Dietary Manipulation to Reduce Ammonia Emission from High-Rise Layer Houses

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

This Technology is Applicable To:

Species: Poultry (Layers)
Use Area: Animal Housing
Technology Category: Ration Manipulation
Air Mitigated Pollutants: Ammonia

System Summary

Ammonia (NH3) generation from poultry production is a result of microbial decomposition of uric acid and undigested nitrogen in bird feces. Ammonia emission is associated with nitrogen (N) content of the feces, which is influenced by feed composition and feed conversion efficiency of the bird. To reduce N content in feces, ration may be formulated with reduced dietary crude protein (CP) and supplemented with limiting amino acids (AA) to match bird dietary requirements, thereby improving digestive conversion efficiency. Utilization of lower CP diets with supplemented essential amino acids is a source reduction method to mitigate ammonia emission from layer hen production facilities. Lower N excretion in the bird feces due to lower total N intake can result in lower NH3 emission from the system. The lower CP diet used in this study had 0.4 to 1.2% less CP than the standard or control diet during various feeding phases. The lower CP diet resulted in about 10% ammonia emission reduction. Formulation based on nutritional requirement at different feeding phases is required to achieve emission reduction without affecting bird performance, i.e. egg production and case weight. The cost of low CP diet is about 1% lower than that of the standard dietary formulation (2008 prices).

 

Applicability and Mitigating Mechanism

  • Lower CP diet can have 0.4 to 1.2% lower CP than a standard diet during the various feeding phases.
  • Soy content is reduced in lower CP diets, and crystalline AA DL-methionine, L-lysine.HCL and L-threonine is supplemented to maintain the same essential AA levels in both diets for a given feeding phase.
  • Tryptophan and isoleucine in the lower CP diet may be slightly lower (from 0.02% to 0.06%) than those in the standard diets without affecting bird performance.

 

Limitations

  • Crude protein in the diet can only be reduced to certain level to avoid negatively impacting bird performance.

Cost

The cost for the lower CP diet with supplemented crystalline AA DL-methionine, L-lysine.HCL and L-threonine is about 1% lower than that for the standard diet. The cost advantage is better now with the current higher grain costs than in year 2003 when the study was conducted.

Authors

Y. Liang1, H. Xin2, R.S. Gates3, E.F. Wheeler4, K.D. Casey5, B.R.Behrends6, D.J.Burnham7
1University of Arkansas, Fayetteville, AR, 2Iowa State University,Ames, IA, 3University of Kentucky, Lexington, KY, 4Pennsylvania State University, University Park, PA, 5Texas AgriLife Research, Amarillo, TX, 6Agri-Tech, a Sparboe Company, Litchfield, MN, 7Aviagen, Huntsville, AL
Point of Contact:
Hongwei Xin, hxin@iastate.edu

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Dust and Ammonia Control in Poultry Production Facilities Using an Electrostatic Space Charge System

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

The proceedings, “Mitigating Air Emissions from Animal Feeding Operations”, with expanded versions of these summaries can be purchased through the Midwest Plan Service.

This Technology is Applicable To:

Species: Poultry
Use Area: Animal Housing
Technology Category: Other Treatment
Air Mitigated Pollutants: Particulate Matter, Ammonia

System Summary

Air quality within poultry production housing has been a major concern for years, particularly with regard to poultry health. The search for strategies to reduce particulate matter and ammonia emissions from animal housing has led to considerable interest in the poultry industry for practical systems to reduce these air emissions. An electrostatic space charge system (ESCS) was designed to reduce aerial dust and ammonia concentrations within a commercial broiler production house. A study was conducted within a commercial broiler house to evaluate the effectiveness of an ESCS for reducing dust and ammonia concentrations over a period of seven flocks. Results of this study indicate the ESCS significantly reduced airborne dust by an average of 43 percent and reduced ammonia by an average of 13 percent. Commercial application of this technology within the production house has the potential to improve in-house air quality and reduce emissions. Electrostatic fields have not been shown to produce adverse health effects in animals or humans. No differences in bird activity were observed in the form of decreased water consumption or increased mortality. No adverse effects of the continuous charge were observed in the form of stray voltage or static discharge at the feeder and water lines.

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Applicability and Mitigating Mechanism

  • An Electrostatic Space Charge System transfers a strong negative charge to airborne dust particles
  • The negatively charged particles precipitate out of the air to grounded surfaces.
  • Nitrogen compounds attached to the dust will also precipitate out of the air.
  • Application of an electrostatic space charge can be effective in reducing poultry house dust and ammonia concentrations in floor-raised meat-bird housing.
  • The system has the potential for use as an emissions control device exterior to animal housing.

 

Limitations

  • The incidences of static discharge to workers were minimal. The intensity of a discharge from direct contact with an ESCS ionizer was similar to touching a spark plug wire on a gasoline engine.

Cost

The cost of materials and installation of the experimental ESCS unit was approximately $4,000. Power consumption of the entire system was less than 100 watts during operation. It is reasonable to assume that a commercially available product would have a reduced capital outlay and quicker return on investment than the experimental prototype used within this study.

Authors

C.W. Ritz1, B.W. Mitchell2, B.D. Fairchild1, M. Czarick1, J.W. Worley11University of Georgia, 2 USDA Agricultural Research Service
Point of Contact:
Casey W. Ritz, critz@uga.edu

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Mitigation of Odor and Pathogens from CAFOs with UV/TIO2: Exploring Cost Effectiveness

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

This Technology is Applicable To:

Species: Swine, Poultry
Use Area: Animal Housing
Technology Category: Air Treatment (UV Photocatalysis)
Air Mitigated Pollutants: Volatile Organic Compounds, Odor, Pathogens

System Summary

Odor and target VOCs responsible for livestock odor are mitigated by UV-185 nm (‘deep’ UV) in presence of TiO2 as a catalyst into less odorous or odorless products such as CO2 and H2O. Percent removals from 80 to 99% were measured in lab-scale experiments involving simulated livestock VOCs/odorants and 1 sec irradiation with a low wattage 5.5 W lamp. Selected VOCs simulating livestock odor included p-cresol, sulfur-containing VOCs, and volatile fatty acids. Treatment cost of $0.25 per pig and continuous operation during growing cycle was estimated when the lab-scale results were extrapolated to typical ventilation rates and electricity cost at a swine finish operation in rural Iowa. The long-term goal is to develop cost-effective technology for the simultaneous treatment of odor and pathogens in livestock housing through logical progression of testing from lab-scale, through pilot-scale and finally at commercial scale. Such treatment would be applicable to both the inflow (for airborne pathogen control) and outflow air (for odor and pathogen control) at typical existing and new mechanically-ventilated barns.

Applicability and Mitigating Mechanism

  • Removal of VOCs and responsible for livestock odor in simulated barn air exhaust with UV light and advanced oxidation.
  • Research continues to move this technology from lab to commercial applications.
  • Potentially applicable to both the inflow (for airborne pathogen control) and outflow air (for odor and pathogen control) at typical existing and new mechanically-ventilated barns
  • On-demand, intermittent operation.

Limitations

  • This technology is still under development
  • Cost estimates are extrapolated from lab-scale experiments
  • Effects of particulate matter on UV treatment needs to be investigated
  • Effectiveness and costs associated long-term full-scale operation are not known at this time.

Cost

Treatment cost of $0.25 per pig and continuous operation during growing cycle was estimated when the lab-scale results were extrapolated to typical ventilation rates and electricity cost at a swine finish operation in rural Iowa. This cost could be further reduced for intermittent, on-demand operation. The capital costs would be mainly cost of ‘on-the-shelf’ deep’ UV lamps (currently at $90 for 10W lamp) and the cost of retrofitting of barn exhaust.

Authors

Jacek A. Koziel1,Xiuyan Yang1, Tim Cutler1, Shicheng Zhang1, Jeffrey Zimmerman1, Steven J. Hoff1, William Jenks1, Hans Van Leeuwen1, Yael Laor2, Uzi Ravid3, Robert Armon31Iowa State University, 2’Ya’ar Research Center, Agricultural Research Organization, Israel, 3Faculty of Civil and Environmental Engineering Technion, Haifa, Israel
Point of Contact:
Jacek Koziel, koziel@iastate.edu

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Effects of Waste Management Techniques to Reduce Dairy Emissions from Freestall Housing

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

The proceedings, “Mitigating Air Emissions from Animal Feeding Operations”, with expanded versions of these summaries can be purchased through the Midwest Plan Service.

This Technology is Applicable To:

Species: Dairy
Use Area: Animal Housing
Technology Category: Management
Air Mitigated Pollutants: Volatile Organic Compounds, Ethanol & Methanol

System Summary

Recent dairy emission research has identified alcohols (methanol and ethanol) as the major volatile organic compound (VOC) group originating from fresh waste (Shaw et al., 2007; Sun et al., 2008). Effective control of these alcohols from dairies will help the dairy industry meet regulatory standards, satisfy public concerns, and improve local and regional air quality. Enhancing industry typical freestall waste management practices, which currently are predominant practices like flushing and scraping of fresh waste, may provide a large impact on mitigation of oxygenated VOC emissions in a cost effective manner.

Our research has shown that flushing is more effective than scraping in reducing methanol (MeOH) and ethanol (EtOH) emissions from barns. Flushing three times daily versus scraping three times daily yields an emission reduction efficiency of 50% for both MeOH and EtOH. Furthermore, flushing frequency by itself significantly reduces emissions. A comparison of 3 times versus 6 times flushing daily showed decreased emissions by 79% for MeOH and 63% for EtOH.

Applicability and Mitigating Mechanism

  • Oxygenated VOC (e.g., alcohols MeOH and EtOH) are produced by fermenting microbes present in fresh waste
  • Frequent waste removal effectively mitigates MeOH and EtOH emissions from fresh waste
  • VOC alcohols are water-soluble and become effectively trapped in water when flushed
  • Flushing is more effective than scraping, and increasing flushing frequency further decreases VOC emissions

Limitations

  • Scraping methods leave a thin film of manure on concrete ground that continues to produce emissions

Cost

There is no cost associated with increasing the flushing frequency of a liquid manure handling system. Essentially, flushing frequency is increased, while the amount of water per flushing event is decreased. Since the water used to flush barns is recycled water from the lagoons, there is no cost to re-circulate lagoon water through the barn alleys.

Authors

M. Calvo, K. Stackhouse, Y. Zhao, Y. Pan, Ts Armitage, and F. Mitloehner, University of California, Davis
Point of Contact:
Frank Mitloehner, fmmitloehner@ucdavis.edu

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Multi-pollutant Scrubbers for Removal of Ammonia, Odor, and Particulate Matter from Animal House Exhaust Air

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

The proceedings, “Mitigating Air Emissions from Animal Feeding Operations”, with expanded versions of these summaries can be purchased through the Midwest Plan Service.

This Technology is Applicable To:

Species: Swine, Poultry
Use Area: Animal Housing
Technology Category: Scrubber
Air Mitigated Pollutants: Ammonia, Odor, Particulate Matter

System Summary

In The Netherlands, Germany and Denmark packed-bed biotrickling filters and acid scrubbers for removal of ammonia from exhaust air of animal houses are off-the-shelf techniques for ammonia removal (70 – 95% average removal). At the moment a new generation of so-called “multi-pollutant scrubbers” is being developed and tested that not only removes ammonia but also aims for significant removal of odor and particulate matter (PM10 and PM2.5) from the air. Recently a 3-year research program has started that monitors and aims to improve the performance of five farm-scale multi-pollutant scrubber from different manufacturers. The preliminary results show that the average ammonia removal is relatively high (83%, n = 7) but that the average removal of odor (40%, n = 8) and particulate matter (PM10: 43%, n = 2; PM2.5: 42%, n = 2) needs to be improved further.

Applicability and Mitigating Mechanism

  • Ammonia scrubbers consist of two types: either acid scrubbers or biotrickling filters
  • Multi-pollutant air scrubbers usually consist of two or more scrubbing stages where subsequent removal of coarse dust, ammonia and odor takes place
  • Scrubber are mainly applied in pig housings with central ventilation ducts; application in poultry housings are scarce because of high dust concentrations
  • Already 10% of all exhaust air from pig houses The Netherlands is treated; this equals a treatment capacity of 79 million m3/hour

Limitations

  • Odor and dust removal is less effective than ammonia removal, at least for now
  • High concentrations of coarse dust result in blockage of packing material and increased energy use (pressure drop)
  • Costs are considered high, but multi-pollutant scrubbers provide an option for large scale livestock operations to remain in operation in areas nearby residential areas and sensitive ecosystems

Cost

Investment and operational cost of scrubbers for newly built production facilities in € / animal space.
Acid Scrubber Biotrickling Filter Multi-pollutant scrubber (3-stage water/acid/biotrickling)
Investment Costs 32.8 43.5 50.3
Operational Costs (year^1):
Depreciation (10%) 2.6 3.4 4.2
Maintenance (3%) 1.5 1.8 2.0
Interest (6%) 0.8 1.0 1.2
Electricity use ((€ 0.11 kWh^-1) 3.3 3.8 3.7
Water use (€ 1.0 m^-3) 0.6 1.7 0.6
Chemical use (€ 0.6 L^-1 H2SO4, 98%) 1.4 n/a 0.7
Water discharge [b 0.6 2.5 1.0
Total operational costs (year^-1) 10.8 14.3 13.5

[a] The investment costs are based on a maximum ventilation capacity of 60 m3 animal place-1 h-1.
[b] Water disposal costs are assumed of € 10/m3 for discharge from acid scrubbing and € 2/m3 for discharge from biotrickling or water scrubbing. For the multi-pollutant scrubber, discharge water from the biotrickling or water scrubbing step is reused in the acid scrubbing step. The systems do not include a denitrification unit which might significantly decrease water discharge costs.
[c] n/a = not applicable.

Authors

Roland W. Melse, Nico W.M. Ogink, Bert J.J. Bosma; Animal Sciences Group, Wageningen University and Research centre, The Netherlands
Point of Contact:
Roland W. Melse, roland.melse@wur.nl

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Significant Odor Reduction from a Highly Efficient Micro-ecosystem based on Biofiltration

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

The proceedings, “Mitigating Air Emissions from Animal Feeding Operations”, with expanded versions of these summaries can be purchased through the Midwest Plan Service.

This Technology is Applicable To:

Species: Swine
Use Area: Animal Housing
Technology Category: Biofilter
Air Mitigated Pollutants: Ammonia, Hydrogen Sulfide, Particulate Matter, Odor

System Summary

Odor Cell Technologies LLC manufactures odor filtration technologies that attach to the exhaust ventilation of CAFO’s. These odor cells are approximately 1.2 m (4 feet) square hollow cubes with porous side walls filled with pine bark that vary in thickness depending upon the cfm and actual run-time of each stage of ventilation. Internal and external hydration is provided to the cells by a uniquely designed irrigation system controlled by timers and sensors. Odor cells utilize the principles of physical entrapment, water chemistry and microbial activity to dramatically improve air quality in and around agricultural and industrial facilities. Using the proven odor reducing principles inherent to composting, the organic odorous particles are entrapped, activated with moisture and attacked biologically at the point source. This allows naturally occurring bacteria to break down and cleanse gases and odors commonly found around these facilities. Odor Cell Technologies LLC‘s patented process creates a “micro-ecosystem” that significantly reduces odors and represents an environmentally friendly option to odor control. The successful installation of our technology has occurred on many sites throughout the Midwest.

Applicability and Mitigating Mechanism

  • Captures odorous organic particulate matter commonly produced by CAFO’s
  • Reduces NH3 and H2S concentrations
  • Utilizes an environmentally friendly filtering media, pine bark, that becomes biologically active with controlled hydration intervals
  • Cost efficient, durable, easily installed and maintained with positive aesthetic appeal
  • Ventilation efficiency can be easily monitored through physical inspection and static pressure measurements

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Limitations

  • Biofiltration is most effective on organic based odors and particulate matter
  • Media moisture levels need to be maintained between 30% and 65%
  • Static pressure requirements vary from .05 inches of water upon installation to .08 inches of water on a mature system
  • Pine bark may not be available at local retail outlets
  • Substitution of the recommended media may affect odor cell performance

Cost

Odor cell frames are constructed using stainless steel, DurameshTM hex netting, stainless steel tubing, nylon fittings and brass nozzles. These construction materials were chosen for durability and longevity due to the environment they will operate in. The following represents current pricing for the most common odor cells:

  • Standard P-8, $1200 plus $50 initial media fill
  • 5 inch odor cell, $1425 plus $65 initial media fill
  • 10 inch odor cell, $1650 plus $125 initial media fill
  • Porous rock base, approximately $20 per odor cell
  • Standard hydration package (Approximately $360 – timer, valves, control box, fittings , tubing, and hose)

Operational and maintenance costs are minimal. Media usage is approximately 10% per year. Hydration cycles can be controlled by an irrigation timer and rain sensor. A typical 1200 head swine finishing barn with 6 standard pit exhaust fans using all 10 inch odor cells would cost $11,130 upon installation (excluding shipping and labor) and $75 a year in operational expense. Assuming a complete change of media every 5 years, this equates to $.62 per pig space over 20 years or $.23 per pig produced over 20 years (assuming 2.6 turns per year).

Authors

Robert R. & Roger Treloar, Odor Cell Technologies LLC
Point of Contact:
Odor Cell Technologies LLC, odorcell@southslope.net

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Biofiltration: Mitigation for Odor and Gas Emissions from Animal Operations

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

The proceedings, “Mitigating Air Emissions from Animal Feeding Operations”, with expanded versions of these summaries can be purchased through the Midwest Plan Service.

This Technology is Applicable To:

Species: Swine, Dairy
Use Area: Animal Housing
Technology Category: Biofilter
Air Mitigated Pollutants: Hydrogen Sulfide, Ammonia, Methane, Volatile Organic Compounds, Odors

System Summary

A biofilter is simply a porous layer of organic material, typically wood chips or a mixture of compost and wood chips, that supports a population of microbes. Odorous building exhaust air is forced through this material and is converted by the microbes to carbon dioxide and water. The compounds in the air are transferred to a wet biofilm that grows on the filter material where microorganisms breakdown the odorous compounds.

Biofiltration can reduce odor and hydrogen sulfide (H2S) emissions by as much as 95% and ammonia by 65%. The method has been used in industry for many years and was recently adapted for use in livestock and poultry systems. Biofilters work in mechanically ventilated buildings or on the pit fans of naturally ventilated buildings. Biofilters can also treat air vented from covered manure storage.

Two configurations of biofilters are being used to treat exhaust air from swine buildings: a horizontal media bed and a vertical media bed. Horizontal biofilters require more land area but are less expensive than vertical biofilters. Horizontal beds can be shallow (< 0.45 m) or deep (> 0.75 m).

Applicability and Mitigating Mechanism

Key factors influencing biofilter size and performance:

  • time the odorous gases spend in the biofilter
  • volume of air treated
  • moisture content of the filter material
  • sizing the biofilter media volume
  • selecting fans capable to push the air through the biofilter
  • choosing biofilter media

Limitations

  • Biofilters are only effective when there is a captured air stream
  • Media moisture content effects the biofilter performance, i.e. dry media results in poor odor reduction
  • Media porosity is related to the fan’s ability to move air through the biofilter. If media is less than 50% porosity most agriculture ventilation fans will not perform satisfactorily

Cost

Costs to install a biofilter include the cost of the materials—fans, media, ductwork, plenum—and labor. Typically, cost for new horizontal biofilter on mechanically ventilated buildings will be between $150 and $250 per 1,700 m3/hr (1,000 cfm). A vertical biofilter is approximately 1.5 times the cost of a horizontal biofilter. Annual operation/maintenance of the biofilter is estimated to be $5-$10 per 1,700 m3/hr (1,000 cfm). This includes the increase in electrical costs to push the air through the biofilter and the cost of replacing the media after 5 years.

Authors

R.E. Nicolai1, K.J. Janni2, D.R. Schmidt21South Dakota State University, 2University of Minnesota
Point of Contact:
Richard Nicolai, richard.nicolai@sdstate.edu

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Practical Partial Biofiltration of Swine Exhaust Ventilation Air

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

This Technology is Applicable To:

Species: Swine
Use Area: Animal Housing
Technology Category: Biofilter
Air Mitigated Pollutants: Odor, Ammonia

System Summary

The mitigation technique discussed is to utilize biofiltration for a portion of swine barn ventilation air. The portion mitigated is that portion of air emitted into stable atmospheres. Stable atmospheres have poor vertical mixing potential and therefore gases and odors emitted tend to remain close to the earth’s surface and can therefore be sensed at longer distances downwind. It is impractical to mitigate all of the exhaust ventilation air required in swine housing. Techniques are needed that apply odor and gas mitigation to a portion of the ventilation air stream, when receptors might experience an odor event. Additionally, many barns incorporate combinations of fans and curtains (i.e. hybrid ventilated) to supply required ventilation air. Any mitigation strategy applied to barn ventilation air must be able to accommodate these hybrid ventilation systems as well.

Ventilation air exhausted during the heat of summer days is exhausted into an atmosphere that is, for the vast majority of times, very unstable providing excellent and natural mixing potential near the building source. In more stable atmospheres, typically present during the evening hours, biofiltration of a critical minimum amount of ventilation air (i.e. partial biofiltration) would reduce ammonia and odor emissions during those times when the potential for odor plumes to travel long distances is greatest. The overall effect would be a more attractive biofiltration strategy that maximizes ammonia and odor reduction potential when most needed.

Applicability and Mitigating Mechanism

  • Biofiltering of a critical minimum amount of ventilation air
  • Applies mainly to hybrid ventilated swine finishing facilities
  • Can be used as an odor “impact based” mitigation strategy

Limitations

  • Requires fan ventilation of barns up to about 81 m3/h-pig (48 ft3/min-pig)
  • Biofilter applications apply added stress to the ventilation system
  • Biofilters require ample water supply to keep the biofilter media in the 50-60% range

Cost

The biofilter application presented in this research required $4,959 for biofilter supplies and equipment including four new biofilter fans (300-head pig finishing room). Biofilter supplies, equipment, and construction labor resulted in a total implementation cost of $6,759 or $22.53/pig space. The added energy to operate the biofilter fans resulted in an additional $0.42/pig-produced.

Authors

Steven J. Hoff1, Jay D. Harmon1, Lide Chen1, Kevin A. Janni2, David R. Schmidt2, Richard E. Nicolai3, Larry D. Jacobson21Iowa State University, 2 University of Minnesota, 3South Dakota State University
Point of Contact:
Steven J. Hoff, hoffer@iastate.edu

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Gas Impermeable Film and Sheet for Control of Methane and Odors in Agricultural Applications

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

The proceedings, “Mitigating Air Emissions from Animal Feeding Operations”, with expanded versions of these summaries can be purchased through the Midwest Plan Service.

This Technology is Applicable To:

Species: Swine, Dairy, Beef, Poultry
Use Area: Manure Storage, Manure Treatment
Technology Category: Covers
Air Mitigated Pollutants: Odors, Methane, Ammonia

System Summary

For many years, food packaging has incorporated barrier layers to contain odors, flavors, oils and moisture along with the food contents while excluding contamination and oxygen. Until recently, agricultural films and geomembranes were monolithic structures employing only a single polymer or blend. Recent advances in extrusion and lamination equipment allow the incorporation of these barrier layers in large scale agricultural structures and operations such as floating covers over animal waste storage, containment geomembranes for biogas generation, silage storage and fumigation films.

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Co-extruding a thin layer of ethylene vinyl alcohol (EVOH) in a linear low density polyethylene (LLDPE) geomembrane dramatically reduces the permeability to a wide range of gases and volatile organic carbon molecules including: methane, ammonia, carbon dioxide, oxygen, aromatic hydrocarbons, aliphatic hydrocarbons, methyl bromide and most odorous compounds. Methane permeabilites for four geomembranes are given below.

Methane Permeability (cc/(m2*day))
PVC LLDPE HDPE Barrier LLDPE
0.76 mm (30 mils) 1.0 mm (40 mils) 1.0 mm (40 mils) 0.5 mm (20 mils)
900 690 300 <1

Applicability and Mitigating Mechanism

  • Barrier to noxious gases and odors
  • Useful in cover and containment systems

Limitations

  • EVOH is a crystalline polymer and is not elastic. It is flexible but should not be used as part of an elastomeric structure.

Cost

Engineered floating covers with ballasted weight systems, gas extraction systems and rainwater removal systems costs vary greatly. For waste lagoon of about 1/2 acre in size, the cover system can cost from $150,000 to $200,000. Addition of the barrier layer to the geomembrane adds less than $5,000.

Authors

Gary Kolbasuk, Raven Industries, Engineered Films Division
Point of Contact:
Gary.Kolbasuk@Ravenind.com

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.

Reduction of Ammonia Emission from Stored Laying-hen Manure Using Topically Applied Additives: Zeolite, Al+Clear, Ferix-3 and PLT

Reprinted, with permission, from the proceedings of: Mitigating Air Emissions From Animal Feeding Operations Conference.

The proceedings, “Mitigating Air Emissions from Animal Feeding Operations”, with expanded versions of these summaries can be purchased through the Midwest Plan Service.

This Technology is Applicable To:

Species: Poultry (Layers)
Use Area: Manure Storage
Technology Category: Chemical Amendment
Air Mitigated Pollutants: Ammonia

System Summary

Manure storage can be a significant source of ammonia (NH3) emission that could negatively impact the environment. Ammonia emission from manure storage may be controlled through physical, chemical and/or biological means. In this study, five treatment agents, including zeolite, 48.5% liquid Al+Clear (aluminum sulfate), granular Al+Clear (aluminum sulfate), granular Ferix-3 (ferric sulfate), and PLT (sodium bisulfate) were topically applied to stored nearly fresh laying-hen manure. Each agent was tested at three application rates, i.e., low, medium and high. Hen manure was stored in 19-litter Teflon-lined vessels under a constant ambient temperature of 23oC (73oF) and a ventilation rate of 11 air changes per hour (3 L/min). The NH3 concentrations and emissions from the vessels were measured and NH3 emission reductions by the treatment regimens were evaluated with reference to the control. The results show that there were no significant difference between the high and medium dosages for Al+Clear, Ferix 3, and PLT after the 7-d storage period. Reduction of NH3 emission by the topical application of the agents over a 7-day manure storage/testing period was as following: A) 36%, 62% or 92%, respectively, for zeolite applied at0.6, 1.3, or 1.9 lb/ft2 (3.1, 6.3, or 12.5 kg m-2) of manure surface area; B) 63% or 89%, respectively, for liquid Al+Clear applied at 0.2, or 0.4 lb/ft2 (1, or 2 kg m-2); C) 56% or 81% respectively, for dry granular Al+Clear applied at 0.1 or 0.2 lb/ft2 (0.5 or 1.0 kg m-2); D) 42% or 90%, respectively, for Ferix 3 applied at 0.1 or 0.2 lb/ft2 (0.5 or 1.0 kg m-2); and E) 74% or 90%, respectively, for PLT applied at 0.1 or 0.2 lb/ft2 (0.5 or 1.0 kg m-2).

 

Applicability and Mitigating Mechanism

  • NH3 volatilization from litter is dependent on pH, moisture content, air velocity, NH4 concentration, and temperature
  • Application of acidulant additives reduces litter pH and suppresses NH3 emission
  • Additives is topically applied to the fresh hen manure in storage

 

Limitations

  • An effective, automated delivery system(s) is (are) needed for the applications and should be fully investigated.
  • The material has a low pH and can be corrosive to handle
  • Ability of the acidulants to reduce pH, and thus reduce emissions, decreases over time

Cost

The costs of the additives with dry form are based on the 50 lb/pack prices of 2008. Ability of the additives to reduce emissions decreases over time. The costs of the topical application of the agents at end of the 7th day was as following: A) 1.56, 1.81 or 1.83 cent/ft2-10% NH3 reduction, respectively, for zeolite applied at 0.6, 1.3, or 1.9 lb/ft2 (3.1, 6.3, or 12.5 kg m-2) of manure surface area; B) 0.25 or 0.36 cent/ft2-10% NH3 reduction, respectively, for liquid Al+Clear applied at 0.2, or 0.4 lb/ft2 (1, or 2 kg m-2); C) 0.36 or 0.49 cent/ft2-10% NH3 reduction, respectively, for dry granular Al+Clear applied at 0.1 or 0.2 lb/ft2 (0.5 or 1.0 kg m-2); D) 0.46 or 0.42 cent/ft2-10% NH3 reduction, respectively, for Ferix-3 applied at 0.1 or 0.2 lb/ft2 (0.5 or 1.0 kg m-2); and E) 0.45 or 0.60 cent/ft2-10% NH3 reduction, respectively, for PLT applied at 0.1 or 0.2 lb/ft2 (0.5 or 1.0 kg m-2).

Authors

H. Li1, H. Xin1, R.S. Burns1, Y.Liang21Iowa State University, 2 University of Arkansas, Fayetteville, AR
Point of Contact:
Hong Li, lwblue@iastate.edu

The information provided here was developed for the conference Mitigating Air Emissions From Animal Feeding Operations Conference held in May 2008. To obtain updates, readers are encouraged to contact the author.