Performance of Additives in Reducing Ammonia Emissions from Cow Slurry
by Mats Andersson
(Revised edition)Preface
The emission of ammonia from manure contributes substantially to
environmental pollution and causes acidification in certain areas of Sweden.
The National Board of Agriculture in Sweden has therefore set the goal to
reduce the total ammonia emission from agriculture with 50 % before 2000
with the respect to 1990. In Sweden, 20 - 25 % of the total ammonia
emissions derive from manure in livestock buildings. The need to reduce
ammonia emissions from livestock buildings is therefore urgent. During the
last years, several additives for manure have been introduced on the Swedish
market. However, the efficiencies of these additives have not been
determined, and those additives which have been evaluated have been
difficult to compare due to different test methods.
The objective of this study has therefore been to determine the
efficiencies of different manure additives in reducing ammonia emissions.
The ammonia emissions from manure treated with different additives have been
analyzed in an ammonia measuring chamber developed at JBT (Dept. of
Agricultural Biosystems and Technology). Seven different additives were
evaluated in this investigation. The investigation has been conducted by Mr.
Mats Andersson, research assistant at the Division of Buildings-, Energy-
and Environmental Technology. Mr. Andersson has also compiled the data and
has written this report. The investigation has been financially supported by
the National Board of Agriculture in Sweden.
Lund in September 1994
Gösta Gustafsson
Head
Division of Buildings-, Energy- and Environmental Technology
Summary
Ammonia emissions contribute substantially to environmental pollution and
cause severe acidification. In Sweden, 20-25 % of the total ammonia emission
derives from manure in animal buildings. Different measures can be applied
to decrease emissions in animal buildings, but they are usually costly
and/or cause unsatisfactory living conditions for the animals. Simple
techniques can be used which would not interfere with the living conditions
for the animals if emission-reducing additives were applied in the manure.
The efficiencies of many of the manure additives on the market have not been
determined, and those additives that have been evaluated are difficult to
compare due to different test methods and methods of evaluation.
The objectives of this study were to investigate the abilities of
different manure additives in reducing ammonia emission, for how they would
be efficient, and to which cost the additives can be used. To be able to
measure the ammonia emission from manure treated with additives, an ammonia
measuring chamber was used. The chamber is designed as a climate chamber for
manure and with this technique it is possible to measure under controlled
conditions.
Seven different additives were evaluated in this study; Add A, Penac G,
Kemira No. 2, Kemira No. 5, Kemira No. 15, fly ash and Adsorb Plus. Two
concentrations of fly ash were evaluated. Three cow slurry samples per
treatment, except for Kemira No. 5, were used in the study. The ammonia
emission from the slurry samples were measured one day after, one week after
and six weeks after the application of the additives. Once every week the
slurry samples were stirred by hand and the crust formations were studied.
One day after the application of the additives in the slurry samples the
treatment with Kemira No. 2 and Adsorb Plus resulted in lower ammonia
emission than from the control (p<0.001). The emissions from the slurries
treated with these two additives were approximately 40 % and 50 % lower than
from the untreated slurries, respectively. At p<0.01, no significant
differences were found between the treatments with Kemira No. 15, fly ash
(low), Penac G and the control. At this significance level, the treatments
with Add A and fly ash (high) resulted in higher emissions than from the
control. The Kemira No. 5 treatment was not replicated and therefore hard to
evaluate. However, this single treatment indicated that this additive can
reduce the ammonia emission.
One week after the application of the additives the treatment with Kemira
No. 2 resulted in lower emission than from the control (p<0.001). The Adsorb
Plus treatment gave even better effect and the emissions were significantly
lower than from the treatment with Kemira No. 2 (p<0.001). Treatments with
these two additives resulted in approximately 40 % and 60 % lower emission
than from the untreated slurries, respectively. At p<0.05 and p<0.01, no
significant differences were found between the control and the other
treatments except with fly ash (high), which resulted in higher emissions
than from the control. The Kemira No. 5 treatment also seemed to have an
emission-reducing effect.
Six weeks after application of the additives, Adsorb Plus still reduced
the ammonia emission compared with the emission from the untreated slurries
(p<0.05). The approximate reduction was 30 %. At this significance level the
treatment with Add A resulted in a higher emission than from the untreated
slurries. All the other slurries treated with the different additives
emitted ammonia at the same rate as the control.
Specimens for Kjeldahl analyses were taken from all the slurry samples on
all the measuring occasions. Correlation analyses between the emission
results and the results from the Kjeldahl analyses were conducted. No good
correlations were found between the emission values and total-N, ammonium-N,
ammonium-N / total-N, total solids and pH-values, and the ammonia emission
values could thus not be explained by the results from the Kjeldahl
analyses.
Crust was formed on all the slurries during all of the six weeks of the
experiment. The thicknesses of the crusts were the same on all the slurries
on all the occasions, except on the one treated with Kemira No. 5 which was
about two times thicker.
A rough economic evaluation of the two best performing additives in this
study (Kemira No. 2 and Adsorb Plus) was also conducted. If an
emission-reducing effect only is expected in the livestock buildings when
applying the additives Kemira No. 2 and Adsorb Plus, the cost would be 780
SEK/kg saved nitrogen and 260 SEK/kg saved nitrogen respectively. If a
reduction of the emission from the slurry storages (two weeks) can also be
expected, the costs will be reduced to 740 SEK/kg saved nitrogen and 240 SEK/kg
saved nitrogen. This economic evaluation is approximate and should only be
used as an indication of the cost levels of using these two additives.
Background and Purpose of the Study
Nitrogen is the macronutrient taken up most by plants. It is, for
instance, a part of the protein and the chlorophyll of the plants. A good
supply of nitrogen in balance with other nutrients leads to strong
vegetative growth. Small changes in nitrogen supply usually have large
influences on the vegetation.
In Sweden during the last half century an increased nitrogen deposition,
due to atmospheric ammonium sulphate, has been detected. This has had a
stimulating effect on vegetative growth until recent years. Moderate
supplies of easy accessible nitrogen usually have a positive effect on
plants and to a certain degree also on fungus and micro-organisms. However,
in some parts of the country the nitrogen deposition has increased so much
that nitrogen saturation has occurred. A symptom of nitrogen saturation is
the increased nitrate leaching from the forest lands located in southern
parts of Sweden.
According to Jordbruksverket (1994), the average nitrogen deposition in
Sweden is approximately 2.2 kg/ha. However, local deposition figures vary
widely, with extreme values of up to 25 kg/ha in the southwest of Sweden (Jordbruksverket,
1991). As the critical load limits for lakes, water courses, soils and
plants throughout the country range between 5 and 15 kg/ha (Luft -90, 1990),
measures have to be taken to prevent an environmental catastrophe.
The nitrogen deposition in Sweden is made up of nitrogen oxides (60%) and
ammonia (40 %). Different combustion processes in motor vehicles and in
energy production contribute to most of the nitrogen oxides, while animal
manure is the main source of the ammonia (80-90 %). The ammonia emission
from animal manure is divided between animal buildings (20-25 %), manure
storages (25-30 %) and manure spreading (50 %).
Different measures can be applied to decrease the ammonia emission in
animal buildings, but they are usually costly and/or cause unsatisfactory
living conditions for the animals. To decrease ammonia emission by applying
additives to the manure, simple techniques can be used which would not
interfere in the living conditions for the animals. The efficiencies of many
of the manure additives on the market have not been determined, and those
additives that have been evaluated are difficult to compare due to different
test methods and methods of evaluation.
The objectives of this study were to investigate the abilities of
different manure additives in reducing ammonia emission, for how long they
would be efficient, and to which cost the additives can be used.
2 Literature Review
In the literature review in this report the processes with which the
ammonia is emitted from manure in animal buildings are described. Some of
the more promising manure additives according to Witter (1991 a), with
emphasis on the principles of their mode of action in reducing ammonia
emission, are also described.
Figure 1.
2.1 Ammonia emissions from animal buildings
2.1.1 A description of ammonia
At normal pressure and temperature ammonia is a gas, which easily reacts
with protons, metals or acid components and forms ions or complexes with
different stabilities (Rank, 1988). It has a strong affinity to water and in
the reaction an ammonium ion is formed. The equilibrium equation according
to Vlek & Craswell (1981) is:
The volatilization rate of ammonia depends on the evaporation of ammonia
into the atmosphere, changes in concentration of NH4+ or NH3 in the
solution, or any other displacement of the equilibrium equation (Rank,
1988). The equilibrium equation is displaced to the right as the temperature
is raised and/or the pH-value is increased (Jordbruksverket, 1991; Rank,
1988). The driving force of the ammonia volatilization from a solution is
differences in the partial pressure of ammonia between the liquid phase and
the atmosphere (Denmead et al., 1982; Freney et al., 1981; Svensson, 1993).
2.1.2 Conversion of nitrogen to ammonia in feces and urine
Nitrogen is excreted by animals both in the form of urine and in the form
of feces. Most of the nitrogen in feces is present in organic forms, while
in urine 65-90 % of the nitrogen is present as urea (Witter, 1991 a). In
fowl, about 60-70 % of the nitrogen excreted is in the form of uric acid.
The ratio of nitrogen excreted in faeces to that excreted in the urine
varies between species, but also depends on the protein level of the feed.
On average, 50-60 % of the nitrogen is excreted in the urine by pigs and
cows.
Ammonia emissions from livestock buildings originate from ammonia formed
by two processes. Organic forms of nitrogen present in the feces may
decompose and hydrolysis of urea, mainly in the urine, may occur. Because
hydrolysis of urea proceeds at a fast rate compared with mineralization of
nitrogen from the feces, urine is generally the main source of ammonia
emissions from livestock buildings. According to Hartung (1992) less than 1
% of the total ammonia emission from stored cattle slurry originates from
the feces (Table 1). Table 1 also shows that a decrease in ammonia release
is possible if water is added to the manure. However, huge amounts of water
are required. The ordinary composition of feces and urine in cow slurry is
2:1 (Frank, 1993).
Composition
of manure |
[%] |
Ammonia
release
[µ NH3/h] |
| Feces |
Urine |
Water |
|
| 100 |
- |
- |
3.1 |
| - |
100 |
- |
426.0 |
| 50 |
50 |
- |
120.0 |
| 75 |
25 |
- |
16.0 |
| 75 |
- |
25 |
3.4 |
| 50 |
- |
50 |
6.6 |
| 25 |
- |
75 |
9.7 |
| 5 |
- |
95 |
2.2 |
Table 1.
Volatilization of ammonia from stored bovine feces and urine with and
with-out added water kept at 30 °C (after Kellems et al., 1979).
Urea hydrolysis is mediated by the enzyme urease and yields ammonium and
carbonate, as follows:
 As soon
as urine comes into contact with faeces, which contain urease, the
conversion of urea starts (Elzing et al., 1992). The conversion rate of urea
into ammonia is temperature dependent, and is greatly decreased at
temperatures below 5-10 °C (Witter, 1991 a). Depending on the pH-value of
the system, gaseous ammonia and/or carbon dioxide may be formed. The optimum
pH-value for urease activity is usually between 6.5 and 7.0. Urea hydrolysis
can take place both under aerobic and anaerobic conditions. Hydrolysis of
uric acid is thought to proceed via the intermediates allantoin, allantoic
acid and urea (Witter, 1991 a). According to Witter (1991 a) and Demmers et
al. (1992), the hydrolysis of uric acid proceeds at a somewhat slower rate
than urea hydrolysis. This means that for fowl, which contains uric acid,
there is adequate time to dry the manure as an effective measure to prevent
formation of urea, and consequently of ammonia. 2.2 Different types of
manure additives
There is an abundance of manure additives of different types on the
market. The most common (and effective) ones can be divided into five groups
as follows:
- pH-regulators (acids)
- pH-regulators (soluble Ca- and Mg-salts)
- Urease inhibitors
- Adsorbents
- Biological immobilization of ammonium
There are some other interesting additives, besides those mentioned
above, which can not be sorted into specific groups. In this report these
additives are presented as "Other additives to reduce ammonia emission from
animal manure". 2.2.1 pH-regulators (acids)
Because the balance between ammonium and ammonia in solution is highly
pH-dependent, reduction of the pH-value to below 7 is a very effective way
in reducing ammonia losses (Hartung, 1992; Witter, 1991 a), see Figure 1.
Pure acids such as nitric, sulfuric or phosphoric acid are more cost
effective than acidic salts such as super phosphate or calcium sulfate
(gypsum) due to their greater solubility (Witter, 1991 a). The amount of
these chemicals that needs to be added to achieve a certain reduction in
ammonia emission is dependent on the solubility and reaction of the
chemical added and the pH-value and buffer capacity of the manure. Because
ammonia is alkaline, ammonia volatilization results in net acidification
of the manure. In an unbuffered system, ammonia volatilization is
therefore self-restricting. In a system where ammonia emissions occur from
urea, the carbonate formed upon urea hydrolysis provides the necessary
alkalinity to sustain ammonia volatilization (Witter, 1991 a). The
carbonate must thus be neutralized to prevent ammonia volatilization.
During the decomposition of organic forms of nitrogen, ammonia is formed
upon deamination of amino acids. Witter (1991 a) claims that it is likely
that this ammonia formation is the main source of alkalinity during the
decomposition of fresh feces, and thus explains the increase in pH-value
observed in the initial stages of the decomposition. Hence, the
calculation of the amount of acid required in solid manures is different
from the one of the required amount of acid in liquid manures.
The
balance between ammonium and ammonia depending on the pH-value (Miner,
1974).
The advantages with the use of acids in reducing ammonia emission from
manure are that virtually 100 % reduction in emission can be achieved and
when the acid is in the form of phosphoric or nitric acid, the fertilizer
value of the manure is increased.
The disadvantages with the use of acids are that they are highly corrosive
and hazardous to use, unless diluted with water. According to Witter (1991
a) the concentrated acids may violently react with the organic matter in
the manure, which probably results in the production of noxious gases. Due
to this fact, the use of acids is probably only realistic with slurries,
and not in the environment of livestock buildings. Spreading of acidified
slurry on soil will result in an acidification of the soil, and problems
with scorching of crops after application of slurries with nitric acid
have also been reported (Witter, 1991 a).
2.2.2 pH-regulators (soluble Ca- and Mg- salts)
Soluble magnesium or calcium salts have been added to manure since the
early part of this century with the purpose of reducing smell, and in some
cases in order to reduce ammonia emissions from the manure. The chloride
and nitrate salts of magnesium and calcium are mostly used, although any
soluble magnesium or calcium salt is suitable (Witter, 1991 a). The
sulfate salts of magnesium and calcium are not sufficiently soluble and
considerably less effective. Fenn et al. (1981) have, according to Witter
(1991 a), proposed a reaction mechanism for how the magnesium and calcium
salts work:


where
X = Cl- or NO3-
Precipitation of CaCO3 reduces ammonia volatilization as it reduces the
(NH4)2CO3 concentration, which easily decomposes to NH3, CO2 and water (Fenn
& Kissel, 1973):
(5)
Magnesium and calcium salts are effective in reducing ammonia
volatilization from manures whenever carbonate is an important source of
alkalinity driving the ammonia volatilization. Little is known, however,
about the different sources of alkalinity of manures.
Witter & Kirchmann (1989) achieved up to 50 % reduction in ammonia
emission during aerobic decomposition of chicken manure through the
addition of CaCl2 and MgCl2. Because of resolubilization of the CaCO3
formed, the efficiency in reducing ammonia emissions is reduced over time.
Witter (1991 b) found that addition of CaCl2 to fresh chicken manure
applied to soil reduced peak rates of ammonia emission after three days by
70 %, but after two weeks the reduction in ammonia emission was less than
40 %.
The advantages with chloride and nitrate salts of magnesium and calcium
are that they are non-hazardous and inexpensive. Nitrate salts have the
advantage of improving the fertilizer value of the manure.
The chloride salts have the disadvantage of increasing the chloride
content of the manure and hence also the chloride content in the soils on
which the manure is spread. The magnesium and calcium salts are effective
in reducing ammonia emission only during a couple of weeks, and are
therefore restricted to use in animal buildings.
2.2.3 Urease inhibitors
Urease inhibitors have been developed in order to reduce ammonia emissions
from urea fertilizers after application to soil. Some of these urease
inhibitors may also be effective in reducing ammonia emissions from
manures where the emission is associated with urea hydrolysis such as
occurs in animal buildings.
Witter (1991 a) claims that of the known urease inhibitors only one group,
phosphoramides, appears to be sufficiently effective in reducing ammonia
emission. Beyrouty et al. (1988) tested some phosphoramide compounds in
the field and found that urea hydrolysis could be reduced by up to 70 %
over a time period of 4-10 days after application of the urea to the soil.
The compounds differed in effectiveness and were differently affected by
the pH-value in the soil. Most of the compounds were more effective under
acidic rather than alkaline conditions.
Investigations concerning the effects of urease inhibitors on ammonia
emissions in animal buildings are scarce (Witter, 1991 a). According to
Kemme et al. (1993), research on pigs on the effects of urease inhibitors
has mainly been focused on performance.
Additives which have attracted great interest lately are those which are
based on an extract (sarsaponin) from the Yucca palm (Yucca schidigera).
The Yucca schidigera plant grows almost exclusively in the south-western
deserts of the USA. Its ability to grow under such adverse conditions is
due to the plant’s capability of binding ammonia (Headon & Walsh, 1993).
The Yucca extract is used either as a feed additive or an additive for
manure. As a feed additive, the product is claimed to improve feed
conversion efficiencies in pigs and chickens, and because of its residual
urease inhibitory properties, to reduce ammonia emission from manure in
animal buildings (Witter, 1991 a). As an additive for manure, ammonia
emission reductions have been obtained in some investigations carried out
in the USA (Headon & Walsh, 1993; Kemme et al., 1993). However, in other
studies conducted by Kemme et al. (1993) ammonia emission from manure was
not reduced when recommended doses of the Yucca extract were added (Microaid).
At higher doses the maximal reduction in ammonia emission was 22 %. In
this trial it was asserted that the mode of action of the Yucca additive
relies on binding or converting ammonia rather than on inhibiting the
enzyme urease.
Use of urease inhibitors may be an effective way to reduce ammonia
emissions from animal buildings. They will probably have less effect on
emissions from manure storages, because there the ammonia is derived from
ammonification of organic matter. If the urease inhibitor used improves
the feed conversion efficiency in the animals there is an added incentive
for farmers to use the compound.
A disadvantage with urease inhibitors is the temporary effect of
reduction, which makes them suitable only for animal buildings (Witter,
1991 a). Further, little is known about the persistence and possible
side-effects of these additives in the environment.
2.2.4 Adsorbents of ammoniacal nitrogen
There is a variety of substances which are effective in adsorbing either
ammonia, ammonium or both. Adsorption of ammoniacal nitrogen reduces the
ammonium content in the manure, and thereby ammonia volatilization. Of the
different materials, clay minerals and peat seem to be the most efficient
ones. Neither bilaminar (e.g. kaolinite) nor multilayer clay minerals
(e.g. montmorillonite) have shown an increased binding activity for
ammonium ions (Krieger et al., 1993). Clinoptilolites, which are
three-dimensionally constructed natural zeolites, on the other hand, seem
to work (Krieger et al., 1993; Witter, 1991 a). Clinoptilolites are used
as either feed additives or manure additives. In some investigations,
clinoptilolites have improved the feed conversion efficiency (Airoldi et
al., 1993), while in other investigations the feed conversion efficiency
has not been improved at all (Witter, 1991 a). Pond & Yen (1980) reported,
according to Krieger et al. (1993), that the effect depends on
concentration, particle size and the geographical origin of the
clinoptilolite used. In an experiment conducted by Airoldi et al. (1993),
a zeolite content of 10 % in the ration was required to reduce ammonia
emission from the manure. Witter & Kirchmann (1989) have tested
clinoptilo-lite as an additive for manure and they showed that the
additive is mainly effective in adsorbing ammonium and not ammonia. Its
ammonium adsorption capacity was about 18 mg NH4+ -N/g.
Peat (in particular Sphagnum fuscum derived peat) is, in contrast to
clinoptilolite, more effective in adsorbing ammonia than ammonium. The
ammonia adsorption capacity of peat is 23 mg NH3 -N/g (Witter, 1991 a),
and increases as the pH-value decreases (Kapuinen, 1992). Whereas most of
the ammonium adsorbed by zeolites is held in an exchangeable form, and may
hence be available for plant uptake or may be removed from the zeolites by
ion-exchange, less than 40 % of the ammonia adsorbed by peat is held in an
exchangeable form (Witter & Kirchmann, 1989).
The advantages with zeolites and peat are that they are effective in
reducing ammonia emissions by adsorbing ammoniacal nitrogen and they are
also non-toxic, non-hazardous and valuable soil conditioners when added to
the soil with the manure.
A disadvantage with these additives is that they are costly to use. Peat
is native to Sweden, whereas zeolites have to be imported which in most
cases makes the use of the former more economical.
2.2.5 Biological immobilization
The microbial activity in the manure is often limited by a lack of
suitable substrates. Addition of such an substrate will therefore result
in increased microbial activity and the decomposition of the added
material. By adding carbon-rich organic materials to manure, the ammonium
nitrogen may be converted into organic forms of nitrogen during
decomposition of the added material. Of the carbon (energy) utilized by
the microorganisms about half is used for maintenance requirements, and
under aerobic conditions, the used carbon is respired as carbon dioxide.
The rest of the carbon in the added organic material is used in synthesis
of new microbial cells, thus increasing the microbial population (Witter,
1991 a). Not only carbon is used in the synthesis but also nitrogen,
amongst other macro- and micronutrients. If the added substrate has a low
nitrogen content, for instance due to a high C/N-ratio, the microorganisms
may use the inorganic forms of nitrogen (ammonium and nitrate) in the
manure. These inorganic forms of nitrogen have thus become biologically
immobilized by the incorporation into new microbial tissue.
The added substrate will eventually become exhausted, and the newly formed
microorganisms will die and serve as substrates for the remaining
microorganisms. The previously immobilized nitrogen will then be
remineralized, and hence increase the ammonium content of the manure which
may lead to ammonia volatilization. To enhance microbial immobilization of
nitrogen and reduce ammonia volatilization, the added substrates must
therefore have the following characteristics (Witter, 1991 a):
- High C/N-ratio.
- The carbon must be in a form that can be readily metabolized by
microorganisms.
- The substrate should ideally provide both rapidly and slowly available
forms of carbon. If the carbon is readily available the substrate must be
added gradually in small doses.
Biological immobilization of nitrogen is an effective method of reducing
ammonium levels in manures, given that a suitable carbon substrate is
available. There are no environmental side-effects associated with this
method, and the initially immobilized nitrogen will later be remineralized
when the manure is applied in the field.
There are some disadvantages connected with this method of reducing
ammonia volatilization from manure. According to Kirchmann & Witter
(1989), no nitrogen immobilization occurs during anaerobic storage of
manures. This means that the method is suitable for solid manures during
storage under aerobic and semi-aerobic conditions as well as in
deep-litter systems, but is less suitable for slurries. Furthermore, the
effective-ness of this method is highly dependent on the characteristics
of the substrate added, the application rate, and ammonium content and
nitrogen mineralization pattern of the manure. There has been too little
research in this field yet to be able to come up with firm recommendations
on the suitability of this method to reduce ammonia emissions from manure.
At JBT, investigations concerning different types of substrates are in
progress, which will yield results during 1995.
2.2.6 Other types of additives to reduce ammonia emissions from animal
manure
There are some other additives on the market which are effective in
reducing ammonia volatilization from manure, but they are less interesting
due to the cost of using them or the environmental impacts associated with
them.
Formaldehyde. When formaldehyde reacts with ammonia a stable organic
complex is formed. Furthermore, the anti-microbial properties of
formaldehyde may inhibit urease and ammonification (Witter, 1991 a). The
additive is hazardous to use and may have negative side-effects after
spreading of the manure.
Lime. Ammonia volatilization from manure can be reduced by liming to a
pH-value above 10, thereby inhibiting the urease. It is difficult to
maintain such a high pH-value in the manure, and the fact that a somewhat
lower pH-value (8-9) will favor ammonia volatilization gives little scope
for this method to reduce ammonia volatilization.
MAP-method. By adding phosphoric acid and magnesium oxide to the manure
(slurry), it is possible to remove the ammonium from the slurry through
precipitation of ammonium as MgNH4PO4 x 6H2O, a salt with low solubility
at an alkaline pH. This new technique (the MAP-method) has been developed
by a German company, Moderne Abwasser-Prozesstechnik GMBH. The
precipitated salt can be sedimented out and can be used as a NPMg-fertilizer.
Using this technique, up to 95 % of the ammonium from the slurry can be
removed. The MAP-method was originally developed for waste water
treatment, and to use it with animal slurries the slurries first have to
be separated into a solid and a liquid phase. The ammonium in the liquid
phase is then removed. Even though the MAP-method is very effective in
reducing ammonia volatilization from slurries, the method will probably
not become widespread due to high costs.
3 Materials and Methods
3.1 The additives used in the study
The additives that were evaluated in the study were:
- Add A
- Penac G
- Kemira No. 2
- Kemira No. 5
- Kemira No. 15
- Fly ash
- Adsorb Plus
Add A is a product marketed by the company Biosolv located in
Stockholm. The additive consists of optional anaerobic bacteria, and the
bacterias are of many different species, e.g. a microbial consortium (Biosolv,
1993). The price of the product is about 105 SEK/l (1992).
Penac G is marketed by the company Penac located in Trelleborg. The
product consists of silicon dioxide which is ground to a fine texture ( =
0.05 mm), and "oxygen treated" (Penac, 1993). The price is about 200 SEK/kg
(1993).
Kemira No. 2 consists mainly of superphosphate Ca(H2PO4)2 and
gypsum CaSO4 . 2H2O. The price is about 2.50 SEK/kg (1993).
Kemira No. 5 consists of peat impregnated of calcium chloride CaCl2
and superphosphate Ca(H2PO4). The price of the product is about 1 SEK/kg
(1993).
Kemira No. 15 consists mainly of hydrogen peroxide H2O2, calcium
chloride CaCl2 and propionic acid CH2CH2COOH. The price is about 3.20 SEK/kg
(1993). All the Kemira-additives are marketed by Kemira AB, located in
Helsingborg (Kemira, 1993).
Fly ash is a rest product from burning of fossil fuels. Fly ash consists
mainly of three components; silicon dioxide SiO2, calcium chloride CaCl2
and dialuminum trioxide Al2O3. The price is lower than 1 SEK/kg (1994)
when imported in large quantities from Denmark. Fly ash is no longer
marketed in Sweden due to excessively high sulphur contents.
Adsorb Plus consists mainly of superphosphate Ca(H2PO4)2 and copper
sulphate CuSO4. Adsorb Plus is marketed in Sweden by Hygrisan AB, located
in Malmö (Hygrisan, 1993). The price of the product is about 5.80 SEK/kg
(1993).
3.2 The measuring chamber
3.2.1 Design
To be able to measure the ammonia emission from manure treated with the
additives an ammonia measuring chamber was used, which was described by
Andersson (1994).
The measuring chamber is designed as a climate chamber for manure. The
chamber consists of a container (bottom area 0.25 m2) in which the manure
(0.010 m3) is kept, and a hood equipped with a ventilation system and
placed on top of the container (Figure 2). The manure temperature is
controlled by an electrically heated water bath (0.045 m3) in which the
container is immersed. To be able to keep uniform water temperature, the
water tank is insulated and the water is circulated by an aquarium pump.
The ventilation hood on the container is equipped with an air intake duct
in the rear (Ø = 0.07 m), an air outlet with an exhaust fan in the front,
a dust filter in front of the exhaust fan and an air mixing fan. The
intake air is, cooled by a heat exchanger, untreated, or heated by a
heating fan. The following parameters can be steplessly varied or may be
kept constant; air flow rate, inlet air temperature and manure
temperature.
Figure 2. A section of the measuring chamber.
The temperatures in the water bath, the manure, the inlet air and the
outlet air are measured using PT 1000 sensors and the relative humidity in
the inlet air is measured using capacitive sensors (Rotronic). The air
flow rate is measured using an orifice plate and a pressure gauge. Through
the dust filter, exhaust air is sucked into an infrared-analyzer (Miran
203) to measure the ammonia concentration. All the parameters mentioned
are continuously recorded by a personal computer via data loggers.
3.2.2 Performance characteristics
The air flow rate through the measuring chamber is steplessly variable
between 30 and 200 m3/m2 h. At the lowest and the highest level the
coefficient of variation (C.V.) of the air flow rate is calculated to 4.1
% and 1.9 % respectively. As the air flow rate is changed the ammonia
volatilization reaches a constant level after approximately 20 minutes.
The stirring fan in the measuring chamber mixes the inlet air by blowing
it diagonally backwards. In one experiment, the air mixing efficiency was
measured by sucking in samples of air over a cow slurry surface through a
thin metal tube from 24 evenly distributed different spots in the chamber.
In Figure 3 each pillar represents an average value of the samples
collected from the three spots sideways in the chamber. The sample spots
were arranged at three levels; high, medium and low. The air flow rates
were 60 m3/m2 h and 140 m3/m2 h. The air at the high level in the chamber
was found to be thoroughly mixed (C.V. = 7.1 % at 60 m3/m2 h and C.V. =
6.4 % at 140 m3/m2 h). At the medium level and the low level in the
chamber the concentration of ammonia tended to increase close to the
chamber gable with the exhaust fan, which is in accordance with the
results found by van Beek (1990) in his investigations on poultry houses.
The C.V. of the ammonia concentration at the medium level was calculated
to 16.2 % and 10.7 % respectively.
Figure 3.
Ammonia
concentrations in different spots in the chamber over a cow slurry
surface. A1 = High level 60 m3/m2 h, B1 = Medium level 60 m2/m2 h, Cl =
Low level 60 m3/2 h, A2 = High level 140 m3/m2 h, B2 = Medium level 140
m3/m2 h, C2 = Low level 140 m3/m2 h, a = Close to air inlet duct, B =
Middle of the chamber, C = Close to exhaust fan.
In another experiment, the decline of ammonia emission was investigated.
Preheated (30 °C) and room temperate (15 °C) cow slurry was used and the
air flow rate was 140 m3/m2 h. The ammonia concentration and the air flow
rate were continuously recorded. Two and five hours of operation resulted
in a 7 % and a 20 % decrease in ammonia emission from preheated slurry,
respectively. The corresponding figures with room temperate slurry were 2
% and 7 %. These results show the importance of quickly conducted ammonia
emission experiments, especially at high temperatures.
Measurement accuracy of the measuring chamber was calculated to 1.7 % as
the C.V. of duplicate determinations of the ammonia volatilization. Six
samples of thoroughly mixed cow slurry were used in this study.
3.3 The measuring procedure with the chamber
The measuring procedure with the chamber consisted of three parts:
Treatments of the manure samples.
Ammonia emission measurements with the chamber.
Treatments of the manure between the measuring occasions.
3.3.1 Treatments of the manure samples
The manure that was used in the study was fresh (one day old) homogeneous
cow slurry. The slurry was distributed in 0.005 m3 portions in 0.010 m3
buckets, so that three slurry samples per treatment were obtained. Two
doses of fly ash and one dose of each other additive were to be evaluated,
which gives 27 slurry samples all together (including three untreated)
that would be portioned. However, the additive Kemira No. 5 was only
sufficient for one slurry sample, and hence 25 slurry samples were used.
The doses of the additives in the slurry samples (0.005 m3) were in
accordance with the recommendations of the different companies:
- Add A, 50.0 x 10-6 m3
- Penac G, 4 x 10-4 kg in 3.0 x 10-6 m3 water
- Kemira No. 2, 135.0 x 10-3 kg
- Kemira No. 5, 68.0 x 10-3 kg
- Kemira No. 15, 1.0 x 10-6 m3
- Fly ash, 5.0 x 10-3 kg (Low)
- Fly ash, 50.0 x 10-3 kg (High)
- Adsorb Plus, 25.0 x 10-3 kg
- Control, untreated
In the calculations of the amounts of substances that were to be added to
the slurry samples, a content of 4 x 10-3 kg nitrogen / kg slurry, of
which 2 x 10-3 kg / kg slurry was ammonium nitrogen, was assumed. It was
also assumed that all the ammonium nitrogen would be converted into
ammonia, and hence the doses of additives were calculated for 2 10-3 kg
nitrogen / kg slurry. The additives were thoroughly mixed by hand in the
buckets with slurry, which then were stored uncovered in a place with the
same climate conditions as in the place with the measuring chamber.
3.3.2 Ammonia emission measurements with the chamber
The ammonia emission from the treated slurry samples were measured with
the chamber on three occasions; one day after, one week after, and six
weeks after the application of the additives.
On each measuring occasion the slurry samples were poured one by one into
the container of the measuring chamber. Specimens for Kjeldahl analyses
(total-N, ammonium-N, total solids and pH) were taken from the slurry
samples. The hood, which is equipped with the ventilation system, was
placed on the manure container, and the measurements were started. Each
measuring period lasted for 20 minutes, which has been found to be
sufficient for the ammonia emission to reach a constant level (Andersson,
1994).
Between the measuring periods, the manure container was thoroughly washed
and dried to prevent any influence from other slurry samples. The total
time required for the measuring period, washing and change of slurry
sample was 40 minutes per slurry sample. The ammonia emission from 25
slurry samples was measured, which required two days of work on each
measuring occasion. To avoid systematic errors, like daily variations in
inlet air temperature, relative humidity in the inlet air etc, the start
order of the slurry samples was randomized. After each measuring period,
the slurry samples were poured back into the bucket and put in the store
room.
A sampling interval of two minutes between measurements of slurry
temperature, inlet air temperature and relative humidity in the inlet air
was used. The experiments were conducted at a air flow rate of 60 m3/m3 h.
3.3.3 Treatments of the manure between the measuring occasions
The slurry samples were mixed by stirring them by hand once a week during
the storage period in order to ensure a uniform ammonia emission, which
otherwise would be pre-vented by crust on top of the slurry. The three
measuring occasions were all conducted one day after a mixing occasion.
The mixing results in a oxygen supply in the slurry, which to some extent
leads to aerobic conditions. The fatty acids in the slurry will then break
down which results in an increase in the pH-value at which ammonia
volatilization becomes greater (Jordbruksverket, 1991).
This emission peak lasts for a couple of hours, after which the emission
of ammonia stabilises. By mixing the slurry the day before a measuring
occasion, the influence of the emission peak which may be expected when
pouring the slurry samples in the manure container of the measuring
chamber will be reduced. The ammonia emission from the different slurry
samples will thus be easier to determine.
4 Results
4.1 Statistical analyses
To be able to evaluate the abilities of the additives in reducing ammonia
emission from manure, comparisons of the means of the emission values were
made by employing the GLM (General Linear Model) model data processing
system. Tukey´s range test was used, and this test controls the Type 1
experiment wise error rate. The significance levels were p<0.05, p<0.01
and p<0.001. In order to attempt to explain the emission results with the
results from the Kjeldahl analyses, correlation analyses (Pearson´s
correlation coefficient) between the variables were conducted at the
significance level p<0.05.
All the climate parameters recorded during the emission experiments are
presented as means with standard deviations.
4.2 The first measuring occasion
| |
Slurry
temperature [°C] |
Inlet air
temperature [°C] |
Relative humidity
in the inlet air [%] |
| Day |
x |
S |
x |
S |
x |
S |
| 1 |
11.36 |
0.53 |
9.51 |
0.38 |
59.0 |
2.0 |
| 2 |
10.82 |
0.51 |
8.99 |
0.31 |
57.6 |
1.7 |
| 1+2 |
0.52 |
11.10 |
9.26 |
0.35 |
58.3 |
1.9 |
|
x = Mean value, S = Standard deviation |
In Table 2 the climate conditions with variations during the two days
of the first measuring occasion are presented. As can be seen in the
table, the variations during each day as well as during the two days
together were relatively small. The variations were considered so small
that they would not influence the ammonia emission levels. The climate
conditions and the ammonia emissions at each measurement are presented in
Table 3.
Table 2. The climate variations during the two days of measuring on the
first occasion.
Table 3. The ammonia emissions from the slurry samples and the climate
conditions during each measuring period on the first measuring occasion.
Treatment
No. |
Additive |
Ammonia
emission
[mg/m² h] |
Slurry
temperature [°C] |
Inlet air
temperature [°C] |
Relative humidity
in the inlet
air [%] |
| |
|
|
x |
S |
x |
S |
x |
S |
| 1 |
Add A |
354 |
10.84 |
0.09 |
9.52 |
0.22 |
60.0 |
0 |
| 1 |
Add A |
354 |
11.27 |
0.13 |
9.84 |
0.16 |
54.0 |
0.8 |
| 1 |
Add A |
358 |
11.32 |
0.50 |
9.67 |
0.13 |
59.6 |
0.5 |
| 2 |
Penac G |
354 |
10.60 |
0.01 |
9.30 |
0.35 |
55.3 |
0.8 |
| 2 |
Penac G |
339 |
10.27 |
0.22 |
8.73 |
0.09 |
57.0 |
0 |
| 2 |
Penac G |
324 |
10.54 |
0.20 |
9.51 |
0.23 |
58.3 |
0.5 |
| 3 |
Kemira No. 2 |
200 |
10.88 |
0.04 |
9.42 |
0.29 |
60.5 |
0.5 |
| 3 |
Kemira No. 2 |
177 |
10.94 |
0.15 |
9.29 |
0.22 |
57.8 |
0.4 |
| 3 |
Kemira No. 2 |
193 |
10.50 |
0.20 |
8.97 |
0.17 |
58.0 |
0 |
| 4 |
Kemira No. 5 |
247 |
11.04 |
0.29 |
9.70 |
0.07 |
60.0 |
0 |
| 5 |
Kemira No. 15 |
339 |
11.02 |
0.22 |
9.74 |
0.10 |
60.0 |
0 |
| 5 |
Kemira No. 15 |
339 |
10.28 |
0.49 |
8.63 |
0.05 |
56.1 |
0.3 |
| 5 |
Kemira No. 15 |
347 |
10.74 |
0.18 |
9.03 |
0.49 |
60.1 |
0.4 |
| 6 |
Fly ash (Low) |
327 |
10.40 |
0.43 |
8.93 |
0.41 |
57.8 |
0.4 |
| 6 |
Fly ash (Low) |
362 |
11.03 |
0.30 |
9.69 |
0.17 |
60.0 |
0 |
| 6 |
Fly ash (Low) |
347 |
10.32 |
0.44 |
8.82 |
0.04 |
55.0 |
0 |
| 7 |
Fly ash (High) |
347 |
10.52 |
0.20 |
8.86 |
0.23 |
58.9 |
0.0 |
| 7 |
Fly ash (High) |
370 |
10.91 |
0.33 |
9.63 |
0.25 |
60.0 |
0 |
| 7 |
Fly ash (High) |
362 |
10.89 |
0.26 |
9.17 |
0.64 |
59.0 |
0.6 |
|
8 |
Adsorb Plus |
146 |
10.35 |
0.11 |
8.77 |
0.27 |
55.7 |
0.5 |
| 8 |
Adsorb Plus |
154 |
10.60 |
0.01 |
8.90 |
0.01 |
55.3 |
0.5 |
| 8 |
Adsorb Plus |
150 |
10.98 |
0.35 |
9.60 |
0.23 |
60.0 |
0 |
| 9 |
Control |
308 |
10.60 |
0.16 |
9.28 |
0.06 |
59.4 |
0.5 |
| 9 |
Control |
308 |
10.71 |
0.25 |
9.20 |
0.08 |
60.0 |
0 |
| 9 |
Control |
327 |
10.70 |
0.14 |
9.29 |
0.02 |
60.0 |
0 |
|
x = Mean value, S = Standard deviation |
Table 4 shows the results from the statistical evaluation of the manure
additives. Means of the emission values of each treatment with the same
grouping letter are not significantly different. The treatment with Kemira
No. 2 and Adsorb Plus showed good effect and were significantly different
from the control (p<0.001). The emissions from the manures treated with
these additives were approximately 40 % and 50 % lower than from the
untreated slurry, respectively. At p<0.01, no significant differences were
found between the treatments with Kemira No. 15, fly ash (low), Penac G
and the control. At this significance level, the treatments with Add A and
fly ash (high) resulted in higher emissions than from the control. The
Kemira No. 5 treatment was not replicated and therefore hard to evaluate.
However, this single treatment indicated that this additive can reduce the
ammonia emission.
Table 4.
Means of the ammonia emission values of each treatment on the first
measuring occasion. Means with the same grouping letter are not
significantly different (p<0.05, p<0.01 and p<0.001).
| Treatment
No. |
Ammonia
emission
[mg/m² h] |
Grouping letters at each significance level |
| |
x |
S |
p<0.05 |
p<0.01 |
p<0.001 |
| 1. Add A |
355 |
2 |
A |
A |
A |
| 2. Penac G |
339 |
15 |
A,B |
A,B |
A |
| 3. Kemira No. 2 |
190 |
14 |
C |
C |
B |
| 4. Kemira No.5* |
247 |
- |
- |
- |
- |
| 5. Kemira No. 15 |
342 |
5 |
A,B |
A,B |
A |
| 6. Fly ash (low) |
345 |
25 |
A,B |
A,B |
A |
| 7. Fly ash (high) |
360 |
12 |
A |
A |
A |
| 8. Adsorb Plus |
150 |
4 |
D |
D |
B |
| 9. Control |
314 |
16 |
B |
B |
A |
* The treatment with Kemira No. 5 was not
replicated.
x = Mean value, s = Standard deviation |
In appendix 9.1 the results from the Kjeldahl analyses are presented.
In the correlation analysis, no good correlations were found between the
emission values and total-N, ammonium-N, ammonium-N / total-N, total
solids and pH-values (Table 5). The ammonia emission values could thus not
be explained by the results from the Kjeldahl analyses.
| |
Ammonia emission |
| Total-N |
0.14 |
| Ammonium-N |
-0.04 |
| Ammonium-N / total-N |
-0.15 |
| Ammonia emission |
1.00 |
| Total solids |
-0.21 |
| pH |
0.10 |
Table 5.
The correlation coefficients (r2) between the ammonia emissions and
total-N, ammonium-N, ammonium-N / total-N, total solids and pH.
4.3 The second measuring occasion
In Table 6 the climate variations during the two days of the second
measuring occasion (one week after the application of the additives) are
presented. As can be seen in the table, the variations during each day as
well as during the two days together were relatively small. The variations
were considered so small that they would not influence the ammonia
emission levels. The climate conditions and the ammonia emissions at each
measurement are presented in Table 7.
Table 6.
The climate variations during the two days of measuring on the second
occasion.
| |
Slurry temperature [°C] |
Inlet air temperature [°C] |
Relative humidity in the inlet air [%] |
| Day |
x |
s |
x |
s |
x |
s |
| 1 |
9.63 |
0.39 |
7.69 |
0.24 |
61.1 |
1.0 |
| 2 |
9.10 |
0.34 |
7.12 |
0.30 |
65.9 |
1.3 |
| 1+2 |
9.37 |
0.37 |
7.41 |
0.27 |
63.4 |
1.2 |
|
x = Mean value, s = Standard deviation |
Table 7.
The ammonia emissions from the slurry samples and the climate conditions
during each measuring period on the second measuring occasion.
Treatment
No. |
Additive |
Ammonia
emission
[mg/m2 h] |
Slurry
temperature [°C] |
Inlet
air temperature [°C] |
Relative humidity in the inlet air [%] |
| |
|
|
x |
S |
x |
S |
x |
S |
| 1 |
Add A |
236 |
9.27 |
0.07 |
7.60 |
0.10 |
61.3 |
0.5 |
| 1 |
Add A |
247 |
9.53 |
0.22 |
7.58 |
0.06 |
59.3 |
0.5 |
| 1 |
Add A |
239 |
9.33 |
0.23 |
7.75 |
0.32 |
62.5 |
0.5 |
| 2 |
Penac G |
254 |
9.26 |
0.06 |
7.75 |
0.17 |
59.7 |
0.5 |
| 2 |
Penac G |
227 |
8.76 |
0.07 |
7.07 |
0.15 |
65.0 |
0 |
| 2 |
Penac G |
227 |
8.95 |
0.03 |
7.35 |
0.12 |
67.5 |
0.5 |
| 3 |
Kemira No. 2 |
166 |
9.16 |
0.16 |
7.72 |
0.19 |
61.0 |
0 |
| 3 |
Kemira No. 2 |
166 |
9.39 |
0.17 |
7.74 |
0.22 |
60.0 |
0 |
| 3 |
Kemira No. 2 |
154 |
8.88 |
0.04 |
7.20 |
0.21 |
66.4 |
0.5 |
| 4 |
Kemira No. 5 |
204 |
9.26 |
0.05 |
7.78 |
0.33 |
62.0 |
0 |
| 5 |
Kemira No. 15 |
243 |
9.31 |
0.29 |
7.72 |
0.37 |
62.0 |
0 |
| 5 |
Kemira No. 15 |
235 |
8.68 |
0.04 |
7.03 |
0.23 |
65.0 |
0 |
| 5 |
Kemira No. 15 |
239 |
9.13 |
0.10 |
7.67 |
0.22 |
61.0 |
0 |
| 6 |
Fly ash (Low) |
239 |
8.74 |
0.14 |
7.10 |
0.22 |
65.3 |
0.5 |
| 6 |
Fly ash (Low) |
243 |
9.42 |
0.12 |
7.76 |
0.30 |
62.0 |
0 |
| 6 |
Fly ash (Low) |
231 |
8.67 |
0.10 |
7.00 |
0.24 |
64.8 |
0.4 |
| 7 |
Fly ash (High) |
243 |
8.90 |
0.02 |
7.40 |
0.21 |
67.0 |
0 |
| 7 |
Fly ash (High) |
262 |
9.28 |
0.14 |
7.64 |
0.08 |
62.0 |
0 |
| 7 |
Fly ash (High) |
270 |
9.26 |
0.12 |
7.74 |
0.29 |
60.8 |
0.4 |
| 8 |
Adsorb Plus |
100 |
8.60 |
0.02 |
7.00 |
0.19 |
65.0 |
0 |
| 8 |
Adsorb Plus |
108 |
8.80 |
0.01 |
6.69 |
0.04 |
64.0 |
0 |
| 8 |
Adsorb Plus |
112 |
9.22 |
0.04 |
7.68 |
0.20 |
62.0 |
0 |
| 9 |
Control |
223 |
8.91 |
0.02 |
7.30 |
0.01 |
67.5 |
0.5 |
| 9 |
Control |
227 |
8.90 |
0.01 |
7.27 |
0.22 |
67.0 |
0 |
| 9 |
Control |
227 |
8.98 |
0.04 |
7.38 |
0.17 |
67.8 |
0.4 |
|
x = Mean value, s = Standard deviation |
Table 8 shows the results from the statistical evaluation of the manure
additives. Means of the emission values of each treatment with the same
grouping letter are not significantly different. The treatment with Kemira
No. 2 still showed good effect and resulted in significantly lower ammonia
emission than from the control (p<0.001). The treatment with Adsorb Plus
resulted in significantly lower emission than from the Kemira No. 2
treatment (p<0.001). Treatments with these two additives resulted in
approximately 40 % and 60 % lower emission than from the untreated slurry,
respectively. At p<0.05 and p<0.01, no significant differences were found
between the control and the other treatments except with fly ash (high),
which resulted in higher emissions than from the control. The treatment with
Kemira No. 5 may also have had an effect. Table 8.
Means of the ammonia emission values of each treatment on the second
measuring occasion. Means with the same grouping letter are not
significantly different (p<0.05, p<0.01 and p<0.001).
|
Treatment |
Ammonia
emission
[mg/m2 h] |
Grouping
letters at each significance level |
|
|
x |
s |
p<0.05 |
p<0.01 |
p<0.001 |
|
1. Add A |
241 |
6 |
A,B |
A,B |
A |
|
2. Penac G |
236 |
22 |
A,B |
A,B |
A |
|
3. Kemira No. 2 |
162 |
7 |
C |
C |
B |
|
4. Kemira No. 5* |
204 |
- |
- |
- |
- |
|
5. Kemira No. 15 |
239 |
4 |
A,B |
A,B |
A |
|
6. Fly ash (low) |
238 |
6 |
A,B |
A,B |
A |
|
7. Fly ash (high) |
258 |
14 |
A |
A |
A |
|
8. Adsorb Plus |
107 |
9 |
D |
D |
C |
|
9. Control |
226 |
2 |
B |
B |
A |
|
* The treatment with Kemira No. 5 was not
replicated.
x = Mean value, s = Standard deviation |
In appendix 9.2 the results from the Kjeldahl analyses are presented. In
the correlation analysis, no good correlations were found between the
emission values and total-N, ammonium-N, ammonium-N / total-N, total solids
and pH-values (Table 9). The ammonia emission values could thus not be
explained by the results from the Kjeldahl analyses.
| |
Ammonia
emission |
|
Total-N |
-0.04 |
|
Ammonium-N |
0.02 |
|
Ammonium-N / total-N |
0.05 |
|
Ammonia emission |
1.00 |
|
Total solids |
-0.12 |
|
pH |
0.36 |
Table 9.
The correlation coefficients (r2) between the ammonia emissions and total-N,
ammonium-N, ammonium-N / total-N, total solids and pH.
4.4 The third measuring occasion
In Table 10 the climate variations during the two days of the third
measuring occasion (six weeks after the application of the additives) are
presented. The variations during the first day of measurement were the
highest, but they were considered so small that they would not influence the
ammonia emission levels. The climate conditions and the ammonia emissions at
each measurement on the third measuring occasion are presented in Table 11.
Table 10.
The climate variations during the two days of measuring on the third
occasion.
| |
Slurry temperature [°C] |
Inlet air temperature [°C] |
Relative humidity in the
inlet air [%] |
| Day |
x |
s |
x |
s |
x |
s |
| 1 |
9.97 |
0.72 |
7.51 |
1.15 |
62.3 |
6.4 |
| 2 |
7.69 |
0.49 |
6.02 |
0.44 |
58.0 |
3.1 |
| 1+2 |
8.73 |
0.61 |
6.70 |
0.84 |
60.0 |
4.9 |
| x = Mean value, s = Standard deviation |
Table 12 shows the results from the statistical evaluation of the manure
additives. At p<0.05 Adsorb Plus was still effective six weeks after
application of the additive (approximately 30 % lower emission than from the
control). At this significance level the treatment with Add A resulted in a
higher emission than from the untreated slurries. All the other slurries
treated with the different additives emitted ammonia at the same rate as the
control.
Table 11.
The ammonia emissions from the slurry samples and the climate conditions
during each measuring period on the third measuring occasion.
Treatment
No. |
Additive |
Ammonia
emission
[mg/m2 h] |
Slurry temperature [°C] |
Inlet air temperature [°C] |
Relative humidity
in the inlet
air [%] |
| |
|
|
x |
S |
x |
S |
x |
S |
| 1 |
Add A |
231 |
9.71 |
0.37 |
7.41 |
0.46 |
67.8 |
0.6 |
| 1 |
Add A |
247 |
11.25 |
0.60 |
10.22 |
0.72 |
45.5 |
2.3 |
| 1 |
Add A |
200 |
11.62 |
0.55 |
7.50 |
0.65 |
64.0 |
0 |
| 2 |
Penac G |
200 |
9.85 |
0.71 |
8.31 |
0.72 |
53.2 |
2.1 |
| 2 |
Penac G |
181 |
7.38 |
0.24 |
5.96 |
0.10 |
55.7 |
0.5 |
| 2 |
Penac G |
189 |
7.78 |
0.19 |
6.65 |
0.30 |
60.8 |
0.4 |
| 3 |
Kemira No. 2 |
193 |
9.36 |
0.37 |
7.60 |
0.63 |
65.2 |
0.9 |
| 3 |
Kemira No. 2 |
177 |
9.68 |
0.56 |
7.61 |
0.35 |
61.1 |
2.1 |
| 3 |
Kemira No. 2 |
158 |
6.99 |
0.30 |
5.73 |
0.34 |
57.6 |
0.5 |
| 4 |
Kemira No. 5 |
177 |
9.37 |
0.48 |
6.73 |
0.53 |
64.9 |
1.0 |
| 5 |
Kemira No. 15 |
200 |
11.67 |
11.05 |
6.20 |
0.52 |
65.0 |
0 |
| 5 |
Kemira No. 15 |
189 |
7.07 |
0.23 |
5.92 |
0.18 |
55.0 |
0 |
| 5 |
Kemira No. 15 |
223 |
9.66 |
0.30 |
7.82 |
0.51 |
65.6 |
0.8 |
| 6 |
Fly ash (Low) |
196 |
7.12 |
0.33 |
6.22 |
0.33 |
56.6 |
0.5 |
| 6 |
Fly ash (Low) |
208 |
9.35 |
0.35 |
6.24 |
0.69 |
63.4 |
0.5 |
| 6 |
Fly ash (Low) |
177 |
7.20 |
0.38 |
5.75 |
0.28 |
54.5 |
0.5 |
| 7 |
Fly ash (High) |
181 |
7.03 |
0.20 |
5.61 |
0.38 |
59.7 |
1.3 |
| 7 |
Fly ash (High) |
216 |
11.66 |
12.30 |
5.96 |
0.57 |
63.0 |
0 |
| 7 |
Fly ash (High) |
216 |
9.66 |
0.40 |
7.60 |
0.47 |
64.0 |
1.2 |
| 8 |
Adsorb Plus |
119 |
7.21 |
0.10 |
5.84 |
0.21 |
55.0 |
0 |
| 8 |
Adsorb Plus |
123 |
7.66 |
0.08 |
5.70 |
0.03 |
54.0 |
0 |
| 8 |
Adsorb Plus |
131 |
9.66 |
0.30 |
7.14 |
0.73 |
68.7 |
0.6 |
| 9 |
Control |
169 |
7.55 |
0.15 |
6.52 |
0.32 |
61.3 |
0.5 |
| 9 |
Control |
181 |
7.15 |
0.14 |
5.87 |
0.44 |
62.4 |
0.9 |
| 9 |
Control |
185 |
7.42 |
0.15 |
6.24 |
0.33 |
62.0 |
0 |
| x = Mean value, s = Standard deviation |
Table 12.
Means of the ammonia emission values of each treatment on the third
measuring occasion. Means with the same grouping letter are not
significantly different (p<0.05, p<0.01 and p<0.001).
| Treatment |
Ammonia emission [mg/m2
h] |
Grouping letters |
| |
x |
s |
p<0.05 |
p<0.01 |
p<0.001 |
| 1. Add A |
226 |
24 |
A |
A |
A |
| 2. Penac G |
190 |
10 |
A,B |
A |
A,B |
| 3. Kemira No. 2 |
176 |
18 |
B |
A,B |
A,B |
| 4. Kemira No. 5* |
277 |
|
|
|
|
| 5. Kemira No. 15 |
204 |
17 |
A,B |
A |
A |
| 6. Fly ash (low) |
194 |
16 |
A,B |
A |
A,B |
| 7. Fly ash (high) |
204 |
20 |
A,B |
A |
A |
| 8. Adsorb Plus |
124 |
6 |
C |
B |
B |
| 9. Control |
178 |
8 |
B |
A,B |
A,B |
* The treatment with Kemira No. 5 was not
replicated.
x = Mean value, s = Standard deviation |
In appendix 9.3 the results from the Kjeldahl analyses are presented. In
the correlation analysis, no good correlations were found between the
emission values and total-N, ammonium-N, ammonium-N / total-N, total solids
and pH-values (Table 13). The ammonia emission values could thus not be
explained by the results from the Kjeldahl analyses.
| |
Ammonia emission |
| Total-N |
-0.29 |
| Ammonium-N |
0.01 |
| Ammonium-N / total-N |
0.28 |
| Ammonia emission |
1.00 |
| Total solids |
-0.20 |
| pH |
0.10 |
Table 13.
The correlation coefficients (r2) between the ammonia emissions and total-N,
ammonium-N, ammonium-N / total-N, total solids and pH.
4.5 Crust formation in the slurries
During the six weeks of experiment the slurries in the buckets were mixed
thoroughly once every week. On each mixing occasion the crust formation in
the slurries was examined visually. Crust had formed on all the slurries
during all of the six weeks. The crusts in the slurries grew at
approximately the same rate and the thicknesses of the crusts were the same
in all the slurries, except in the one treated with Kemira No. 5 which was
twice as thick.
4.6 Economic evaluation
A rough economic evaluation of the two best performing additives in this
study (Kemira No. 2 and Adsorb Plus) was made. The following conditions were
used:
- The dosages of the additives were those used in the laboratory experiments;
135.0 x 10-3 kg Kemira No. 2 / 5 kg slurry and 25.0 x 10-3 kg Adsorb Plus /
5 kg slurry.
- The nitrogen content of the cow slurry was 0.35 %.
- The ammonium-N release in per cent of the total-N in cow slurry in livestock
buildings was 6 % and from cow slurry storages 8 % (Jordbruksverket, 1991).
- The ammonia emissions used were the mean emission values recorded in the
laboratory test on the first and second measuring occasion: Kemira No. 2;
185 mg/m2 h and 162 mg/m2 h; Adsorb Plus 150 mg/m2 h and 107 mg/m2 h;
control 314 mg/m2 h and 226 mg/m2 h.
- The prices of the products were 2.50 SEK/kg for Kemira No 2 and 5.80 SEK/kg
for Adsorb Plus.
- The storage time for the cow slurry was 8 months
In the economic evaluation of the additives, following formulas were used:
(7)
By dividing equation (6) by equation (7) the costs of using the additives
can be calculated:
(8)
where
a = the cost of using the additives [SEK/year]
b = the amount of cow slurry produced [kg/year]
c = the dosage of the additives [kg additive/kg slurry]
d = the prices of the additives [SEK/kg additive]
e = the saved amount of nitrogen [kg N/year]
f = the ammonia emission from untreated slurry on the first measuring
occasion [mg/m2 h]
g = the ammonia emission from slurry treated with the additives on the
first measuring occasion [mg/m2 h]
h = the ammonium-N release in per cent of the total-N in the slurry in
animal buildings [%] i = the nitrogen content in the slurry [%]
j = the costs of using the additives [SEK/kg saved nitrogen]
The costs of using Kemira No. 2 and Adsorb Plus were calculated to 780
SEK/kg saved nitrogen and 260 SEK/kg saved nitrogen, respectively.
A reduction of the ammonia emission from the slurry storages was included
in the calculations, and then the following formula was used:
(9)
where k = the saved amount of nitrogen [kg/year]
l = the time period during which the additives reduce the ammonia
emission; 2 weeks
m = the storage period of the slurry
n = the ammonia emission from untreated slurry on the second measuring
occasion [mg/m2 h]
o = the ammonia emission from slurry treated with the additives on the
second measuring occasion [mg/m2 h]
p = the ammonium-N release in per cent of the total-N in the slurry from
slurry storages [%]
By dividing equation (6) by equation (9) the costs of using the additives
were calculated. The costs of using Kemira No. 2 and Adsorb Plus decreased
slightly to 740 SEK/kg saved nitrogen and 240 SEK/kg saved nitrogen,
respectively.
These calculations were based on laboratory results and assumptions, and
they can only be used as indications of the cost levels of using the
additives. Even though no costs associated with the spreading of the
additives were used in the calculations, it is clear that the use of slurry
additives is a fairly expensive method of reducing the ammonia emission from
livestock buildings.
5 Discussion
Why did the additives Kemira No. 2 and Adsorb Plus reduce the ammonia
emissions from the cow slurries so effectively and why did the other
additives fail to work satisfactory? One answer might be that both the
additives are based upon superphosphate Ca(H2PO4)2, and according to
equations (3), (4) and (5) the concentration of (NH4)2CO3 in the slurry
formed in the urea hydrolysis is reduced due to the precipitation of CaCO3.
The pH-value decreases and the ammonia emission is reduced. This could be
the cause of the ammonia emission reductions, even though no correlations
between the pH-values and the ammonia emissions were detected.
It is more difficult to explain why additions to the slurries of the
substances based upon silicon dioxides, Penac G and fly ash, resulted in the
same or slightly higher emissions, as those from the untreated slurries.
Witter (1994) reached similar results with finely ground rock, and his
explanation is that additions of these substances result in pH-value
increases.
The treatment with the additive Kemira No. 5 was not replicated and thus
hard to evaluate. However, the treatment seemed to decrease the ammonia
emission, which can be explained by the contents of calcium chloride and
superphosphate in the formulation.
The treatment with the additive Kemira No. 15 did not result in a
emission decrease, which is hard to explain due to the contents of salts and
acids in the formulation.
On the first and the third measuring occasions the treatments with Add A
resulted in statistically higher ammonia emissions than from the controls
(p<0.01 and p<0.05, respectively). According to the company that markets Add
A, Biosolv, the population of bacteria requires certain living conditions,
e.g. that the livestock are fed with "the right type of feed". Biosolv also
claims that the time period required for the additive to reduce the ammonia
emission with full effect is a couple of months. Whether the lack of effect
in reducing ammonia emission is due to unsuitable feed, too short a
measuring period, an inability to work under laboratory conditions, or
simply an inability to reduce ammonia emission from cow slurry, is hard to
tell. In this experiment, however, the treatment with Add A resulted in an
increased ammonia emission at the first and the third measuring occasion.
No good correlations were found between the emission values and the
values from the Kjeldahl analyses. Applications of the additives Kemira No.
2 and Adsorb Plus in manure were expected to result in decreases in pH, but
these decreases were not detected in the analyses. Rank (1988) reports that
very small decreases in pH are required to lower the ammonia emission
substantially. One reason could be that the pH may have increased during the
storage (four weeks in a freezer) and the thawing period of the specimens
from the slurry samples prior to the analyses. Another reason might be that
the precision of the pH-measuring was not sufficiently accurate, but this
hypothesis fails when considering that the contents of ammonium-N should
then have been much lower than what was detected.
6 Conclusions
One day after the application of the additives in the slurry samples the
treatment with Kemira No. 2 and Adsorb Plus resulted in lower ammonia
emission than from the control (p<0.001). The emissions from the slurries
treated with these two additives were approximately 40 % and 50 % lower than
from the untreated slurries, respectively. At p<0.01, no significant
differences were found between the treatments with Kemira No. 15, fly ash
(low), Penac G and the control. At this significance level, the treatments
with Add A and fly ash (high) resulted in higher emissions than from the
control. The Kemira No. 5 treatment was not replicated and therefore hard to
evaluate. However, this single treatment indicated that this additive can
reduce the ammonia emission.
One week after the application of the additives the treatment with Kemira
No. 2 resulted in lower emission than from the control (p<0.001). The Adsorb
Plus treatment gave even better effect and the emissions were significantly
lower than from the treatment with Kemira No. 2 (p<0.001). Treatments with
these two additives resulted in approximately 40 % and 60 % lower emission
than from the untreated slurries, respectively. At p<0.05 and p<0.01, no
significant differences were found between the control and the other
treatments except with fly ash (high), which resulted in higher emissions
than from the control. The Kemira No. 5 treatment also seemed to have an
emission-reducing effect.
Six weeks after application of the additives, Adsorb Plus still reduced
the ammonia emission compared with the emission from the untreated slurries
(p<0.05). The approximate reduction was 30 %. At this significance level the
treatment with Add A resulted in a higher emission than from the untreated
slurries. All the other slurries treated with the different additives
emitted ammonia at the same rate as the control.
The probable cause of Kemira No. 2 and Adsorb Plus, both of which based
on superphosphate, reducing the ammonia emission is that the carbonate ions
present in the slurries are precipitated as calcium carbonate. The pH then
decreases, which results in a lower ammonia emission.
In the correlation analyses of the results from all three of the
measuring occasions no good correlations were found between the emission
values and total-N, ammonium-N, ammonium-N / total-N, total solids and
pH-values. Thus, in neither of the cases could the ammonia emission values
be explained by the results from the Kjeldahl analyses.
The climate variations during each day, as well as during the two days
together, of each measuring occasion were relatively small, and were
considered so small that they would not influence the ammonia emission
levels.
Crust had formed on all the slurries throughout the six weeks of the
experiment. The crusts on the slurries grew at approximately the same rate
and the thicknesses of the crusts were the same on all the slurries, except
on the one treated with Kemira No. 5, which were about two times thicker.
The economic evaluation showed that if a reduction in ammonia emission is
only expected in livestock buildings when applying the additives Kemira No.
2 and Adsorb Plus, the cost would be 780 SEK/kg saved nitrogen and 260 SEK/kg
saved nitrogen respectively. If a reduction of the emission from the
storages (two weeks) also can be expected the costs will be reduced to 740
SEK/kg saved nitrogen and 240 SEK/kg saved nitrogen. This economic
evaluation is approximate and should only be used as an indication of the
cost levels of using these two additives.
7 Future Research and Development
Application of manure additives as a means to decrease ammonia emissions
from animal buildings is very interesting due to the generally simple
application techniques required and the low interference in the living
conditions of the animals. More research must be conducted in this field to
develop the technique and to investigate its limits. The research and
development should be aimed in the following directions:
- Most of the tested additives on the market have been evaluated
with different test methods which make the effects of these additives
hard to compare. Also, new additives are being continuously introduced
into the market. Therefore standardized test procedures must be
developed.
- To be able to determine the absolute ammonia emission reducing
effect of the additives tested in this study they have to be tested in
full-scale trials.
- Inexpensive additives have to be developed.
- Additives with long effects have to be developed. The main reason
why manure additives are expensive to use is the limited time they are
effective. The largest ammonia emissions occur during storage and
spreading of the manure.
- The application techniques of the additives must be developed.
When, where and how should the additives be spread?
8 References
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Odor control in swine houses by the use of natural zeolites: First
approach to the problem. Livestock Environment IV, Fourth International
Symposium - University of Warwick, pp. 701-708. St. Joseph. Michigan.
Andersson, M. 1994.
A climate chamber for measuring ammonia emission. XII World Congress on
Agricultural Engineering, Proceedings, Vol.1, pp. 499-506. Milano.
Beyrouty, C. A., Nelson, D. W. & Sommers, L. E. 1988.
Effectiveness of phosphoroamides in retarding hydrolysis of urea
surface-applied to soils with various pH and residue cover. Soil Sci., Vol.
145, pp. 345-352.
Biosolv. 1993.
Personal communication. BioSolv, Enskede. Sweden.
Demmers, T. G. M., Hissink, M. G. & Uenk, G. H. 1992.
Het grogen van pluimveemest in een droogtunnel en het effect hiervan op
de ammoniakemissie. IMAG-DLO, Report 92-6, pp. 22. Wageningen
Denmead, O. T., Freney, J. R. & Simpson, J. R. 1982.
Dynamics of ammonia volatilization during furrow irrigation of maize.
Soil Sci. Soc. Am. J., Vol. 46, pp. 149-155.
Elzing, A., Kroodsma, W., Scholtens, R. & Uenk, G. H. 1992.
Ammonia emission measurements in a model system of a dairy cattle
housing: Theoretical considerations. IMAG-DLO, Report 92-3. Wageningen.
Fenn, L. B. & Kissel, D. E. 1973.
Ammonia volatilization from surface applications of ammonium compounds
on calcareous soils: I. General theory. Soil Sci. Soc. Am. Proc., Vol. 37,
pp. 855-859.
Fenn, L. B., Matocha, J. E. & Wu, E. 1981.
Ammonia Losses from Surface-Applied Urea and Ammonium Fertilizers as
Influenced by Rate of Soluble Calcium. Soil Sci. Soc. Am. J., Vol. 45, pp.
883-886.
Frank, B. 1993.
Personal information. Swedish University of Agricultural Sciences,
Department of Agricultural Biosystems and Technologies. Lund.
Freney, J. R., Denmead, O. T., Watanabe, J. & Crasswell, E. T. 1981.
Ammonia and nitrous oxide losses following applications of ammonium
sulphate to flooded rice. Aust. J. Agric. Res., Vol. 32, pp. 37-45.
Hartung, J. 1992.
Emmision und Kontrolle von Gasen und Geruchsstoffen aus Ställen und
Dunglagern. Zbl. Hyg. 192, pp. 389-418.
Headon, D. R. & Walsh, G. 1993.
Yucca schidigera extracts and ammonia control. Livestock Environment IV,
Fourth International Symposium - University of Warwick, pp. 686-693. St.
Joseph. Michigan.
Hygrisan. 1993.
Personal communication. Hygrisan AB, Malmö. Sweden.
Jordbruksverket. 1991.
Ammoniakförluster från jordbruket - Förslag till åtgärdsprogram.
Jordbruksverket, Rapport 1991:11.
Jordbruksverket. 1994.
Ammoniakförluster från jordbruket - Möjligheter till och konsekvenser av
en minskning av ammoniakutsläppen i södra och västra Götaland med 50 % till
år 2000. Jordbruksverket, rapport 1994:8.
Kapuinen, P. 1992.
Djupströbäddens egenskaper och funktion i köttdjursstall. NJF-Teknik
-92, 212. Espoo.
Kellems, R. O., Miner, J. R. & Church, D. C. 1979.
Effect of ration, waste composition and length of storage on the
volatilization of ammonia hydrogen sulfide and odors from cattle waste. J.
Anim. Sci., Vol. 48, pp. 436-445.
Kemira. 1993.
Personal information. Kemira Kemi AB, Helsingborg. Sweden.
Kemme, P. A., Jongbloed, A. W ., Dellaert, B. M. & Krol-Kramer, F.
1993.
The use of a Yucca shidigera extract as "urease inhibitor" in pig
slurry. Proceedings of the First International Symposium on Nitrogen Flow in
Pig Production and Environmental Consequences, EAAP Publication No. 69, pp.
330-335. Wageningen.
Kirchmann, H. & Witter, E. 1989.
Ammonia volatilization during aerobic and anaerobic manures
decomposition. Plant and Soil, Vol. 115, pp. 35-41.
Krieger, R., Hartung, J. & Pfeiffer, A. 1993.
Experiments with a feed additive to reduce ammonia emissions from pig
fattening houses - preliminary results. Proceedings of the First
International Symposium on Nitrogen Flow in Pig Production and Environmental
Consequences, EAAP Publication No. 69, pp. 295-300. Wageningen.
Luft -90. 1990. Luft -90.
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Miner, J. R. 1974.
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Ser. EPA-660-2-74-023. U. S. Environmental Protection Agency. Washington DC.
Penac. 1993.
Personal communication. Penac, Trelleborg. Sweden.
Pond, W. G. & Yen, J. T. 1980.
Response of growing pigs to dietary zeolite. Proceedings IVPS Congress,
297. Copenhagen.
Rank, M. 1988.
Untersuchungen zur Ammoniakverflüchtigung nach Gülledüngung.
Dissertation. Der Technischen Universität München.
Svensson, L. 1993.
Ammonia volatilization from land-spread livestock manure - Effects of
factors relating to meteorology, soil/manure and application technique.
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Engineering. Dissertation. Uppsala.
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Berechnung der Ammoniak-Emission aus Geflügelhaltungen. In: Ammoniak in
der Umwelt, Proceedings Symposium, Braunschweig, KTBL, Darmstadt, Beitrag
Nr. 39, pp. 10.
Vlek, P. L. G. & Craswell, E. T. 1981.
Ammonia volatilization from flooded soils. Fert. Res., Vol. 2, pp.
227-245.
Witter, E. & Kirchmann, H. 1989.
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volatilization during manure´s decomposition. Plant and Soil, Vol. 115, pp.
53-58.
Witter, E. 1991 a.
Use of additives to reduce ammonia volatilization. Unpublished. Swedish
University of Agricultural Sciences, Department of Soil Science. Uppsala.
Witter, E. 1991 b.
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pp. 369-380.
9 Appendices
9.1 Appendix 1: Results from the Kjeldahl analyses of the slurry
samples on the first measuring occasion.
|
Treatment
No. |
Additive |
Total-N
[%] |
Amm.-N
(%) |
Amm.-N /
Total-N [%] |
Total solids
[%] |
pH |
|
1 |
Add A |
0.31 |
0.16 |
51 |
7.6 |
8.1 |
|
1 |
Add A |
0.31 |
0.13 |
43 |
7.9 |
8.1 |
|
1 |
Add A |
0.35 |
0.16 |
47 |
8.4 |
8.1 |
|
2 |
Penac G |
0.28 |
0.14 |
51 |
8.8 |
8.0 |
|
2 |
Penac G |
0.37 |
0.17 |
45 |
8.4 |
7.9 |
|
2 |
Penac G |
0.32 |
0.17 |
54 |
- |
8.1 |
|
3 |
Kemira No. 2 |
0.34 |
0.16 |
46 |
10.1 |
8.0 |
|
3 |
Kemira No. 2 |
0.34 |
0.16 |
47 |
10.8 |
7.9 |
|
3 |
Kemira No. 2 |
0.29 |
0.16 |
57 |
10.2 |
7.9 |
|
4 |
Kemira No. 5 |
0.35 |
0.10 |
30 |
10.2 |
7.9 |
|
5 |
Kemira No. 15 |
0.34 |
0.17 |
51 |
8.6 |
8.0 |
|
5 |
Kemira No. 15 |
0.34 |
0.16 |
46 |
9.4 |
7.9 |
|
5 |
Kemira No. 15 |
0.37 |
- |
- |
9.0 |
7.7 |
|
6 |
Fly ash (Low) |
0.39 |
0.16 |
43 |
10.8 |
8.1 |
|
6 |
Fly ash (Low) |
0.34 |
0.17 |
49 |
8.7 |
7.9 |
|
6 |
Fly ash (Low) |
0.30 |
0.16 |
52 |
8.2 |
8.1 |
|
7 |
Fly ash (High) |
0.33 |
0.18 |
33 |
8.6 |
7.9 |
|
7 |
Fly ash (High) |
0.36 |
0.17 |
47 |
9.7 |
8.1 |
|
7 |
Fly ash (High) |
0.32 |
0.16 |
50 |
9.5 |
8.0 |
|
8 |
Adsorb Plus |
0.35 |
0.16 |
43 |
9.3 |
8.0 |
|
8 |
Adsorb Plus |
0.31 |
0.16 |
49 |
7.9 |
8.2 |
|
8 |
Adsorb Plus |
0.35 |
0.16 |
52 |
8.9 |
8.1 |
|
9 |
Control |
0.33 |
0.11 |
33 |
8.6 |
7.9 |
|
9 |
Control |
0.35 |
0.15 |
42 |
8.0 |
8.0 |
|
9 |
Control |
0.32 |
0.15 |
46 |
8.8 |
8.1 |
9.2 Appendix 2: Results from the Kjeldahl analyses of the slurry samples
on the second measuring occasion.
Treatment
No. |
Additive |
Total-N
[%] |
Amm.-N
(%) |
Amm.-N /
Total-N [%] |
Total solids
[%] |
pH |
| 1 |
Add A |
0.33 |
0.15 |
46 |
9.0 |
7.9 |
| 1 |
Add A |
0.34 |
0.13 |
40 |
8.6 |
7.9 |
| 1 |
Add A |
0.36 |
0.16 |
43 |
10.7 |
8.0 |
| 2 |
Penac G |
0.36 |
0.21 |
59 |
9.8 |
8.1 |
| 2 |
Penac G |
0.39 |
0.15 |
39 |
13.1 |
8.0 |
| 2 |
Penac G |
0.31 |
0.16 |
51 |
8.7 |
8.0 |
| 3 |
Kemira No. 2 |
0.33 |
0.15 |
45 |
10.9 |
7.9 |
| 3 |
Kemira No. 2 |
0.30 |
0.14 |
46 |
11.6 |
8.0 |
| 3 |
Kemira No. 2 |
0.32 |
0.15 |
47 |
10.4 |
8.1 |
| 4 |
Kemira No. 5 |
- |
- |
- |
- |
- |
| 5 |
Kemira No. 15 |
0.33 |
0.15 |
45 |
8.8 |
8.0 |
| 5 |
Kemira No. 15 |
0.30 |
0.15 |
52 |
9.1 |
8.2 |
| 5 |
Kemira No. 15 |
0.37 |
0.15 |
42 |
9.1 |
8.1 |
| 6 |
Fly ash (Low) |
0.33 |
0.16 |
50 |
8.7 |
8.0 |
| 6 |
Fly ash (Low) |
0.30 |
0.16 |
54 |
9.1 |
8.0 |
| 6 |
Fly ash (Low) |
0.31 |
0.15 |
49 |
9.1 |
8.2 |
| 7 |
Fly ash (High) |
0.27 |
0.16 |
57 |
9.8 |
8.2 |
| 7 |
Fly ash (High) |
0.31 |
0.16 |
50 |
10.0 |
8.0 |
| 7 |
Fly ash (High) |
0.37 |
0.13 |
36 |
13.1 |
7.8 |
| 8 |
Adsorb Plus |
0.36 |
47 |
43 |
9.6 |
7.7 |
| 8 |
Adsorb Plus |
0.39 |
0.15 |
39 |
10.6 |
8.0 |
| 8 |
Adsorb Plus |
0.33 |
0.16 |
49 |
9.3 |
7.7 |
| 9 |
Control |
0.30 |
0.16 |
53 |
8.4 |
8.2 |
| 9 |
Control |
0.32 |
0.15 |
46 |
8.3 |
8.0 |
| 9 |
Control |
0.30 |
0.16 |
51 |
8.5 |
8.1 |
9.3 Appendix 3: Results from the Kjeldahl analyses of the slurry
samples on the third measuring occasion.
Treatment
No. |
Additive |
Total-N
[%] |
Amm.-N
(%) |
Amm.-N /
Total-N [%] |
Total solids
[%] |
pH |
| 1 |
Add A |
0.31 |
0.16 |
50 |
9.2 |
7.9 |
| 1 |
Add A |
0.30 |
0.12 |
39 |
10.1 |
9.0 |
| 1 |
Add A |
0.28 |
0.126 |
43 |
9.9 |
8.7 |
| 2 |
Penac G |
0.33 |
0.13 |
39 |
9.6 |
8.7 |
| 2 |
Penac G |
0.35 |
0.13 |
36 |
12.3 |
9.0 |
| 2 |
Penac G |
0.34 |
0.12 |
34 |
11.9 |
8.8 |
| 3 |
Kemira No. 2 |
0.32 |
0.13 |
41 |
15.9 |
8.5 |
| 3 |
Kemira No. 2 |
0.32 |
0.14 |
42 |
12.1 |
7.5 |
| 3 |
Kemira No. 2 |
0.34 |
0.13 |
38 |
12.9 |
8.7 |
| 4 |
Kemira No. 5 |
0.36 |
0.12 |
35 |
13.4 |
8.6 |
| 5 |
Kemira No. 15 |
0.33 |
0.13 |
38 |
8.9 |
8.7 |
| 5 |
Kemira No. 15 |
0.29 |
0.13 |
44 |
10.1 |
8.9 |
| 5 |
Kemira No. 15 |
0.29 |
0.12 |
43 |
10.1 |
8.0 |
| 6 |
Fly ash (Low) |
0.35 |
0.12 |
35 |
12.4 |
8.8 |
| 6 |
Fly ash (Low) |
0.29 |
0.13 |
44 |
9.4 |
8.5 |
| 6 |
Fly ash (Low) |
0.32 |
0.11 |
36 |
11.3 |
8.8 |
| 7 |
Fly ash (High) |
0.37 |
0.12 |
32 |
14.1 |
8.9 |
| 7 |
Fly ash (High) |
0.34 |
0.13 |
39 |
13.7 |
8.8 |
| 7 |
Fly ash (High) |
0.32 |
0.15 |
46 |
11.5 |
8.7 |
| 8 |
Adsorb Plus |
0.35 |
0.14 |
39 |
10.0 |
8.7 |
| 8 |
Adsorb Plus |
0.32 |
0.14 |
43 |
11.0 |
8.7 |
| 8 |
Adsorb Plus |
0.33 |
0.13 |
40 |
10.3 |
7.6 |
| 9 |
Control |
0.37 |
0.12 |
33 |
13.1 |
8.8 |
| 9 |
Control |
0.29 |
0.11 |
38 |
9.7 |
8.8 |
| 9 |
Control |
0.30 |
0.12 |
40 |
9.2 |
8.8 |
Ammonia emissions contribute substantially to environmental pollution and
cause severe acidification. In Sweden, 20-25 % of the total ammonia emission
derives from manure in animal buildings. One technique to decrease ammonia
emissions from animal buildings is to apply emission-reducing additives in
the manure. However, the efficiencies of many of the manure additives on the
market have not been determined, and those additives that have been
evaluated are difficult to compare due to different test methods and methods
of evaluation.
The objectives of this study were to investigate the abilities of
different manure additives in reducing ammonia emission, for how long they
would be efficient, and to which cost the additives can be used.
The results show that high reductions (up to 50 %) in ammonia emissions
are possible to obtain with some of the additives, at least during the first
week after the application of the additives. The reductions decrease over
time, and they are hardly noticeable after six weeks. The costs to which
these additives can be used are high in relation to the amount of nitrogen
they save.
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