region which also affect the dispersion of the pollutant in the ground atmospheric layer and the processes of photo dissociation, chemical destruction and diffusion [5, 6]. Different measures and techniques for N2O emission reduction are developed and applied in nitric acid production plants around the world [7-9]. Installing a non-platinum secondary catalyst that is decomposing N2O to nitrogen and oxygen right after its formation in the ammonia burner is a secondary measure that provides 73 % reduction of N2O emissions [10]. The achieved N2O reduction level has a positive effect upon the ambient air quality in the industrial source surrounding area and is a tool to prevent adverse changes of the global climate system. The present research aim is to study the dispersion of N2O emissions from a nitric acid plant with and without a secondary decomposing catalyst being installed and to assess their impact upon the ambient air quality in the surrounding area having in mind the specific topographic and meteorological conditions of the region. 2. MATERIAL AND METHODS Within the present research a mathematical modeling is done along with a software simulation of the dispersion of N2O emissions from a single fixed source โ€“ a nitric acid plant with 363000 tons per year production capacity in the industrial area of Devnya, Bulgaria. A secondary decomposing catalyst for N2O emission reduction has been installed in the plant in September 2005 [10]. According to the European Environment Agency currently there is no specific software product developed for mathematical modeling of N2O emission dispersion due to the fact that N2O is inert in the troposphere [11-17] and thus all dispersion models for emissions from area, transport or point sources in urban regions can not be applied [18, 19]. Within this research a practically approbated software product BREEZE AERMOD is used for emission
  • 2. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 449 dispersion modeling taking into account the topography of the region. In order to ensure maximum reliability of the meteorological conditions of the region validated data is used in the form of hourly meteorological file containing information on 6 parameters โ€“ wind speed and direction, ambient air temperature, relative humidity, atmospheric pressure, sun radiation intensity. Research period starts in 2005, due to the fact that before that year there arenโ€™t N2O emission reduction measures applied in the nitric acid plant, and ends in 2012. In order to avoid obtaining of wrong results due to variation of the meteorological conditions N2O emission dispersion modeling is done over two main scenarios. The first scenario presents N2O emission dispersion with no N2O reduction measures being applied in the nitric acid plant. The other scenario presents N2O emission dispersion with a secondary N2O decomposing catalyst being installed in the plant. Emission dispersion with no N2O reduction measures being applied is simulated using data from a single N2O emission measurement in 2005 before the implementation of the secondary catalyst and meteorological data for 2005 and 2012. Emission dispersion with a secondary N2O decomposing catalyst being installed is simulated using emission data in the form of hourly N2O concentration file for 2012 and meteorological data for 2005 and 2012. For every of the four simulations hourly average and annual average N2O concentration in the ground atmospheric layer are calculated referring to European and national standards for determination of hourly average and annual average limit values for the content of oxides of nitrogen in the ambient air [20, 21]. 3. RESULTS AND DISCUSSION 3.1. Topographic Characteristic of the Region The nitric acid plant is located in the east industrial area of Devnya, Bulgaria. The terrain is mostly lowland with some hilly areas and the elevation varies between 0 and 300 m. The highest point in the 5 km radius area is to the north-northwest from the source. To the south, where Beloslav Lake is situated, the terrain is flat. The nearest settlement is Povelyanovo, a suburb of Devnya (to the north). Other settlements in the area are Razdelna, Beloslav and Strashimirovo with elevation almost equal to the elevation of the source site. Settlements to the north from the source such as Slanchevo (elev. 145 m), Kipra (elev. 135 m) and Banovo (elev. 340 m) can be affected by the emission dispersion. These settlements are situated in hilly areas where displacement is higher or almost equal to the geometric height of the source and for that reason certain meteorological conditions may cause increased pollutant concentrations in the ambient air. Fig-1 presents a topographic map of the source region. Fig-1: Topographic map of the source region
  • 3. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 450 3.2 Climate and Meteorological Conditions of the Region The climate of the source region is typical for its long and dry summer with high coefficient of windless periods and small rainfall quantity. Winter period is short and relatively soft with greater percentage and quantity of rainfall than summer period. There are breeze currents with east โ€“ west direction circulating along Varna Lake and Beloslav Lake. At day time breeze currents come from east while at night they come from west. Moderate winds are typical for the region. The terrain advantages the formation of inversion fog and considerable pollution of the ambient air. Statistical data indicates that about 60 % of calendar days are foggy. Fig-2 and Fig-3 present wind roses built for the source region for 2005 and 2012. Both figures indicate that most winds come from southeast with speed varying from 1.54 to 3.09 m/s. Winds with speed over 5.14 m/s are very unusual and mostly come from north-northeast. The percentage of windless periods is very low. Fig-2: Wind rose for 2005 Fig-3: Wind rose for 2012 3.3 Results Within the present research a single organized source of N2O emissions is studied โ€“ P1 stack at the nitric acid plant. The height of the stack is 130 m and the diameter is 1.44 m. Due to the fact that N2O is inert in the troposphere and emissions are expected to expand on long distance from the source the study area is determined with the following proportions โ€“ 20000 m on west โ€“ east direction and 10000 m on south โ€“ north direction. The density of the recipients with a certain N2O concentration is 41 recipients on x (east) and 21 recipients on y (north) with 500 m step or the total amount of the recipients is 861. Using BREEZE AERMOD software a simulation of N2O emission dispersion is done. Hourly average and annual average N2O concentration in the ground atmospheric layer are calculated. Table-1 indicates calculation results for peak values of hourly average N2O concentration, recipientsโ€™ coordinates and elevation and date/time when peak values are obtained. ะขable-1: Peak values of hourly average N2O concentration (ฮผg/m3 ) Avg . Per. Hig h Type Val Date UTM Elev. Hil l Ht. Flag Ht. Rec. Typ e Grid ID YYMMDD HH East (m) North (m) (m) (m) (m) Simulation without secondary catalyst being installed and meteorological data for 2005
  • 4. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 451 1HR 1ST Avg. Conc. 301.96247 5/09/17/18 553291.9 5 4783610.56 0 0 2 GC R0G02000 Simulation without secondary catalyst being installed and meteorological data for 2012 1HR 1ST Avg. Conc. 16705.48516 12/10/28/01 553785.9 4784607.48 155. 1 209 2 GC MN101000 Simulation with secondary catalyst being installed and meteorological data for 2005 1HR 1ST Avg. Conc. 117.69145 5/01/19/10 554791.9 5 4783610.56 0 0 2 GC R0G02000 Simulation with secondary catalyst being installed and meteorological data for 2012 1HR 1ST Avg. Conc. 3126.84989 12/01/25/05 553785.9 4784607.48 155. 1 209 2 GC MN101000 As indicated in Table-1 results show a significant decrease of hourly average N2O concentration in the ambient air after the implementation of the secondary decomposing catalyst. Simulation without secondary catalyst being installed and meteorological data for 2005 indicates that the peak value of hourly average N2O concentration is 302 ยตg/m3 while simulation with secondary catalyst being installed and meteorological data for the same year indicates hourly average N2O concentration of 117.7 ยตg/m3 which is 2.5 times lower. Simulation without secondary catalyst being installed and meteorological data for 2012 indicates that the peak value of hourly average N2O concentration is 16705.5 ยตg/m3 while simulation with secondary catalyst being installed and meteorological data for the same year indicates hourly average N2O concentration of 3126.8 ยตg/m3 which means 81 % reduction of N2O level in the ambient air. Specific meteorological conditions in 2012 (e.g. ambient air temperature, atmospheric stability class determined by the mixing height, sun radiation, etc.) need to be emphasized leading to higher N2O concentrations in the ground atmospheric layer. Simulation with secondary catalyst being installed and meteorological data for 2012 indicates that the peak value of hourly average N2O concentration in the ground atmospheric layer is 10 times higher than the peak value of the simulation without secondary catalyst being installed and meteorological data for 2005. This proves the necessity of modeling 4 simulations for every combination of meteorological data and process conditions. Figures 4 โ€“ 7 present contours of hourly average N2O concentration (ยตg/m3 ) in the ground atmospheric layer for every simulation. Fig -4: Hourly average N2O concentration (ฮผg/m3 ) without secondary catalyst being installed and meteorological data for 2005
  • 5. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 452 Fig -5: Hourly average N2O concentration (ฮผg/m3 ) without secondary catalyst being installed and meteorological data for 2012 Fig-6: Hourly average N2O concentration (ฮผg/m3 ) with secondary catalyst being installed and meteorological data for 2005
  • 6. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 453 Fig-7: Hourly average N2O concentration (ฮผg/m3 ) with secondary catalyst being installed and meteorological data for 2012 The peak value of hourly average N2O concentration for simulation without secondary catalyst being installed and meteorological data for 2005 is obtained at 18.00 h on 17 September 2005 with southeast wind blowing with speed 2.53 m/s (Table-1 and Fig-4) while the peak value for simulation with secondary catalyst being installed and meteorological data for the same year is obtained in January with west- northwest wind blowing with speed 0.5 m/s (Table-1 and Fig- 6). Logically the implementation of the secondary decomposing catalyst leads to 61 % decrease of the hourly average N2O concentration due to significant N2O emission reduction at the nitric acid plant. Peak values of hourly average N2O concentration in the ground atmospheric layer for both simulations with meteorological data for 2012 are obtained with south wind blowing with speed 2 m/s โ€“ in October for simulation without secondary catalyst being installed (Table-1 and Fig-5) and in January for simulation with secondary catalyst being installed (Table-1 and Fig-7). Both peak values are registered in the same recipient with higher elevation than the source height. Excluding the impact of the adverse meteorological conditions in 2012 a significant decrease of hourly average N2O concentration is calculated โ€“ over 81 % reduction for simulation with secondary catalyst being installed compared to simulation without secondary catalyst being installed. Beside N2O concentration decrease a significant reduction of N2O dispersion area in the atmosphere is observed. As indicated on Fig-5 and Fig-7 the area with hourly average N2O concentration below 200 ฮผg/m3 [20, 21] is 29 km2 for simulation without secondary catalyst being installed and less than 2 km2 for simulation with secondary catalyst being installed. Peak values of annual average N2O concentration and recipientsโ€™ coordinates and elevation are presented in Table-2. Table-2: Peak values of annual average N2O concentration (ฮผg/m3 ) High Avg. Conc. UTM Elev. Hill Ht. Flag Ht. Rec. Type Grid ID East (m) North (m) (m) (m) (m) Simulation without secondary catalyst being installed and meteorological data for 2005 1ST 8.92915 553291.95 4783610.56 0 0 2 GC R0G02000
  • 7. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 454 Simulation without secondary catalyst being installed and meteorological data for 2012 1ST 48.37149 551285.9 4785607.48 157.2 260 2 GC MN101000 Simulation with secondary catalyst being installed and meteorological data for 2005 1ST 2.11113 553291.95 4783610.56 0 0 2 GC R0G02000 Simulation with secondary catalyst being installed and meteorological data for 2012 1ST 9.57512 551285.9 4785607.48 157.2 260 2 GC MN101000 Results in Table-2 indicate that annual average N2O concentration in the ground atmospheric layer is over 8.9 ฮผg/m3 for simulation without secondary catalyst being installed and meteorological data for 2005 and 2.1 ฮผg/m3 for simulation with secondary catalyst being installed and meteorological data for the same year which is over 4 times lower. For simulation with secondary catalyst being installed and meteorological data for 2012 annual average N2O concentration is 9.6 ฮผg/m3 which is over 5 times lower than the peak value for simulation without secondary catalyst being installed and meteorological data for the same year. Comparison between simulations with and without secondary catalyst being installed and meteorological data for 2005 indicates that 76.4 % reduction of annual average N2O concentration has been achieved. Comparison between both simulations with meteorological data for 2012 indicates 80.2 % reduction of annual average N2O concentration. Figures 8 - 11 present contours of annual average N2O concentration (ยตg/m3 ) in the ground atmospheric layer for every simulation Fig-8: Annual average N2O concentration (ฮผg/m3 ) without secondary catalyst being installed and meteorological data for 2005
  • 8. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 455 Fig-9: Annual average N2O concentration (ฮผg/m3 ) without secondary catalyst being installed and meteorological data for 2012 Fig-10: Annual average N2O concentration (ฮผg/m3 ) with secondary catalyst being installed and meteorological data for 2005
  • 9. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 456 Fig-11: Annual average N2O concentration (ฮผg/m3 ) with secondary catalyst being installed and meteorological data for 2012 As indicated on Figures 8 โ€“ 11 annual average N2O concentration in the ground atmospheric layer depends strongly on the meteorological conditions of the region. Adverse meteorological conditions in 2012 affect the dispersion of N2O emissions thus causing 4 times higher annual average N2O concentrations than peak values calculated for simulations with meteorological data for 2005. Although meteorological conditions have considerable influence upon N2O emission dispersion a significant decrease of annual average N2O concentration is registered after the implementation of the secondary decomposing catalyst in the nitric acid plant. By analogy with the results obtained for hourly average N2O concentration modeling annual average N2O concentration in the atmosphere proves significant decrease of N2O emission dispersion area. As presented on Fig-8 and Fig-10 the area with annual average N2O concentration below 2 ฮผg/m3 is over 20 km2 for simulation without secondary catalyst being installed while for simulation with secondary catalyst being installed N2O concentration below 2 ฮผg/m3 is registered on a small area directly next to the emission source. 4. CONCLUSIONS Research results indicate a significant decrease of N2O concentration in the ground atmospheric layer after the implementation of the secondary decomposing catalyst in the nitric acid plant โ€“ 71 % average reduction of hourly average N2O concentration and 78 % average reduction of annual average N2O concentration for all the simulations done. Beside the reduction of N2O concentration a significant decrease of N2O emission dispersion area in the ground atmospheric layer is observed. Research results prove the reduction potential of the secondary decomposing catalyst and the positive effect of N2O emission reduction upon ambient air quality in the source region. On that basis a conclusion is made that nitric acid plants with similar parameters can be situated directly next to urban areas without causing adverse effect upon ambient air quality having in mind the topography of the region and possible cumulative effect with other air pollutant sources [22]. High temperature catalytic reduction of N2O emissions from nitric acid production is proved to be an effective measure for atmospheric N2O concentration decrease and a tool to combat adverse changes of global climate system.
  • 10. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 03 Issue: 05 | May-2014, Available @ http://www.ijret.org 457 REFERENCES [1] The Kyoto Protocol to the United Nations Framework Convention on Climate Change, 1998 [2] Ravishankara A. R., Daniel J. S., Portmann R. W. Nitrous Oxide: The Dominant Ozone-Depleting Substance Emitted in the 21st Century. Science, Vol. 326 (5949), 123, 2009 [3] Petrova D., Kostadinova P., Sokolovski E., Dombalov I. Greenhouse Gases and Environment. Journal of Environmental Protection and Ecology, Vol. 7 (3), 679, 2006 [4] Wuebbles D. J. Nitrous Oxide: No Laughing Matter. Science, Vol. 326 (5949), 56, 2009 [5] Chuturkova R., Stefanova M. Assessment of the Effect of Nitrous Oxide Emissions from Nitric Acid Production upon Ambient Air Quality in Devnya Region. Journal Scientific and Applied Research, Vol. 4, 163, 2013 [6] McElroy M. B., McConnel J. C. Nitrous oxide โ€“ a natural source of stratospheric NO. Journal of Atmospheric Sciences, Vol. 28 (6), 1095, 1971 [7] European Comission, Integrated Pollution Prevention and Control. Reference Document on BAT for the manufacture of Large Volume Inorganic Chemicals โ€“ Ammonia, Acids and Fertilizers, 2007 [8] Agency for Energy and the Environment. Reduction of Nitrous Oxide in the Nitric Acid Industry. The Hague, 2001 [9] Stefanova M. Industrial Methods for Nitrous Oxide Emission Reduction. Ecological Engineering and Environment Protection, Vol. 12 (3-4), 89, 2013 [In Bulgarian] [10] Stefanova M., Chuturkova R. Nitrous Oxide Catalytic Reduction at a Nitric Acid Plant in Bulgaria. Environ. Prot. Eng., 2014 (in press) [11] Vallero D. A. Fundamentals of Air Pollution. Academic Press, Burlington, MA, USA, 2007 [12] Tinsley I. J. Chemical Concepts in Pollutant Behavior. Willey, NJ, USA, 2004 [13] Kaur H. Environmental Chemistry. Global Media, Meerut, IND, 2010 [14] Bhagi A. K., Chatwal G. R. Environmental Chemistry. Global Media, Mumbai, IND, 2010 [15] Bailey R. A., Clark H. M., Ferris J. P. Chemistry of the Environment. 2nd edition. Academic Press, San Diego, CA, USA, 2002 [16] Jadhav, H. V., Purohit S. H. Global Pollution and Environmental Monitoring. Global Media, Mumbai, IND, 2008 [17] P. Kudesia V., Ritu Kudesia. Air Pollution. Global Media, Meerut, IND, 2008 [18] Borrego C., Schayes G. Air Pollution Modeling and its Application. Kluwer Academic Publishers, Secaucus, NJ, USA, 2002 [19] Pandurangappa C., Lakshminarayanachari K. Mathematical Model for an Area Source and the Point Source in an Urban Area. International Journal of Research in Engineering and Technology, Vol. 01 (1), 20, 2012 [20] Council Directive 1999/30/EC of 22 April 1999 relating to limit values for sulphur dioxide, nitrogen dioxide and oxides of nitrogen, particular matter and lead in ambient air. OJ L 163, 41, 1999 [21] Regulation โ„– 12 of 15 July 2010 relating to limit values for sulphur dioxide, nitrogen dioxide and oxides of nitrogen, particular matter and lead in ambient air. Governmental newspaper, Vol. 58, 27, 2010 [22] Abdel Salam H. A. Prediction of Pollutants Emission Dispersion of Phosphate Fertilizers Production Facility. International Journal of Research in Engineering and Technology, Vol. 02 (11), 306, 2013