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Energy Sources, Part A, 31:223–231, 2009
Copyright © Taylor & Francis Group, LLC
ISSN: 1556-7036 print/1556-7230 online
DOI: 10.1080/15567030701399479
Air-borne SO2 Pollution Monitoring
in the Upstream Petroleum Operation Areas
of Niger-Delta, Nigeria
E. O. OBANIJESU,1 F. M. ADEBIYI,2 J. A. SONIBARE,3 and
O. A. OKELANA1
1Chemical Engineering Department, Ladoke Akintola University of
Technology, Ogbomoso, Nigeria2Environmental Pollution Research Laboratory, Department of Chemistry,
Obafemi Awolowo University, Ile-Ife, Nigeria3Environmental Engineering Research Laboratory, Chemical Engineering
Department, Obafemi Awolowo University, Ile-Ife, Nigeria
Abstract In the process of crude oil production, sulfur dioxide (SO2) gas is producedas a result of flaring and booming of crude oil associated gases. This paper presents
the study carried out on the monitoring of SO2 emission from some oilfields inthe crude oil producing areas of Niger-Delta region of Nigeria. Six locations were
studied while monitoring involved morning and evening times for four months usinga Testo 350 Flue Gas Analyzer. Comparison of the mean measurements with Nigerian
FEPA tolerance limits indicate that SO2 values from 60 m away from the point sourcesfor all the fields were comparatively higher than their maximum tolerance limits of
50 �g/m3 for long term exposure and SO2 values were also comparatively higherthan the emission limit range (30–300 �g/m3) for SO2 from stationary sources. It is
concluded that this breach of tolerance level may result in acid rain formation, whichcan be detrimental to the environment while the long-term effect can alter the ecology
of the areas. It is recommended that the environmental matrix quality for soil, water,and air be carried out for these areas periodically.
Keywords gas analyzer, oil field, pollution monitoring, SO2
Introduction
The release of gaseous emissions arising from the flaring and booming of associated
gas into the environment is common during upstream petroleum operations in the Niger-
Delta region of Nigeria. Problems associated with this practice appear to be growing
in the region owing to the increase in crude oil production. During gas flaring, SO2
is produced as a primary air pollutant. The SO2 undergoes oxidation to produce sulfur
trioxide (SO3), which is further transformed into a dry or moist sulfuric acid (H2SO4), a
secondary air pollutant, through contact with atmospheric vapor. This pollutant may be
transported in the atmosphere over distances of hundreds to thousands of kilometers and
deposited wet or dry. The wet deposition is known as acid rain with pH normally below
Address correspondence to Emmanuel Ogo-Oluwa Obanijesu, Department of Chemical Engi-neering, Ladoke Akintola University of Technology, Ogbomoso, Nigeria. E-mail: [email protected]
223
224 E. O. Obanijesu et al.
5.6 (Environment Canada, 2005) while the dry deposition takes place when the sulfate
and gas particles are deposited on, or absorbed onto surfaces. This acid rain goes into
the soil and is taken up by the animals or growing plants in the areas and can alter the
ecology of the areas.
SO2, though not detectable by odor, its adverse effects on health, vegetation, and
buildings can be readily observed (Palmer, 1974). It causes damage to vegetation, animals,
and properties and causes ill health to humans. Through a series of complex chemical
reactions, SO2 emitted by natural gas flares are converted to acids, which may result
in acidity of rain. Photochemical processes, because of their production of radicals, are
strongly coupled to SO2 to form H2SO4 (Song et al., 2003):
SO2 C OH�! HOSO�
2
HOSO�
2 C O2 ! HO�
2 C SO3
HO�
2 C NO ! NO2 C OH�
SO3 C H2O ! H2SO4
(1)
According to Guendel et al. (1994), the reaction usually involves several atmospheric
reactions, which may include those heterogeneous reactions taking place within fog as:
2SO2 C O2 C Catalyst ! 2SO3
SO3 C H2O ! H2SO4
(2)
The catalyst in Eq. (2) above may be ammonia and when this is the case, an acidic
component of the atmosphere may be produced in the conversion process (Renard et al.,
2004); this is usually rapid. In the atmosphere, SO2 and SO3 dissolve in the available
water vapor to form H2SO3 and H2SO4, respectively. These acids are highly corrosive in
nature and come back to the earth as acid rain. Acid rain having pH of about 2.6 destroys
vegetation, lakes, rivers, and rooftops, among others.
Flaring is a common method of disposal of flammable waste gases in the upstream
oil, downstream refining, and chemical processing industries (Akeredolu and Sonibare,
2004); it is an open-air flame usually at the tip of a long stack. The flame is exposed to
the weather elements, particularly winds (Ritter et al., 2002). Gas flares are chosen as the
choice disposal option for handling waste hydrocarbon gases because of their ability to
burn efficiently (Strosher, 1996). Though emission species can be reduced with complete
combustion within available short residence time making flame temperature a primary
variable in the combustion process (Roe et al., 1998), Sonibare and Akeredolu (2004)
identified SO2 as one of these species left if sour gas is involved in combustion.
Gaseous emission monitoring study is part of environmental performance monitor-
ing of production operations aimed at achieving continuous performance improvement
with the ultimate goal of minimizing negative impacts on the environment arising from
production operations. In recognition of the problems this primary air pollutant could
create, different studies are being carried out globally in order to predict and control its
impact on environment. With technological advancements, the vast amount of data about
ambient air is generated to know the quality of air in the environment and administer the
appropriate corrective actions wherever necessary. This study was carried out to predict
the impact of SO2 emissions on air quality in some upstream petroleum operations area
of Nigeria.
Airborne SO2 from Some Oilfields in Niger-Delta 225
For example, in Canada, regulatory approaches on sulfur emissions from Alberta
petroleum production and processing operations address both environmental protection
in the form of ambient air quality guidelines and pollution protection through sulfur
recovery and flaring guidelines (Brian, 2005). Similarly, in the UK SO2 released into the
environment through power stations (combustion processes) led to widespread acidifica-
tion of freshwaters in the uplands since 1850; in recognition of this primary air pollutant’s
contribution to UK and European countries air sheds, the UK agreed in the Gothenburg
Protocol in 1999 to reduce the annual emission of SO2 (expressed as the element S)
to 625 kt-S. This and earlier decisions has led to the drastic declination of annual UK
emission of SO2 which peaked in 1970 at 3,259 kt-S and decreased to 594 kt-S by 1999
and further reduced by 80% by 2001 with a projection of further declination by 2010 in
commitments within the international protocols (NEGTAP, 2001). This reduction in the
SO2 concentration in the UK over the last three decades has virtually eliminated direct
effects on vegetation, leading to an expansion of some lichen species.
Methodology
Six flow stations located at Niger-Delta region of Nigeria were studied for this work
(Figure 1). The first site (Oilfield 1) was located in a swamp and saltwater region of the
Niger-Delta and was mounted on a concrete barge capable of producing about 45,000 bpd
and designed to be unmanned. It has a provision for accommodation with a houseboat as
a support. It operates on electronic instrumentation, electric drive, and a massive power
generation that serves both the facility and the community. The second station (Oilfield 2)
was a sand-filled three-process train facility with production capacity of 135 Mb/d. The
third field (Oilfield 3) is a double bank station with a design capacity of about 80,000
bbl/d. It consists of a flow station, an offshore development platform, and 17 clusters,
unmanned, fully automatic, and fail-safe. The operations crew visits the station on a
daily basis from a terminal logistic base. Oilfield 4 was a 30,000 bpd flow station which
Figure 1. Niger-Delta: Rivers, states and vegetations. (Source: Waado, 2005.)
226 E. O. Obanijesu et al.
Figure 2. Testo 350 portable emission analyzer.
supplies stabilized crude along with produced water to a terminal about 3 km away via
a 12 delivery line. The fifth site (Oilfield 5), which is a swamp piled, three-bank flow
station with each having 45 Mb/d capacities. The station is supported on a piled structure
with a single deck, and built on a piled area of about 50 m by 100 m. Oilfield 6 covers
about 16 km2 and is located at about 65 km southwest in the swamp and salt-water
region of Warri. The field has 17 hydrocarbon bearing reservoirs and presently about 21
producing wells are tied into the station.
A Testo 350 Flue Gas Analyzer (Testo AG, Hampshire, UK) (Figure 2) was used to
measure the SO2 emissions in and around these stations. This analyzer has a detection
limit of 0–5,000 ppm with 1 ppm resolution and a response time of 30 seconds. A
combined wind vane and digital anemometer (Taylor wind scope, Taylor Precision Instru-
ments, Oak Brook, IL, USA) was used to determine wind direction and speed. Sampling
was carried out at 60 m, 200 m, and 500 m from each point source. Measurements were
taken in the morning between 8:00 am and 11:59 am when activities were going on
within the facilities and at afternoon between 4:00 pm and 5:00 pm when the staff was
supposed to be resting.
Air sample was continuously extracted from the atmosphere and a portion of the
sample sent to the analyzer to determine the pollutant of interest. The control unit, which
is a portable measuring instrument for spot checks and measurements on site, is equipped
with a probe socket and an integrated differential pressure probe. The comprehensive
range of probes makes it possible for accurate measurements of temperature, pressure,
humidity, velocity, current, and voltage.
Results and Discussion
The results of the SO2 measurements at the six oilfields are presented in Tables 1–6 with
the summary in Figure 3. At point source distance 60 m, Oilfield 1 with a mean value
of 472 �g/m3 has the highest SO2 concentrations followed by Oilfield 2 with a mean
Airborne SO2 from Some Oilfields in Niger-Delta 227
Table 1
Daily SO2 concentrations for Oilfield 1 (�g/m3)
Point source distance, m
Week 60 200 500
1 400 120 90
2 390 110 85
3 600 400 120
4 610 309 125
5 350 100 90
6 330 90 93
7 400 120 90
8 390 100 93
9 300 180 115
10 310 188 110
11 500 125 125
12 490 120 130
13 750 180 115
14 730 170 110
15 500 125 125
16 500 120 125
Mean 472 160 108
Table 2
Daily SO2 concentrations for Oilfield 2 (�g/m3)
Point source distance, m
Week 60 200 500
1 350 290 160
2 340 300 150
3 210 250 250
4 200 255 250
5 750 180 115
6 750 175 110
7 500 125 125
8 510 120 125
9 750 180 115
10 700 180 110
11 400 125 125
12 420 110 130
13 600 180 115
14 590 170 110
15 500 125 125
16 500 120 125
Mean 462 180 140
228 E. O. Obanijesu et al.
Table 3
Daily SO2 concentrations for Oilfield 3 (�g/m3)
Point source distance, m
Week 60 200 500
1 750 180 115
2 740 180 110
3 500 125 125
4 490 120 125
5 80 65 50
6 80 66 52
7 100 80 60
8 80 75 57
9 120 90 71
10 135 100 100
11 135 100 100
12 125 94 89
13 700 170 110
14 700 160 100
15 500 115 120
16 500 110 120
Mean 353 114 94
Table 4
Daily SO2 concentrations for Oilfield 4 (�g/m3)
Point source distance, m
Week 60 200 500
1 650 315 185
2 650 320 180
3 710 350 200
4 700 340 190
5 100 685 150
6 90 680 155
7 145 100 80
8 140 90 79
9 150 890 160
10 145 880 165
11 160 120 180
12 150 110 190
13 620 305 180
14 620 300 170
15 700 330 210
16 700 320 200
Mean 402 383 167
Airborne SO2 from Some Oilfields in Niger-Delta 229
Table 5
Daily SO2 concentrations for Oilfield 5 (�g/m3)
Point source distance, m
Week 60 200 500
1 200 65 60
2 200 60 59
3 250 80 70
4 240 86 77
5 60 70 100
6 59 66 90
7 75 80 150
8 70 75 130
9 300 125 80
10 300 120 71
11 455 135 90
12 450 120 89
13 210 64 60.5
14 200 63 59
15 260 80.5 71
16 250 84 73
Mean 224 86 83
Table 6
Daily SO2 concentrations for Oilfield 6 (�g/m3)
Point source distance, m
Week 60 200 500
1 300 315 60
2 300 310 60
3 1,125 120 75
4 1,100 120 77
5 250 280 200
6 220 280 200
7 300 450 200
8 290 440 190
9 70 150 600
10 70 140 590
11 80 200 100
12 70 190 950
13 310 320 60
14 300 310 70
15 1,120 120 74
16 1,100 125 73
Mean 438 242 224
230 E. O. Obanijesu et al.
Figure 3. Average SO2 measured concentrations in and around the studied areas.
value of 462 �g/m3. At point source distance 200 m, Oilfield 4 with a mean value of
383 �g/m3 has the highest SO2 concentrations followed by Oilfield 6 with a mean value
of 242 �g/m3. Likewise, at point source distance 500 m, Oilfield 6 with a mean value of
224 �g/m3 has the highest SO2 concentrations followed by Oilfield 4 with a mean value
of 167 �g/m3 while Oilfield 5 has the lowest mean values of SO2 at each of the point
source distances. As may be expected, the highest concentrations of SO2 were obtained
at point source distance 60 m (the closest point to the sources) with a mean value of
393 �g/m3 and a range of 224–472 �g/m3. This is about twice the mean concentrations
at distance 200 m and thrice that of the distance 500 m away from the sources.
Comparison of the mean measurements (Figure 3) with Nigerian FEPA (1991)
tolerance limits indicate that SO2 values from 60 m away from the point sources for all
the fields were comparatively higher than their maximum tolerance limits of 50 �g/m3 for
long-term exposure. At point source distances 200 m and 500 m, the SO2 concentrations,
though very high, fall within the limits of SO2 emissions from the stationary sources. The
comparatively high concentration of SO2 pollutant at these sites may result in acid rain
in the studied areas and this could partly be responsible for the acid rain once reported
in the Niger Delta area of the country (NDES, 1997).
Conclusion and Recommendation
The SO2 measurement data interpretation from these oil fields indicates that the produc-
tion of the crude oil could pose considerable environmental hazards. If, in the process
of production and refining of the crude oil, the effluent are not well managed before
discharge or there is still continuous flaring and booming of gases, the environment can
be polluted. As a result of large quantities of SO2 that are fared and boomed, there
may be a need to recover these gases for commercial use. Processes such as flue gas
desulphurization, tall stacks, wet scrubbing, and adsorption could be applied to control
the air-borne SO2 pollution. It is recommended that the environmental matrixes (soil,
water, and air) qualities of these areas be done periodically as in the case of other oil
producing regions of the developed nations.
Airborne SO2 from Some Oilfields in Niger-Delta 231
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