1. Introduction
Odor pollution, often overlooked in environmental discussions, refers to the presence of unpleasant odors in the atmosphere that disrupt human well-being and affect economic activities. These odors can originate from a wide range of sources, including industrial facilities, agricultural operations, sewage treatment plants, landfills, and waste incinerators. While not always immediately hazardous to health, persistent odor pollution can lead to a decline in quality of life for those exposed to it, as well as to property value loss.
Unlike other pollutants, odors are subjective in nature, with their perception varying greatly between individuals. Some people might find a specific odor tolerable, while others may experience distress, nausea, or headaches [
1,
2,
3]. The psychological effects of constant exposure to unpleasant smells are profound, with studies [
4] linking it to increased stress levels, sleep disturbances, and reduced productivity.
Odor pollution is not limited to urban or industrial areas; rural communities can also suffer from the effects, for example those near large-scale farming operations or waste management facilities. Public awareness of odor pollution has been growing, with more advocacy for better regulation, monitoring, and control of odor emissions.
The economic impact of odor pollution may be significant, especially in areas where tourism, hospitality, and real estate values are affected. Persistent odors can lead to the abandonment of properties and loss of business. Governments and businesses are increasingly pressured to develop and implement effective odor control technologies and strategies to minimize these disruptions.
As urbanization and industrialization continue to expand globally, addressing odor pollution will become increasingly critical to maintaining the livability of communities and the health of the environment [
5]. Effective solutions will require cooperation between governments, industries, scientists, and affected communities to understand, manage, and mitigate this often invisible but impactful form of environmental pollution.
Odor levels may be estimated by means of dispersion models [
6] that typically calculate 1-hour average concentrations. Since odor is perceived on time scales of the order of one breath (i.e., few seconds), a method is needed to transform the 1-hour average concentrations into peak hourly concentrations. This task is often accomplished with a constant peak-to-mean factor that may be applied while postprocessing the model results, even though more complex methodologies are also described in the scientific literature [
7].
Among the most common sources of emissions within plants are stacks, which are referred to as “point sources” from a modeling perspective. These sources are characterized by their geographical coordinates, height and diameter (geometrical parameters), and exit speed, exit temperature and emission rate of each pollutant (emission parameters). Stacks may be very high as, for example, in power plants or incinerator plants, while in other plants they are relatively short (e.g., less than 10 m). Sometimes odor is emitted by these short stacks, for example by the food industry, rendering plants, farming plants, just to mentioning a few. The effects of emissions from short stacks on the receptors near to the plant are more severe than those of taller stacks. The situation is complicated by the fact that the exit terminals of these short stacks may be vertical and unobstructed, vertical with a rain cap, horizontal, with any slope with respect to the vertical and even pointing down with a gooseneck shape. Temperature and exit velocity are important variables for calculating plume rise which may be reduced when a rain cap is present, or when the stack terminal is horizontal. In these situations, the initial vertical velocity of the plume is reduced or null, and the plume rise is due only to the thermal buoyancy if the exit temperature exceeds the ambient temperature. Since the impact of these stacks is close to the point of release, it is important to simulate their emissions as precisely as possible.
A method to describe the effects of rain caps or horizontal terminals has been described by the US-EPA [
9], and consists in suppressing the vertical mechanical momentum by forcing the exit velocity to 0.001 m/s. Also, in order to maintain volumetric flow and buoyancy, an equivalent stack diameter must be given in input to the model. By equating the volumetric flow calculated with the actual values of diameter (d) and exit velocity (v), and the volumetric flow calculated with the equivalent diameter (d
Eq) and the reduced vertical velocity (0.001 m/s), it is possible to show that d
Eq = d×(v/0.001)
0.5. Therefore, the equivalent diameter may be very large with respect to the actual diameter. For example, if the actual diameter is 0.4 m and the exit velocity is 6 m/s, the equivalent diameter is about 31 m. This large diameter is not a problem when the atmospheric dispersion model adopts empirical equations for describing the plume rise (for example the Briggs equations [
8]), because it enters only in the calculation of the buoyancy flux. On the contrary, it cannot be used in a numerical algorithm based on the solution of partial differential equations, because in that case it would be the plume diameter at time zero, and such a large value would be unrealistic.
AERMOD [
10], the US-EPA preferred model for near-field dispersion of emissions for distances up to 50 km [
11], adopts the method described in [
9] for rain capped or horizontal stacks when building downwash is not involved [
12]. Instead, if a stack is subject to
building downwash - i.e., the capture of a plume in the low-pressure area in the lee side of a building, potentially increasing ground-level concentrations of pollutants - AERMOD adopts the numerical plume rise algorithm PRIME [
13]. In this situation, if a POINTCAP source (stack with rain cap) is simulated, the initial plume diameter is set equal to twice the stack diameter in order to account for the initial spread of the plume, when it impacts the cap from below. Also, the initial vertical velocity of the plume is set to 0.001 m/s, and the initial horizontal velocity is set to one fourth of the exit velocity and directed as the wind. If a POINTHOR source (horizontal stack) is simulated, the plume diameter remains the stack diameter, the initial vertical velocity of the plume is set to 0.001 m/s, and the initial horizontal velocity is set equal to the exit velocity and directed as the wind.
CALPUFF [
14] is a Lagrangian puff dispersion model belonging to the list of the alternative models of the US-EPA [
11]. Alternative models are those that can be used in regulatory applications with case-by-case justification to the Reviewing Authority in situations where the preferred models are not applicable or available. CALPUFF is capable to simulate many types of sources, among which, point, area, buoyant line and volume. Starting from version 7, CALPUFF is capable to simulate also road sources. Point sources in CALPUFF are associated to a momentum flux factor (FMFAC) that can assume only the values 1 or 0. For vertical and unobstructed stacks, FMFAC=1 and the whole vertical momentum is used for determining the plume rise. For a rain capped stack or a horizontal stack, FMFAC must be set to 0, in order to simulate the suppression of the vertical momentum. With FMFAC=0 the plume rise is due only to the thermal buoyancy when the plume temperature exceeds the ambient temperature. When the parametric plume rise is used in CALPUFF (MRISE=1) and FMFAC=0, the stack height is reduced by three diameters to simulate the
stack tip downwash (STD) – i.e., the capture of a plume in the low pressure area in the lee side of a stack, particularly important when the stack has a large diameter and a low exit speed - independently from the value of the input variable related to the activation of the STD (MTIP). On the contrary, when the numerical plume rise is used (MRISE=2) and FMFAC=0, the analysis of the Fortran code of CALPUFF (version 7) - as well as the results of sensitivity analysis - shows that the vertical momentum is not suppressed, and the only effect is the reduction of the stack height by three diameters to simulate the STD only if MTIP=1. In other words, if the user selects the numerical plume rise (MRISE=2) and does not select to simulate the STD (MTIP=0), for a given stack the plume rise is identical both with FMFAC=0 and with FMFAC=1 (i.e., FMFAC does not work).
LAPMOD [
15] is an open source Lagrangian particle model that simulates many types of sources. A theoretical description of LAPMOD, as well as its validation against the experimental datasets of Kincaid (rural conditions), and Indianapolis (urban conditions) can be found in [
16,
17]. The results of the two validations describe LAPMOD as a reliable model according to the performance evaluation criteria proposed by [
18], that are based on FA2, NMSE and fractional bias [
19]. An intercomparison between LAPMOD and other dispersion models for odor applications has been presented in [
20]. For point sources the model includes two numerical plume rise schemes derived by the works of Janicke and Janicke [
21] and Webster and Thomson [
22]. The user selects which one of the two algorithms must be used for all the point sources of a specific simulation. Independently from the selected plume rise algorithm, LAPMOD describes the orientation of the stack tip by means of two angles: the azimuthal angle and the polar angle. The azimuthal angle specifies the stack orientation on the horizontal plane, while the polar angle specifies the tilting of the stack with respect to the vertical. Then, horizontal stacks with any orientation over the horizontal plane can be simulated, therefore the emission may have any direction. This is different than the implementation in AERMOD, where the initial plume direction of a horizontal stack is always downwind. Instead, stacks with rain-cap are simulated by LAPMOD as done by AERMOD. The initial plume diameter is equal to twice the stack diameter to simulate the initial spread of the plume; the vertical component of the exit velocity is set to 0.001 m/s; the horizontal component of the exit velocity has an intensity equal to one fourth of the exit velocity and is directed along the wind. In calm conditions (i.e., wind speed lower than 0.5 m/s) the initial plume direction is determined randomly.
The first part of this work describes a comparison between CALPUFF and LAPMOD for different types of stacks. The analysis was limited to these two models because they use exactly the same meteorological input deriving from the binary output file of CALMET [
23]. The comparison with AERMOD would be interesting, but that means to use another set of meteorological data, making it more difficult to understand if possible different results are due to the way the stack terminal is simulated or to the meteorological input to the models. In the second part of the work, LAPMOD is used for simulating the impact of the same stack with six different terminals and different exit temperatures. The simulations have been performed for two sites characterized by different meteorological conditions.
4. Conclusions
The intercomparison between LAPMOD and CALPUFF has shown that most of the results are within FA2, therefore the two models seem in reasonable agreement for the specific analysis described in this work. Of course, there are differences between the results because the formulation of the two models is different: one is a puff model while the other one is a particle model; the algorithms for calculating the concentration are different; the ways to treat the effects of orography are different, just to say a few. In detail, some differences related to the simulation of rain capped stacks are due to different specific assumptions: CALPUFF does not increment the initial diameter of the plume, CALPUFF – when numerical plume rise is used – does not set the vertical exit speed to zero, the whole vertical velocity is used and it just reduces the stack height of three diameters. On the contrary for rain capped stacks LAPMOD increases the initial diameter of the plume, suppresses the vertical component of the emission velocity, and uses a horizontal velocity equal to one fourth the vertical one.
The application of LAPMOD to a stack with six different terminals (vertical unobstructed, vertical with rain cap, horizontal pointing north, east, south and west) has shown that the lower concentrations at the closest receptors are always predicted for the vertical unobstructed stack. This is particularly true for low emission temperatures, that are not infrequent in odor emitting stacks. Moreover, the results of rain capped stacks are different from those of horizontal stacks, therefore it does not seem correct to treat them in the same way as done in CALPUFF by setting FMFAC=0. Additionally, the results of horizontal stacks depend on their horizontal orientation, therefore it does not seem correct to treat them in the same way as done in AERMOD with the POINTHOR source which always sets the emission direction along the wind.
Most importantly, the results show that the choice of the stack terminal has important effects on the odor levels predicted at the closest receptors. When receptors are very close to the sources, the use of vertical unobstructed stacks seems to be the most advisable choice.
The results described in this article are derived solely from numerical analysis. Their confirmation or refutation by validation with experimental data would be desirable.
Figure 1.
Position of the discrete receptors (red circles). The source is in (0,0).
Figure 1.
Position of the discrete receptors (red circles). The source is in (0,0).
Figure 2.
Wind roses for year 2022 at Site 1 (a) and Site 2 (b).
Figure 2.
Wind roses for year 2022 at Site 1 (a) and Site 2 (b).
Figure 3.
Site 1. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for (a) vertical unobstructed stack and (b) rain capped stack.
Figure 3.
Site 1. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for (a) vertical unobstructed stack and (b) rain capped stack.
Figure 4.
Site 2. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for (a) vertical unobstructed stack and (b) rain capped stack.
Figure 4.
Site 2. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for (a) vertical unobstructed stack and (b) rain capped stack.
Figure 5.
Site 1. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C. Vertical unobstructed stack.
Figure 5.
Site 1. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C. Vertical unobstructed stack.
Figure 6.
Site 1. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C. Vertical stack with rain cap.
Figure 6.
Site 1. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C. Vertical stack with rain cap.
Figure 7.
Site 2. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C. Vertical unobstructed stack.
Figure 7.
Site 2. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C. Vertical unobstructed stack.
Figure 8.
Site 2. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C. Vertical stack with rain cap.
Figure 8.
Site 2. Scatter plot of the 98th percentile of hourly peak concentrations of LAPMOD versus CALPUFF for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C. Vertical stack with rain cap.
Figure 9.
Site 1. Scatter plot of the 98th percentile of hourly peak concentrations predicted by LAPMOD for different terminal types versus those predicted for a vertical unobstructed stack for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C.
Figure 9.
Site 1. Scatter plot of the 98th percentile of hourly peak concentrations predicted by LAPMOD for different terminal types versus those predicted for a vertical unobstructed stack for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C.
Figure 10.
Site 2. Scatter plot of the 98th percentile of hourly peak concentrations predicted by LAPMOD for different terminal types versus those predicted for a vertical unobstructed stack for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C.
Figure 10.
Site 2. Scatter plot of the 98th percentile of hourly peak concentrations predicted by LAPMOD for different terminal types versus those predicted for a vertical unobstructed stack for different emission temperatures: (a) T=30 °C, (b) T=50 °C; (c) T=70 °C; (d) T=90 °C; (e) T=100 °C; (f) T=150 °C.
Figure 11.
Site 1. Examples of plume shapes in cold environment for an emission temperature of 30 °C and different terminal types: (a) vertical unobstructed; (b) rain capped; (c) horizontal pointing north; (d) horizontal pointing east; (e) horizontal pointing south; (f) horizontal pointing west.
Figure 11.
Site 1. Examples of plume shapes in cold environment for an emission temperature of 30 °C and different terminal types: (a) vertical unobstructed; (b) rain capped; (c) horizontal pointing north; (d) horizontal pointing east; (e) horizontal pointing south; (f) horizontal pointing west.
Figure 12.
Site 1. Examples of plume shapes in hot environment for an emission temperature of 30 °C and different terminal types: (a) vertical unobstructed; (b) rain capped; (c) horizontal pointing north; (d) horizontal pointing east; (e) horizontal pointing south; (f) horizontal pointing west.
Figure 12.
Site 1. Examples of plume shapes in hot environment for an emission temperature of 30 °C and different terminal types: (a) vertical unobstructed; (b) rain capped; (c) horizontal pointing north; (d) horizontal pointing east; (e) horizontal pointing south; (f) horizontal pointing west.
Figure 13.
Site 1. Examples of plume shapes in hot environment for a vertical unobstructed stack with different emission temperatures: (a) 30 °C; (b) 50 °C; (c) 70 °C; (d) 90 °C; (e) 100 °C; (f) 150 °C.
Figure 13.
Site 1. Examples of plume shapes in hot environment for a vertical unobstructed stack with different emission temperatures: (a) 30 °C; (b) 50 °C; (c) 70 °C; (d) 90 °C; (e) 100 °C; (f) 150 °C.
Figure 14.
Site 1. Examples of plume shapes in hot environment for a vertical rain capped stack with different emission temperatures: (a) 30 °C; (b) 50 °C; (c) 70 °C; (d) 90 °C; (e) 100 °C; (f) 150 °C.
Figure 14.
Site 1. Examples of plume shapes in hot environment for a vertical rain capped stack with different emission temperatures: (a) 30 °C; (b) 50 °C; (c) 70 °C; (d) 90 °C; (e) 100 °C; (f) 150 °C.
Table 1.
Source parameters.
Table 1.
Source parameters.
| Parameter |
Value |
Units |
| Height |
8.0 |
m |
| Diameter |
0.5 |
m |
| Volumetric flow |
8000 |
Nm3/h |
| Odor concentration |
4000 |
ouE/m3
|
| OER |
9540 |
ouE/s |
Table 2.
Exit temperatures and speeds.
Table 2.
Exit temperatures and speeds.
| Temperature (°C) |
Speed (m/s) |
| 30 |
12.6 |
| 50 |
13.4 |
| 70 |
14.2 |
| 90 |
15.0 |
| 100 |
15.5 |
| 150 |
17.5 |