Abstract
This review described the state of the science concerning the generation, measurement, and mitigation of ammonia (NH3) emissions from beef cattle feedyards. NH3 emissions primarily come from urinary urea in cattle manure. In the past, constant emission factors were used to inventory NH3 emissions. Currently, NH3 emission factors estimated by process-based mechanistic models reflecting various factors affecting NH3 emissions in the feedyard environment are available. This review of current literature indicated the average NH3 emissions from a beef cattle feedyard was approximately 119 g/head/day (range 24 to 318 g/head/day), and the average NH3 flux was approximately 58 µg/m2/s (range 2 to 185 µg/m2/s). Although more realistic estimates of NH3 emission flux from open-lot livestock facilities were being obtained using process-based models, there was still significant variation depending on the diet composition, manure management practices, and the feedyard environment, including both seasonal weather patterns and synoptic weather events. We note the need to improve inventories of NH3 emissions into categories of crude protein percentage, manure management implemented, and feedyard environment. Some mitigation strategies can be effective, such as diet manipulation, growth-promoting technologies, and manure or pen-surface amendments. Of those, precision diet feeding to meet but not exceed protein requirements appeared to be the most practical way to reduce ammonia emissions over the animals’ feeding period; laboratory studies suggested that shorter-term reductions in emission flux may be possible with the other approaches, but they were far more speculative at this point as to both their efficacy and their cost of implementation.
1 Introduction
Over the past few decades, livestock and poultry farmers have scaled up farming operations to meet society’s demand for high-quality meats, milk, eggs, and by-products. The concentration of animals in feeding operations has played a large role in fulfilling the demand for animal protein with fewer animals and while using fewer land resources. Concentration of animals in close proximity during a portion of their production cycle also concentrates their nutrient emissions. More specifically, these undesirable potential implications of confined (or “concentrated”) animal feeding operations (CAFOs) are caused by gas and particulate matter (PM) emissions from various types of animal wastes, including manure (feces and urine), waste feed, bedding, and wastewater. Gaseous emissions from CAFOs include NH3, greenhouse gases (carbon dioxide, CO2; methane, CH4; and nitrous oxide, N2O), and other air pollutants such as volatile organic compounds (VOCs), many of which are odorous.
NH3 emissions from CAFOs are a high-profile environmental quality concern because they can contribute to the eutrophication of surface waters, nitrate contamination of ground waters, soil acidity, secondary formation of fine PM, and impaired air quality (USEPA, 2004; Hribar, 2010; ). Gaseous NH3 in the atmosphere has been reported as a significant contribution to the formation of airborne fine particulate matter (PM2.5) through reactions with water vapor and other air pollutants, including oxidation products of sulfur dioxide (SO2) or nitrogen oxides (NO and NO2, or NOx) (Li et al., 2008; Wyer et al., 2022). Indeed, U.S. Environmental Protection Agency (USEPA) recently reduced the annual health-based National Ambient Air Quality Standard for PM2.5 from 12.0 µg/m3 to 9.0 µg/m3 (USEPA, 2024). Since NH3 is a precursor gas that may be easier to mitigate than others among PM2.5’s other precursors (Meng et al., 2017; Gu et al., 2021; Wyer et al., 2022), if ambient PM2.5 standards are further reduced, ambient air-quality standards for NH3 may be introduced. Furthermore, NH3 may also contribute to climate change through N2O formation as an intermediate byproduct of ammonium (NH4+) oxidation in the microbial processes of nitrification and denitrification (USEPA, 2010). In addition, NH3 emissions may contribute to nitrogen (N) deposition in neighboring ecosystems, which in turn may affect ecosystem function by promoting eutrophication, soil acidification, and disrupting biodiversity (; Thompson et al., 2015; Morris, 2016; ).
As public awareness and concern over the potential adverse effects of NH3 emissions on the environment and human health increased, governmental regulation of CAFOs led to a push and the adoption of sustainable management practices by livestock producers (Waldrip et al., 2015). Sound scientific evidence is needed to evaluate current and proposed regulations that go beyond encouraging practices regarding CAFOs, air quality, PM, and NH3 emissions in particular. It is necessary to understand the emission mechanisms and processes influencing emissions, know the appropriate measurement methodologies and techniques and uncertainties associated with their use, evaluate current scientific literature for feedyard-based emissions data, survey the industry feedyard management practices, anticipate the impact of emerging regulatory trends and socioeconomics on emissions, and identify the most practical approaches to mitigation and potential barriers to their adoption.
In this review, we reported the state of the science concerning NH3 emissions from beef cattle feedyards. The review is organized into five major areas: 1) pathway of NH3 emissions through N metabolism in the ruminant animal, 2) dynamics of NH3 emissions from pen surfaces, 3) methods quantifying NH3 emissions in the feedyard, 4) the current level of NH3 emissions in beef cattle feedyards, and 5) recommended management practices to mitigate NH3 emissions from feedyards. Details of the literature search methodology, including search engines, terms used, inclusion and exclusion criteria, and the total number of materials reviewed, are provided in the Supplementary Material.
2 Pathway of ammonia emissions from ruminant animal
Ruminants, specifically pre-gastric fermenters, have a unique digestive system that evolved to digest and use forage resources that are less or not digestible in monogastric animals. The unique digestive organ called the reticulo-rumen is an anaerobic microbe fermenter with the remarkable ability to convert dietary protein into microbial protein. Ruminal microorganisms can use not only dietary protein but also non-protein-N, which does not contain amino acids (e.g., urea and NH3) as N sources for microbial protein synthesis. In the reticulo-rumen, N sources are degraded by rumen microbes to peptides, amino acids, and eventually to NH3 by the deamination of amino acids and then these compounds are used to synthesize microbial protein (Hristov and Jouany, 2005; NASEM, 2016). Microbial protein has a similar amino acid composition to the amino acid composition of tissue and milk protein, which makes it almost an ideal source of amino acids for the ruminant (NRC, 2001; Hristov et al., 2011). The metabolizable protein needs of the ruminant for maintenance and production are met primarily by microbial proteins that are washed out of the reticulo-rumen and feed proteins, which are not degraded by rumen microbes, with a small contribution from endogenous N, which originates from the animal’s own viscera rather than from dietary sources such as sloughed-off intestinal cells in the post-ruminal (small and large intestine) metabolism (NRC, 2001; NASEM, 2016). A portion of NH3 produced in ruminal N metabolism is absorbed across the ruminal epithelium into the portal vein and converted mostly into urea by the urea cycle in the liver to avoid NH3 toxicity (NASEM, 2016). Urea produced by the liver is partly excreted in the urine by the kidneys, with the remainder recycled back to the gastrointestinal tract (GIT) through either direct transfer from blood across the epithelial tissue or via saliva as a N source for protein synthesis (NASEM, 2016). The process in which NH3 in the rumen is converted into urea by the liver and reused as a N source in GIT is called urea recycling (or N recycling), and it plays an important role in N preservation mechanism of the ruminant (NASEM, 2016). Undigestible and unabsorbed N sources in ruminal and post-ruminal metabolism are excreted as feces. The overall N metabolism pathway in the ruminant is shown in Figure 1.
Figure 1
The excretion of NH3 is largely determined by the form of NH3 in the ruminant’s metabolism. For example, if it is in a gas phase (NH3), it is most likely to be excreted as eructation, exhaled gas, and flatus. However, if it is in an ionized (NH4+) or solid form, it is more likely to be incorporated into the manure (feces and urine). Since the form of NH3 produced in the digestion of the ruminant is determined by the NH3/NH4+ equilibrium state (Equation 1), it is important to understand the factors that affect the NH3/NH4+ equilibrium and the ruminal and post-ruminal environments. The equilibrium between NH3 and NH4+ is not a redox-dependent reaction, but a pH and temperature (T) dependent reaction in aqueous solutions (Equations 2, 3; ) as illustrated in Figure 2. This is because there is no change in the oxidation states of N or hydrogen (H), which is the key feature of redox reactions.
Figure 2
The ruminal and post-ruminal environments depend on diet composition, management, and cattle’s health condition, but they are generally anaerobic, reductive (oxidation-reduction potential (Eh) of -250 to -450 mv; Van Soest, 1994),< 8 pH, and ~39°C (NASEM, 2016). Considering the general pH and T in the rumen and post-rumen, it is reasonably assumed that NH3 exists in mostly the NH4+ form. In addition, Mohiuddin and Khattar (2019) reported that the pKa of this reaction is about 9.15 and this reaction toward NH4+ occurs almost instantaneously under biological conditions (pH 7.4 and 36.5°C). However, the aqueous solution in the rumen and post-rumen is more dynamic and complex due to anaerobic microbial interactions and reductive conditions, thus in addition to pH and T, the change in pressure, ionic strength, and salinity may affect the conversion of NH3 form due to byproducts from microbial digestion and GIT metabolism.
Thus, based on the data investigated to date, we aimed to discuss specifically the form of NH3 estimated to be emitted by each NH3 emission pathway: 1) exhalation, 2) eructation, 3) flatus, and 4) the excreted N sources in manure, considering the unique N metabolism and the viscera environment of the ruminant. Environmental conditions and the predominant forms of NH3 associated with each NH3 emission pathway are described in the Supplementary Material. In summary, since pH and T are widely recognized as the primary factors influencing the chemical form of NH3 under biological conditions, NH4+ is the dominant form in the ruminant’s GIT. Consequently, most NH3 emitted from ruminants is considered to originate from excreted N in manure (Figure 3).
Figure 3

A schematic of ammonia emission pathways from the ruminant. The protein pathways inside the ruminant were reprinted from Vaga (2017).
3 Dynamics of ammonia emissions from pen surfaces
Excreted N in feces and urine is the main source of NH3 emissions from the beef cattle feedyard. Fecal NH3 is derived from undigested feed residues, microbial cells, endogenous secretions, sloughed cells from GIT (Waldrip et al., 2015), and urine NH3 derived from urea, hippuric acid, and purine-based catabolism residues (
Urea (CO(NH2)2) is not volatile, but once it comes in contact with the urease enzyme (urea amidohydrolase), which is ubiquitous in manure and soil (Waldrip et al., 2015), it is rapidly hydrolyzed to NH3 and CO2 (
Figure 4

A conceptual model of NH3 formation and volatilization. The image was reprinted from Hristov et al. (2011).
Most NH3 emission from the beef feedyard originates from urine NH3, particularly urinary urea (
The instantaneous magnitude and rate of NH3 loss are the result of complex physical and chemical processes on feedyard surfaces (Harper, 2005;
Table 1
| Environmental factor | Correlation coefficient (Kendall’s tau-b) | p-value |
|---|---|---|
| Wind friction velocity | 0.34 | <0.01 |
| Manure temperature | 0.36 | <0.05 |
| Air temperature | 0.16 | <0.05 |
| Temperature difference between the manure and the air | 0.46 | <0.05 |
| Cattle numbers in the feedyard | 0.21 | <0.01 |
Correlation coefficient observed between environmental factors and NH3 volatilization.
4 Quantifying ammonia emissions
To accurately quantify NH3 emissions in the feedyard, it is necessary to understand the characteristics of NH3 emissions occurring in the feedlot environment. NH3 is a colorless gas with a distinct, pungent smell. It occurs naturally and is normally found in trace amounts in the atmosphere (range: 1 to 25 ppb; Renard et al., 2004). Due to its high reactivity and the pervasiveness of the urease enzyme, the process of NH3 formation and volatilization is almost instantaneous and begins immediately after manure is excreted (Hristov et al., 2011). Once emitted into the atmosphere, NH3, where it is the dominant alkaline gas, reacts with atmospheric sulfuric and nitric acids forming ammonium sulfate, ammonium bisulfate, and ammonium nitrate, which precipitate in atmospheric water droplets as secondary fine particles (PM2.5) and are regulated by USEPA as a so-called “criteria” air pollutant (Renard et al., 2004;
NH3 emissions from open feedyards are generally lower than those encountered in closed or housed animal production systems (Todd et al., 2005, 2006; Hristov et al., 2011). This is because open feedyards are exposed to ambient air, allowing for dilution airflow that reduces NH3 concentrations in the atmospheric boundary layer. Although ambient conditions are spatially and temporally variable, NH3 emissions from beef feedyards are quickly dispersed by atmospheric turbulence (Waldrip et al., 2015). In other words, most agricultural open sources like a feedyards tend to be scattered both temporally and spatially, and most of the gaseous NH3 emitted by feedyards may be shortly adsorbed to surrounding cropping and natural ecosystems by dry deposition (Harper et al., 2004; Harper, 2005), converted to fine particles, or mixed into the upper atmosphere. Additionally, manure in open feedyards is typically distributed over a larger area and may dry out more quickly due to exposure to sunlight and wind. Although more NH3 may be released during the drying process, dried manure emits less NH3 compared to the wetter manure often found in closed systems. In addition, open-lot feedyards often have lower stocking density compared to animal operations under the roof, which reduces the total amount of NH3 being produced per unit of emitting area.
Quantifying gas emissions from open sources requires equipment that can measure low concentrations of NH3 quickly, accurately, and robustly. Any measurement procedure that alters the natural ambient state (e.g., manure property and turbulence at the emitting surface) will introduce bias to measured NH3 emission rates (Harper et al., 2010a). For NH3, any measurement technology that interferes with the turbulent transport process away from the source (the rate-limiting process) can result in large errors. This is unlike CH4, CO2, or NO2, which are less soluble and less affected by turbulent transport as mass-flow (biological) gases (Harper et al., 2010a). Therefore, measuring the NH3 concentration emitted in the natural ambient state with the acquisition of weather data is better for the quantification of NH3 emission in the feedyard compared to other approaches such as creating an artificial airflow inside a flux chamber.
Quantifying NH3 emissions requires at least two components: 1) a method to measure the atmospheric concentration of NH3 and 2) a method to measure weather data for converting the concentration into emission using a dispersion model or a method to directly measure the airflow rate (usually for lab scale) (Waldrip et al., 2015). It is important to note that concentration is only a percentage. 1 ppm of NH3 just means that NH3 is 0.0001% of the sampled air. It says nothing about the actual amount of NH3 injected into the atmosphere. Therefore, it is necessary to approach the term of emissions (mass per time). If the total volumetric airflow (m3/s) and the NH3 concentration (g/m3) from an emission source were measured, the two terms must be multiplied to obtain the emission rate in g/s. The main text of this review describes only the most widely used method currently applied in practice. However, the Supplementary Material provides an overview of five major approaches for measuring NH3 concentrations (acid trap, chemiluminescence, electrochemical sensor, infrared analyzer, and tunable diode analyzer) and estimating NH3 emissions (N mass balance, flow-through chamber, micrometeorological methods, air dispersion models, and satellite remote sensing). As each method has advantages, disadvantages, and applicability varies, readers are encouraged to consult all methods and select the one most appropriate for their specific research conditions and objectives.
4.1 Measurement of ammonia concentration
4.1.1 Open-path tunable diode laser absorption spectrometry
Open-path tunable diode laser absorption spectrometry (OP-TDLAS) is a technique designed to measure the path-averaged concentration of specific species within a gas mixture using laser-absorption spectrometry. The basic principle of OP-TDLAS involves passing the laser through the gas mixture, detecting the amount of light absorbed by NH3 molecules at specific wavelengths according to the change in the degree of recovery rate from the detector, and then computing the NH3 concentration based on the calibration between NH3 concentration and the amount of light absorbed at certain wavelengths (Figure 5). Such a specific waveband (so-called narrow absorption line), specifically designed for NH3, avoids mutual absorption interference of other gases such as CO2, CH4, and water vapor (Harper et al., 2010a). The amount of light absorbed by the NH3 molecules is proportional to the concentration of NH3 along the optical path. NH3 gas molecules typically absorb light in the range of around 200 (Boreal Laser INC), 620~740, or 931~954 cm-1 (
Figure 5

A figure of the OP-TDLAS on a beef cattle feed yard.
The main advantage of using OP-TDLAS at beef cattle feedyards is quick, accurate, and robust NH3 measurement in a feedyard environment where NH3 rapidly volatilizes from relatively large emitting areas. As an example, the detailed specification of OP-TDLAS by Boreal Laser Inc (Edmonton, Canada) has 8–6500 or 40-15,000 ppm-m as a detectable NH3 range and a ±2% uncertainty about reading accuracy. The response time required for measuring accurate NH3 concentration is 1 s. Once factory calibration is completed, it has a longer calibration cycle than other sensors. If stored properly, the measurement will remain accurate for several years. In addition, the open path between the laser and retroreflector can typically be covered to 5~500 m in measurements, but this can be increased further depending on the performance of the reflector. In terms of disadvantages, OP-TDLAS is expensive and requires careful maintenance. It may require skilled operators for setup, calibration, and maintenance due to the complexity of the technology involved. It is susceptible to maintaining clear line of sight between the laser and retroreflector. Environmental conditions like dust and condensation can increase the opacity of the air along the optical path and degrade the quality of an instrument’s signal.
4.2 Estimation of ammonia emissions
4.2.1 Air dispersion models
Direct measurement of NH3 emissions from open cattle feedyards is challenging due to their size, the spatial and temporal variable nature of emissions from open sources, and the labor, cost, and time consumption associated with measuring and maintaining instruments (
In the case of open beef feedyards, several air modeling systems could be applied such as 1) Gaussian model-based AERMOD (American Meteorological Society/Environmental Protection Agency Regulatory Model) system and 2) backward Lagrangian stochastic (bLS) model-based WindTrax system, but bLS model-based WindTrax is generally applicable for beef cattle feedyards.
4.2.1.1 Gaussian model-based AERMOD system
A Gaussian dispersion model describes the transport of pollutants from a point source as a steady-state plume whose horizontal and vertical spread are modeled as Gaussian distributions whose parameters are specified by ensembles of weather variables affecting boundary-layer turbulence. The AERMOD System is a steady-state, Gaussian plume model that incorporates air dispersion based on planetary boundary layer turbulence structure and scaling concepts, including treatment of both surface and elevated sources, and both simple and complex terrain (USEPA, available online: https://www.epa.gov/scram/air-quality-dispersion-modeling). It is the preferred regulatory dispersion model of USEPA and is a free system used for emission estimation of target gases across various industries. An advantage of such Gaussian model-based system is that the plume dispersion parameters are based on theory and inputs are well characterized by experimental data (
4.2.1.2 bLS model-based WindTrax
Lagrangian stochastic models (LS) describe the trajectories of tracer particles in turbulence from a statistical perspective of random velocity fields. They are considered by some authors the most natural and accurate means of calculating atmospheric transport (Wilson and Sawford, 1996).
Where: Q: NH3 emission rate (kg/m2/s) from the area source of known configuration. C: NH3 concentration (mg/m3); Cb = the background NH3 concentration (mg/m3). (C/Q)sim: a model prediction of the ratio of concentration to the emission. N: the total number of (computational) particles released from the source. W0: the vertical velocity at touchdown within the source (m3/min per surface area; m2).
The advantages of the bLS dispersion model are its ability to accurately represent wind features near the ground, their role in gas transport, (Harper et al., 2011) and to be faster and more flexible in calculating turbulent dispersion from surface area sources than “forward” models (
bLS model-based WindTrax is an easy-to-use graphical interface designed for the assessment of turbulent transport on the micro-meteorological scale and for simulating short-range atmospheric dispersion (for horizontal distances within about 1 km of the source) using bLS models (Thunder Beach Scientific, available online: http://www.thunderbeachscientific.com/). This program is free, and guidelines and introductions are provided so that users can use them correctly. Before running the program, users should carefully review the associated documentation for detailed guidance on model inputs, options, and best practices.
5 Ammonia emission factors from beef cattle feedyard
Although measurements of NH3 emission have been improved, direct measurements at each feedyard are not feasible due to the time, cost, and labor required. In addition, NH3 emissions in beef cattle feedyards vary greatly depending on the diet (e.g., CP%), environmental conditions (e.g., air T, wind speed, turbulence, and precipitation), and operation-specific management practices (e.g., stocking density, manure storage, feeding management, and manure handling). Thus, measurements taken at one point in time on one feedyard may not accurately capture seasonal and temporal fluxes of emissions that occur due to changes in weather, animal diet, or other management practices (Waldrip et al., 2015). Although the emissions cannot be represented in a single value due to variables in the operation-specific management practices and environment, the need for a standard representing NH3 emissions in general from livestock operations for inventory purposes is being highlighted.
In the past, researchers focused on measuring emissions and comparing them to constant emission factors (EF), which are derived from the literature by selecting data from studies that measured emissions from operations that are assumed to represent production facilities for a specific livestock type and region. Although they are not a perfect standard, constant EF are often used by regulatory agencies and environmental advocacy groups to estimate the footprint of specific animal-production systems (
Process-based modeling uses mathematical models to simulate the many processes and interactions that occur within a system such as a beef cattle feedyard. Dynamic process-based models that quantify emissions based on classical principles of thermodynamics and kinetics potentially provide a cost-effective method of estimating emissions and evaluating how changing climate and management practices affect emissions from animal agriculture (Waldrip et al., 2015). Representative process-based modeling used to quantify NH3 emissions from beef cattle feedyards includes IHF, modified mass difference approach, flux-gradient technique (ECV), and IDM.
We have summarized results reported to date for NH3 flux (µg/m2/s) and the NH3 EF (per capita emission rates; PCER, g/head/d) using several process-based models by season (Tables 2, 3). Open path laser was often used to measure the NH3 concentration and bLS Inverse dispersion model was widely used to convert the measured NH3 concentration into NH3 emissions from the beef cattle feedyard. A wide range of NH3 flux has been reported, from 2 to 185 µg/m2/s (average 58 µg/m2/s). It was generally found that NH3 flux follows the following order: summer > autumn > spring > winter. Also, a wide range of NH3 emissions have been reported ranging from 24 to 318 g/head/d, and average 119 g/head/d. The highest NH3 emissions were observed in the autumn, but the variation was large in each season, thus, no significant differences were represented between seasons (p > 0.05). It was found that 9 to 116 (average 43) NH3 kg/head/y are emitted annually.
Table 2
| Reference | Location | Measurement or Estimation Method | NH3 flux (µg/m2/s) | |||||
|---|---|---|---|---|---|---|---|---|
| NH3 concentration | NH3 emission | Spring | Summer | Autumn | Winter | Annual | ||
| Hutchinson et al. (1982) | Colorado | Acid trap | Vertical gradient flux model | 29 | 44 | |||
| Shi et al. (2001) | Texas | Acid trap | Flux chamber | 55 | ||||
| Koziel et al. (2004) | Texas | Chemiluminescence | Flux chamber | 28 | 5 | |||
| Todd et al. (2005) | Texas | Acid trap | Flux gradient model | 70 | 34 | 36 | ||
| Texas | Chemiluminescence | Vertical gradient flux model | 61 | 5 | ||||
| Todd et al. (2006) | Texas | Acid trap | Integrated horizontal flux model | 3 | 16 | 2 | 2 | |
| Todd et al. (2007) | Texas | Acid trap or Chemiluminescence | Flux gradient model | 72 | 39 | |||
| McGinn et al. (2007) | Alberta, Canada | Open path laser | bLS Inverse dispersion model | 84 | ||||
| Rhoades et al. (2008) | Texas | Chemiluminescence | bLS Inverse dispersion model | 89 | 77 | |||
| Van Haarlem et al. (2008) | Alberta, Canada | Open path laser | bLS Inverse dispersion model | 10 | ||||
| Staebler et al. (2009) | Alberta, Canada | Open path laser | bLS Inverse dispersion model | 76 | ||||
| Texas | N mass balance | 64 | 36 | |||||
| Rhoades et al. (2010) | Texas | Chemiluminescence | bLS Inverse dispersion model | 84 | 77 | 63 | 58 | 71 |
| Colorado | Acid trap | Flux chamer | 83-109 | |||||
| Sun et al. (2015) | New Jersey | Open path laser | Eddy covariance | 37 | ||||
| Parker et al. (2016) | Texas | Chemiluminescence | Flux chamber | 8-38 | ||||
| McGinn et al. (2016) | Alberta, Canada | Open path laser | Inverse dispersion model | 50 | ||||
| Shonkwiler and Ham (2018) | Colorado | Open path laser | bLS Inverse dispersion model | 60 | ||||
| Colorado | Open path laser | FIDES Inverse dispersion model | 48 | |||||
| Wang et al. (2024) | Victoria Australia | Open path laser | bLS Inverse dispersion model | 113 | 185 | 104 | 107 | 127 |
| Range | 3-113 | 16-185 | 2~104 | 2-107 | 36-127 | |||
| Average | 52 | 68 | 57 | 36 | 76 | |||
| Total average | 58 | |||||||
Seasonal NH3 flux from beef cattle feedyards.
Table 3
| Reference | Location | Measurement or Estimation Method | NH3 emission factors (g/head/day) | |||||
|---|---|---|---|---|---|---|---|---|
| NH3 concentration | NH3 emission | Spring | Summer | Autumn | Winter | Annual | ||
| Hutchinson et al. (1982) | Colorado | Acid trap | Vertical gradient flux model | 50 | ||||
| Texas | N mass balance | 108 | 66 | |||||
| McGinn et al. (2007) | Alberta, Canada | Open path laser | bLS Inverse dispersion model | 140 | ||||
| Texas | Open path laser | bLS Inverse dispersion model | 151 | 149 | ||||
| Rhoades et al. (2008) | Texas | Chemiluminescence | bLS Inverse dispersion model | 89 | 78 | |||
| Todd et al. (2008) | Texas | Acid trap | bLS Inverse dispersion model | 118 | 128 | 64 | ||
| Van Haarlem et al. (2008) | Alberta, Canada | Open path laser | bLS Inverse dispersion model | 318 | ||||
| Victoria, Australia | Chemiluminescence | bLS Inverse dispersion model | 69 | |||||
| Queensland, Australia | Chemiluminescence | bLS Inverse dispersion model | 24 | |||||
| Staebler et al. (2009) | Alberta, Canada | Open path laser | bLS Inverse dispersion model | 245 | ||||
| Todd et al. (2009) | Texas | N mass balance | 82-149 | |||||
| Rhoades et al. (2010) | Texas | Chemiluminescence | bLS Inverse dispersion model | 85 | ||||
| Todd et al. (2011) | Feedlot A, Texas | Open path laser | bLS Inverse dispersion model | 110 | 158 | 122 | 71 | 115 |
| Feedlot E, Texas | Open path laser | bLS Inverse dispersion model | 73 | 103 | 83 | 60 | 80 | |
| Waldrip et al. (2013b) | Feedlot A, Texas | Manure-DNDC | bLS Inverse dispersion model | 173 | ||||
| Feedlot E, Texas | Manure-DNDC | bLS Inverse dispersion model | 77 | |||||
| Victoria, Australia | Chemiluminescence | Integrated horizontal flux model | 156 | |||||
| Sun et al. (2015) | New Jersey | Open path laser | Eddy covariance | 63 | ||||
| Shen et al. (2016) | Victoria, Australia | Acid trap | bi-directional NH3 exchange model | 126 | ||||
| McGinn and Flesch (2018) | Feedlot A, Alberta, Canada | Open path laser | Inverse dispersion model | 117 | ||||
| Feedlot B, Alberta, Canada | Open path laser | Inverse dispersion model | 100 | |||||
| Shonkwiler and Ham (2018) | Colorado | Open path laser | bLS Inverse dispersion model | 89 | ||||
| Colorado | Open path laser | FIDES Inverse dispersion model | 71 | |||||
| Redding et al. (2019) | Queensland, Australia | Laser absorption spectroscopy | bLS Inverse dispersion model | 127 | ||||
| Colorado | Open path infrared gas analyzer | Gaussian plume approach | 55 | |||||
| Wang et al. (2024) | Victoria Australia | Open path laser | bLS Inverse dispersion model | 170 | 190 | 126 | 155 | 160 |
| Range | 73~170 | 24~190 | 83~318 | 60~156 | 77~173 | |||
| Average | 112 | 104 | 172 | 91 | 114 | |||
| Total average | 119 | |||||||
Seasonal NH3 emissions from beef cattle feedyards.
Although it is agreed that more realistic NH3 EF are being obtained using process-based models, there is still significant variation of estimated NH3 EF depending on the diet, the model used, and the feedyard environment. This deviation is most likely caused by differences in geographical environment and management implemented in actual feedyards as well as inherent assumptions made in modeling. Therefore, when investigating EF in the future, a detailed description of the environment, diet, and management practices implemented by the feedyard is necessary to evaluate the impact of each category of manure management implemented and the feedyard environment and estimate accurate EF for each scenario. We suggest an investigation list of feedyard environments to aid in assessing NH3 emissions in Table 4. The information on feedyard management and diet reported in the previous papers to date is insufficient to implement this categorization. Improved models and measurement equipment are still needed for estimating more accurate NH3 EF measurements under the ever-changing feedyard environment in the future.
Table 4
| Section | Type | Items | Answer |
|---|---|---|---|
| Feed | Nutrient composition | DM (% as fed) | |
| CP (% DM) | |||
| Starch (% DM) | |||
| NDF (% DM) | |||
| ADF (% DM) | |||
| TDN (g/kg DM) | |||
| NEg (Mcal/kg DM) | |||
| Use of specific feed ingredients to mitigate nitrogen emissions | |||
| Intake (kg of DM/head/day) | |||
| Average feeding time(s) and interval(s) (e.g., 0600 and 1400 hours, fed twice per day) | |||
| Growth promotants and metabolic modifiers | Use of monensin, growth-promoting hormone implant, ß-adrenergic agonists, and/or others | ||
| Animal | Initial body weight (kg) | ||
| Final body weight (kg) | |||
| Head count | |||
| Animal density (head/area) | |||
| Total days on feed | |||
| Manure and pen surface management | Manure cleaning cycle (e.g., days or times per year) | ||
| Manure storage method (e.g., composting) | |||
| Use of manure amendments | |||
| Use of water sprinklers on the pen surface | |||
| Weather | Precipitation events and/or severe wind events | ||
| Activity records | Cattle receipt (date) | ||
| Cattle shipment (date) | |||
| Manure removal (date) | |||
Investigation list of feedyard management and environment.
DM, dry matter; CP, crude protein; NDF, neutral detergent fiber; ADF, acid detergent fiber; TDN, total digestible nutrients; NEg, net energy for gain.
6 Management practices to mitigate ammonia emissions
The major best management practices (BMP) available for use to mitigate NH3 emissions in open-lot livestock facilities have been listed and recommended by USDA-NRCS (Table 5;
Table 5
| Category | NRCS code | Management practices |
|---|---|---|
| Feed management | 592 | Diet manipulation Growth-promoting technologies Phase feeding |
| Manure amendment | 632 | Surface amendment and manure separation |
| Dust control | 375 | Water sprinkler |
| Pen maintenance | N/A | Manure harvesting and pen drainage |
Best management practices (BMP) for open-lot livestock facilities to decrease NH3 deposition.
References from USDA-NRCS; conservation management practices.
The fundamental solution to mitigate NH3 emission in beef cattle feedyards is to minimize N excretion in manure by optimizing pre-excretion stages management, but there is an intrinsic limitation in achieving this goal due to the inefficient utilization of feed N in the ruminant. The efficiency of N utilization in ruminants is typically low (around 25%) and highly variable (10% to 40%) compared with the higher efficiency of other production animals (
6.1 Ammonia mitigation practices in the pre-excretion stage
6.1.1 Precision feeding
The terminology of precision feeding was coined to suggest that livestock feeding can be fine-tuned to maintain or improve performance and better realize other benefits (Reddy and Krishna, 2009). In other words, the ingredients and chemical composition of the diet are modified over the growth stage of the animal so that the nutrient composition of the diet more closely meets the nutrient requirements of the animal and the excreted nutrients in manure are minimized (
Ideally, a nutritionist can balance animal performance with subsequent effects on the environment using current nutrient models. However, the question remains whether precision feeding can be realistically applied to a commercial beef cattle feedyard (Waldrip et al., 2015). This is because there are several challenges to overcome for precision feeding to be practical. Factors that limit the practicality of precision feeding include (1) variability in animal nutrient requirements, (2) seasonal and climatic effects, (3) variability in the composition of feed ingredients, (4) logistics, and (5) variability in the estimation of DMI (
Although we acknowledge the practical limitations of implementing precision feeding, scientific advancements to date have led to the development of several effective strategies within precision feeding systems to mitigate NH3 emissions. Representative examples include phase feeding and the use of growth-promoting technologies, which will be discussed in detail next. Dietary protein requirements decrease as cattle mature because of reduced protein deposition and simultaneous increase in fat deposition (Hristov et al., 2011; Waldrip et al., 2015). Phase feeding is a type of precision feeding where dietary protein concentrations are reduced late in the feeding period (Waldrip et al., 2015). Use of growth-promoting technologies are used in tandem with precision feeding strategies to maximize the efficiency and effectiveness of nutrient utilization by cattle, specifically for improving growth, feed efficiency, and production sustainability (Tedeschi et al., 2003). In conclusion, we believe that the factors limiting the practical use of precision feeding can ultimately be alleviated through the accumulation of knowledge and technology development from continued research, although the logistical hurdles of implementation at the feedyard-level remain to be overcome. Addressing these limitations and overcoming these hurdles to the adoption of precision feeding will help to maintain or improve animal performance while minimizing NH3 emissions.
6.1.2 Manipulation of crude protein concentration and protein type
NH3 emissions from beef cattle feedyards are sensitive to dietary CP concentrations (
Table 6
| Reference | Management type | Measurement or Estimation Method | Application dose | NH3 or N Excretion | p-value | ||
|---|---|---|---|---|---|---|---|
| NH3 concentration | NH3 emission | Range Value (% DM) | Result | Rate (%) | |||
| CP manipulation | N mass balance | 13.4 to phase-fed (10.5–12.0) | 158 to 108 g/head/d | 32 | 0.01 | ||
| Pandrangi et al. (2003) | CP manipulation | Acid trap | Flux chamber | 13.0 to 11.0 | 1.69 to 0.79 g/m2/d | 53 | <0.05 |
| CP manipulation | Acid trap | Flux chamber | 13.0 to 11.5 | 1.95 to 1.24 g/m2/d | 37 | <0.01 | |
| Todd et al. (2006) | CP manipulation | Acid trap | Flux chamber | 13.0 to 11.5 | 0.18 to 0.10 g/m2/d | 44 | <0.01 |
| CP manipulation | Acid trap | Integrated Horizontal flux | 0.29 to 0.22 g/m2/d (Spring data) | 24 | <0.01 | ||
| CP manipulation | N mass balance | 13.0 to 10 | 5.2 to 1.7 g/head/d | 67 | <0.01 | ||
| CP manipulation | N mass balance | Feeding CP 13.9% vs Oscillating feeding of low (9.1%) and high (13.9%) at 48h intervals | 59.6 to 39.7 g/d | 33 | <0.01 | ||
| Quinn et al. (2007) | CP manipulation | N mass balance | 14.2 to phase-fed (avg 12.1%) | 150 to 109 | 27 | 0.02 | |
| CP manipulation | N mass balance | 12.3 to phase-fed (avg 12.5%) | 92 to 76 | 17 | 0.11 | ||
| CP manipulation | Meta-Analysis | 13.6 to phase-fed (avg 11.5%) | 158 to 108 | 32 | 0.01 | ||
| CP manipulation | Meta-Analysis | 13.4 to phase-fed (avg 11.7%) | 73 to 62 g/head/day | 15 | 0.32 | ||
| CP manipulation | Acid trap | Flux chamber | 13.5 to 11.6 (for 45 days) | 7.1 to 3.7 g/m2/d | 48 | <0.10 | |
| Todd et al. (2013) | CP manipulation | Open path laser | Meta-Analysis Inverse dispersion model | 16.0, 13.5, and 11 | 169.9, 104.4 to 90.1 g/head/day | 47 | N/A |
| Menezes et al. (2016) | CP manipulation | N mass balance | 14.0 to 10.0% DM | 130.3 to 93.2 g/d | 28 | <0.01 | |
| Mejia Turcios (2024) | CP manipulation | Cattle pen enclosures | -150 g/head/d on rumen available protein to microbial crude protein ratios (RAP: MCP) vs. +150 g/head/d on RAP: MCP. | N/A | 52 | <0.01 | |
| Stackhouse et al. (2012) | Growth promoting technologies | Optical sensors (Innova 1412 and TEI 55C) | Flux chamber | 33.1 mg/kg DM of monensin, 12.2 mg/kg DM of tylosin phosphate 8.3 mg/kg of DM of zilpaterol hydrochloride implantation with a combination of 120 mg trenbolone acetate and 24 mg estradiol | 109 to 63 g/head/day | 42 | <0.01 |
| Ross (2021) | Growth promoting technologies | N/A | Finishing ration containing 27.3 g ractopamine/907 kg dry matter | N/A | 17 | 0.03 | |
| Growth promoting technologies | N mass balance | Implanted 120 mg of trenbolone acetate, 24 mg of estradiol USP, and 29 mg of tylosin tartrate | 51 to 46 g/head/day | 10 | N/A | ||
| Wendler et al. (2025) | Growth promoting technologies | N mass balance | Optaflexx (ractopamine hydrochloride, 300 mg/head/day for 35 d) and Experior (lubabegron fumarate, 36 mg/head/day for 56 d + 4 d removal) | 3338 to 3126 g cumulative NH3 | 5-14 | <0.01 | |
Evaluation of management practices to mitigate NH3 emission in the pre-excretion stage.
N/A, not available; 6.2 Ammonia mitigation practices in the post-excretion stage.
In addition, manipulating the type of protein source in the diet can be helpful to mitigate N losses in manure. There are two types of protein: rumen degradable protein (RDP) and rumen undegradable protein (RUP). RDP is the protein broken down by the microbes in the rumen and used for microbial growth. RUP is the protein that escapes fermentation in the rumen and is digested in the small intestine. In beef cattle, 40 to 80% of non-retained N is excreted in the urine, and this quantity typically increases as dietary CP and RDP concentrations increase in the diet (NASEM, 2016). Therefore, N excretion can be reduced by increasing the proportion of RUP from the protein source required to satisfy the protein requirements (RDP+RUP) of cattle in the diet. However, it is important to ensure that RDP levels are high enough to satisfy the N requirement of the rumen microorganisms, as a deficiency would be expected to decrease the extent of fermentation and ultimately increase NH3 emission intensity due to decreased feed efficiency. Increasing RUP level is also expected to increase N utilization efficiency by enhancing urea recycling to compensate for rumen microbial requirements due to RDP deficiency.
6.1.3 Growth-promoting technologies
Growth-promoting technologies (implants and feed additives) are commonly used to reduce NH3 emissions by less N excretion through increasing the efficiency of energy use for growth and by low cumulative NH3 emissions from fewer days on feed required to reach finished weight. Although the specific mechanism for increasing productivity by growth-promoting technologies in beef cattle is different, growth-promoting technologies such as hormone implants and ß-adrenergic agonists increase nutrient use for protein synthesis and indirectly lead to decreased lipogenesis (Hutcheson et al., 1997; Nichols et al., 2002; Lean et al., 2014). It was reported that implants enhance both ADG and feed conversion, while implanted cattle often have less marbling and lower quality grades (Preston and Herschler, 1992; Selk, 1999; Ohnoutka et al., 2021). Also, monensin, which is generally included as a growth-promoting technology, is an ionophore antimicrobial that increases overall energy yield from feed and improves animal growth performance by increasing the ratio of propionate to acetate and decreasing the deamination of amino acids through preferentially inhibiting gram-positive bacteria in the rumen (Perry et al., 1976; Russell and Strobel, 1988; Tedeschi et al., 2003). Also, it prevents and controls Coccidiosis caused by Eimeria ssp in ruminants. An increase in protein synthesis with growth-promoting technologies would be expected to reduce N excretion. It has been reported that the use of conventional productivity-enhancing technologies (combination of implant, monensin, tylosin, ß-adrenergic agonists, and others), mitigated NH3 emissions by 10~42%, but the effect of only implants mitigated 17% of NH3 emissions (Stackhouse et al., 2012; Ross, 2021;
6.2 Ammonia mitigation practices in the post-excretion stage
6.2.1 Manure amendments
Manure amendment can be divided into chemical and physical amendments (
Evaluation of manure amendment on the open feedyard surface to mitigate NH3 emission has shown a wide range (19 to 98%) in mitigation effectiveness (Table 7). The urease inhibitor reduced NH3 emissions by 26–66% on the manure surface in lab and pilot-scale studies but did not show significant mitigation at the field scale. However, nitrogen fertilizers coated with the urease inhibitors showed a significant mitigation of NH3 emissions on grassland (67-79%). This suggests that further research is needed to determine the best application methods for urease inhibitors to achieve significant NH3 reduction in feedyard manure. The effects of calcium chloride, humate, and aluminum sulfate, which lower the pH and inhibit urease decomposition, resulted in a mitigation rate of 20 to 71% (Shi et al., 2001; Spiehs and Woodbury, 2022) at the lab and pilot scale. As physical amendments, the lignite showed a mitigation rate of 66% (
Table 7
| Reference | Management type | Measurement or Estimation Method | Application dose | NH3 or N Excretion | p-value | ||
|---|---|---|---|---|---|---|---|
| NH3 concentration | NH3 emission | Range Value (% DM) | Result | Rate (%) | |||
| Varel et al. (1999) | Urease inhibitor (N-(n-butyl) thiophosphoric triamide; NBPT) | Acid trap | N mass balance (Kjeldahl digestion) | 22.8 kg/ha once per week for 42 days | 5.0 to 2.1 g/kg manure (by 35 days) | 58 | N/A |
| Shi et al. (2001) | Urease inhibitor (NBPT) | Acid trap | Flux chamber | 1 kg/ha for 21 days | 4 to 1.44 g NH3-N | 65 | <0.05 |
| Urease inhibitor (NBPT) | Acid trap | Flux chamber | 2 kg/ha for 21 days | 4 to 1.37 g NH3-N | 66 | <0.05 | |
| Surface amendment (Calcium chloride) | Acid trap | Flux chamber | 9000 kg/ha | 4 to 0.9 g NH3-N | 78 | <0.05 | |
| Surface amendment (Humate) | Acid trap | Flux chamber | 9000kg/ha | 4 to 0.9 g NH3-N | 68 | <0.05 | |
| Surface amendment (Aluminum sulfate) | Acid trap | Flux chamber | 9000kg/ha | 4 to 0.7 g NH3-N | 98 | <0.05 | |
| Surface amendment (commercial product, Ammonia Hold, Lonoke, Arkansas) | Acid trap | Flux chamber | 750 kg/ha | 4 to 2.7 g NH3-N | 32 | <0.05 | |
| Surface amendment (Lignite) | Chemiluminescence | Integrated Horizontal flux | 4.5 kg/m2 | 156 to 53 g NH3-N/head/day | 66 | N/A | |
| Szymula et al. (2021) | Surface amendment (Biochar) | Berthelot reaction method | 3% addition of biochar | 18 to 11 mg/L | 41 | <0.05 | |
| Surface amendment (Zeolite) | Berthelot reaction method | 3% addition of zeolite | 18 to 17 mg/L | 9 | N/S | ||
| Surface amendment (Mixture of bentonite and zeolite) | Berthelot reaction method | 3% addition of a mixture of bentonite and zeolite | 18 to 13 mg/L | 28 | <0.05 | ||
| Spiehs and Woodbury (2022) | Surface amendment (Aluminum sulfate) | Acid trap | Flux chamber | 300g/6 kg of manure + water Data from 0 to 7 days | Approximate 43 to 33 mg/m2/h | ~20 | <0.05 |
| 600g/6 kg of manure + water Data from 7 to 14 days | Approximate 26 to 10 mg/m2/h | ~60 | <0.05 | ||||
| Parker et al. (2004) | Urease inhibitor (NBPT) | Acid trap | Flux chamber | 1 kg/ha | 26 to 13 µg/m2/s | 49 | <0.05 |
| Urease inhibitor (NBPT) | Acid trap | Flux chamber | 2 kg/ha | 26 to 9 µg/m2/s | 68 | <0.05 | |
| Parker et al. (2011) | Urease inhibitor (NBPT) | Acid trap | Flux chamber | 5 kg/ha initially and then doubled every 4 days to a maximum of 40 kg/ha | 40 to 12 µg/m2/s | 73 | <0.05 |
| Urease inhibitor (NBPT) | Acid trap | Flux chamber | 5 kg/ha | 40 to 11 µg/m2/s | 70 | <0.05 | |
| Urease inhibitor (NBPT) | Acid trap | Flux chamber | Urea coated with NBPT at 0.1% (w/w) of urea | 19 to 6 kg/ha | 69 | <0.05 | |
| Parker et al. (2016) | Urease inhibitor (NBPT) | Chemiluminescence | Flux chamber | 1, 2, 4, 8, and 40 kg/ha | 31 to 30 µg/m2/s (40 kg/ha data) | 4 | N/S |
| Urease inhibitor (NBPT) | Acid trap | Wind tunnels | 40 kg N/ha of urea + NBPT | N/A | 79 | <0.05 | |
| Krol et al. (2020) | Urease inhibitor (NBPT) | Acid trap | Integrated Horizontal flux | 20, 30, 40 kg N/ha of urea + NBPT and urea+ NBPT + NPPT | N/A | 67 | N/A |
| Hutchinson et al. (1982) | Water application | Acid trap | Vertical gradient flux model | 60 mm precipitation | 42 to 25 µg/m2/s | 40 | N/A |
| After precipitation, surface drying for 2day | 25 to 65 µg/m2/s | Increased 160 | N/A | ||||
| Todd et al. (2005) | Water application | Acid trap | Flux gradient model | Precipitation (Dose: N/A) | 93 to 55 µg/m2/s | 41 | N/A |
| Pandrangi et al. (2003) | Water application | Acid trap | Flux chamber | 270 mL of water (at 9 day) | 8~16 to 10~18 µg/m2/s | Increased 26 | N/A |
| Saarijärvi et al. (2006) | Water application | Passive-diffusional samplers | Flux chamber | 20 mm of water | 25 to 11 µg/m2/s | 56 | N/A |
| Water application | Acid trap | Flux chamber | 5 mm of water | 451 to 335 µg/m2/s (for 1 day data) | 27 | <0.01 | |
| Parker et al. (2011) | Water application | Acid trap | Flux chamber | 173 mL of water | 40 to 25 µg/m2/s | 37 | <0.05 |
| Lee et al. (2023) | Water application | EC sensor | Flux chamber | 5 mm of deionized water | 36 to 39 µg/m2/s (by 4 days data) | Increased 8 | <0.01 |
Evaluation of management practices to mitigate NH3 emission in the post-excretion stage.
N/A, not available; N/S, not significant.
6.2.2 Water application
Water sprinklers are recognized to decrease dust emissions and have been adopted by some to mitigate heat stress for cattle, but they have not been used to mitigate NH3 from the beef cattle feedyard (
In summary, there is scientific agreement that the water application may mitigate NH3 emissions (27~56%) under carefully controlled conditions and over short time scales. However, because of the lack of consensus on the use of water application, there is a concern that the NH3 mitigation due to water sprinkling is temporary and generates more NH3 during the evaporation process, especially when rapid evaporation of water occurs due to hot, windy weather. The impact of the water application on NH3 emissions continues to be investigated and a clearer interpretation of this is expected to emerge in the future.
7 Discussion
The current major hurdle facing cattle feedyards in applying the above BMPs solely for NH3 mitigation is whether the practically achievable benefits justify their costs. To be specific, feed composition is made close to the requirements of cattle with safety margins, and the pre-excretion technologies (e.g., growth-promoting technologies) are used to increase the nutrient-use efficiency of cattle, minimizing the nutrient excretion in most feedyards. According to Legesse et al. (2018), through such improvements in livestock management and in reproductive efficiency, NH3 (kg) emitted per beef (kg) decreased 20% from 1981 to 2011. However, some studies have reported that the expansion of large-scale intensive livestock operations, such as CAFOs, has contributed to increasing total NH3 emissions (Legesse et al., 2018; Schultz et al., 2019; Wyer et al., 2022). Therefore, to mitigate NH3 emissions, higher-precision feeding and active use of pre- and post-excretion practices are necessary. However, overly strict implementation of precision feeding strategies may introduce unintended variability in livestock performance and increase operational costs due to reduced safety margins and the need to modify existing feedyard infrastructure. In addition, post-excretion BMPs constitute essentially unrecoverable expenses unless the BMP facilitates the production of a marketable product. Therefore, the benefits of the practices implemented to mitigate NH3 emissions while bearing additional costs are an important factor in the feedyard’s decision to implement BMP.
High ambient NH3 concentrations (average 42 ppm) have been reported to have a negative impact on the bovine lungs in respiration chamber-scale experiments, leading to increased total white cell and mononucleated cell counts (p< 0.05,
Based on the results currently reported, the following additional benefits can be considered for the use of BMP related to NH3 mitigation. Precision feeding and diet manipulation aims to provide nutrient supply more precisely with the nutrient requirements, thus the benefits include economic returns through reduced excretion to the environment and improved efficiency of resource utilization by leading to decreased feed intake and thereby decreased enteric CH4 emissions (Zuidhof, 2020;
In the case of manure amendment, it is not directly related to animal performance, but it is related to benefits for manure value (C:N ratio) and the mitigation of other gases (H2S, GHGs, and VOCs). The C:N ratio in manure could vary greatly depending on diet, manure storage, manure management, and feedyard environments. It is generally reported that the C:N ratio of beef and dairy manure is 10 to 15:1 (Okopi et al., 2024). While close to the optimal C:N ratio (20 to 30:1) for net N mobilization through soil microorganisms (Hadas et al., 1992), manure C is insufficient in most cases. Manure amendments, which are a C source and particularly physical amendment, can improve C:N ratio and a MC (50-70%) for composting and land application. In addition, manure amendments have been reported to be effective in mitigating various gas emissions from cattle manure (Wheeler et al., 2011; Spiehs et al., 2019; Kaikiti et al., 2021;
Lastly, the practice of water application was proposed as a method to reduce heat stress in terms of animal production, but it could potentially improve feed efficiency during the summer (Mader and Davis, 2004). Water application may be a cost-effective solution for industry PM control in some circumstances (Yonkofski et al., 2019), and it has been reported to have the mitigation effect of other gases (GHGs such as CH4 and N2O) as well (Parker et al., 2021). Precipitation, which is the natural way to apply water, was observed to mitigate the emission of CH4 and N2O below detection levels for several days after the precipitation event in the feedyard (Parker et al., 2021). In lab-scale experiments, increased N2O emission has been observed after precipitation for several days (Parker et al., 2017, 2018), but this phenomenon has not been observed on the field scale (Parker et al., 2021). Further research is still needed because there are concerns about more gas volatilization during the drying process after water application and practical research is necessary into how water can be applied to feedyards as precipitation to achieve beneficial effects.
The direction we should take to mitigate NH3 emissions in feedyards is to maximize N-use efficiency of beef cattle by optimizing the pre-excretion management while simultaneously minimizing the environmental impacts using post-excretion management. To encourage the adoption of a given management practice, more research is needed to quantify its benefits, to describe as fully as possible the conditions under which those benefits may be realized in practice and at scale, to develop new promising practices, and to reckon transparently with a practice’s perverse effects, if any.
8 Conclusion
NH3 emitted from beef cattle feedyards is a high-profile environmental concern because of health hazards, its contribution to fine particulate formation, and contamination of air and surface waters. Mitigation of NH3 emissions addresses social concerns, minimizes the risk of undesirable environmental events, and is important to the sustainability of the beef industry. In this review, we reported the state of the science concerning NH3 emissions from beef cattle feedyards, methods for quantifying NH3 emissions, NH3 EF, and some management practices to mitigate NH3. Ammonia emissions primarily come from urinary urea in cattle manure on feedyard surfaces. A significant portion of the N in the manure is converted to NH4+ and is eventually volatilized to the atmosphere as NH3. In the past, constant EFs were used to inventory NH3 emissions. Currently, NH3 EF estimated by process-based mechanistic models reflecting various factors affecting NH3 emissions in the feedyard environment are available. As process-based mechanistic models, the backward Lagrangian stochastic model was widely used to convert NH3 concentration measurements into emissions in the beef cattle feedyard. This review of current literature indicated the average NH3 emissions from the cattle feedyard as 119 g/head/day (ranging from 24 to 318 g/head/day), and the average NH3 flux rate as 58 µg/m2/s (ranging from 2 to 185 µg/m2/s). Although it is agreed that more realistic NH3 EF are being obtained using process-based models, there is still significant variation of estimated NH3 EF depending on the diet composition, the manure management, and the feedyard environment. We note the need to improve inventories of NH3 emissions into categories of manure management implemented and feedyard environment. Some mitigation strategies can be effective, such as manipulating the diet to reduce N excretion, increasing animal performance with growth-promoting technologies, and using manure amendments. Of those, precision diet feeding to meet, but not exceed, protein requirements appears to be the most practical way to reduce N losses. However, careful diet manipulation and additional research are needed to avoid unintended negative consequences for animal production.
Statements
Author contributions
ML: Data curation, Formal Analysis, Investigation, Visualization, Writing – original draft, Writing – review & editing. BA: Conceptualization, Funding acquisition, Methodology, Project administration, Resources, Supervision, Validation, Writing – original draft, Writing – review & editing. LT: Methodology, Resources, Validation, Writing – review & editing. JK: Methodology, Resources, Validation, Writing – review & editing. CB: Resources, Validation, Writing – review & editing. VG: Resources, Validation, Writing – review & editing. JS: Resources, Validation, Writing – review & editing. KC: Resources, Validation, Writing – review & editing.
Funding
The author(s) declare that financial support was received for the research and/or publication of this article. This research was funded by the NRCS Conservation Innovation Grant (project number NR213A750013G037), and additional support was provided by the Colorado Livestock Association.
Conflict of interest
The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.
Generative AI statement
The author(s) declare that no Generative AI was used in the creation of this manuscript.
Publisher’s note
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Supplementary material
The Supplementary Material for this article can be found online at: https://www.frontiersin.org/articles/10.3389/fanim.2025.1608387/full#supplementary-material
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Summary
Keywords
gas quantification, emission factors, emission mitigation, feedyard management practices, air quality, sustainable agriculture
Citation
Lee M, Auvermann BW, Tedeschi LO, Koziel JA, Brandani CB, Gouvêa VN, Smith JK and Casey KD (2025) Ammonia emissions from beef cattle feedyards: a review. Front. Anim. Sci. 6:1608387. doi: 10.3389/fanim.2025.1608387
Received
08 April 2025
Accepted
03 June 2025
Published
02 July 2025
Volume
6 - 2025
Edited by
Titus Zindove, Lincoln University, New Zealand
Reviewed by
Diego Ignacio Manriquez, Colorado State University, United States
Rangarirayi Lucia Mhindu, Midlands State University, Zimbabwe
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Copyright
© 2025 Lee, Auvermann, Tedeschi, Koziel, Brandani, Gouvêa, Smith and Casey.
This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.
*Correspondence: Brent W. Auvermann, Brent.Auvermann@ag.tamu.edu
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