FI127616B - Compositions for treating nitrogen containing organic wastes - Google Patents

Compositions for treating nitrogen containing organic wastes Download PDF

Info

Publication number
FI127616B
FI127616B FI20165130A FI20165130A FI127616B FI 127616 B FI127616 B FI 127616B FI 20165130 A FI20165130 A FI 20165130A FI 20165130 A FI20165130 A FI 20165130A FI 127616 B FI127616 B FI 127616B
Authority
FI
Finland
Prior art keywords
composition
manure
weight
acid
ammonia
Prior art date
Application number
FI20165130A
Other languages
Finnish (fi)
Swedish (sv)
Other versions
FI20165130A (en
Inventor
Pekka Pohjola
Original Assignee
Algol Chemicals Oy
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Algol Chemicals Oy filed Critical Algol Chemicals Oy
Priority to FI20165130A priority Critical patent/FI127616B/en
Priority to EP17707938.1A priority patent/EP3416931A1/en
Priority to PCT/FI2017/050090 priority patent/WO2017140947A1/en
Publication of FI20165130A publication Critical patent/FI20165130A/en
Application granted granted Critical
Publication of FI127616B publication Critical patent/FI127616B/en

Links

Classifications

    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N37/00Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom having three bonds to hetero atoms with at the most two bonds to halogen, e.g. carboxylic acids
    • A01N37/36Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom having three bonds to hetero atoms with at the most two bonds to halogen, e.g. carboxylic acids containing at least one carboxylic group or a thio analogue, or a derivative thereof, and a singly bound oxygen or sulfur atom attached to the same carbon skeleton, this oxygen or sulfur atom not being a member of a carboxylic group or of a thio analogue, or of a derivative thereof, e.g. hydroxy-carboxylic acids
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01CPLANTING; SOWING; FERTILISING
    • A01C3/00Treating manure; Manuring
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/16Alumino-silicates
    • B01J20/165Natural alumino-silicates, e.g. zeolites
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/02Biological treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/14Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
    • C02F11/148Combined use of inorganic and organic substances, being added in the same treatment step
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/20Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation using specific microorganisms or substances, e.g. enzymes, for activating or stimulating the treatment
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F3/00Fertilisers from human or animal excrements, e.g. manure
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/09Carboxylic acids; Metal salts thereof; Anhydrides thereof
    • C08K5/092Polycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/16Treatment of sludge; Devices therefor by de-watering, drying or thickening using drying or composting beds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/145Feedstock the feedstock being materials of biological origin
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Soil Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Environmental Sciences (AREA)
  • Molecular Biology (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Dentistry (AREA)
  • Biochemistry (AREA)
  • Microbiology (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Biotechnology (AREA)
  • Plant Pathology (AREA)
  • Pest Control & Pesticides (AREA)
  • Agronomy & Crop Science (AREA)
  • Analytical Chemistry (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Abstract

A composition for treatment and composting of nitrogen containing organic wastes, in particular manure, comprising (a) sodium bentonite; (b) organic polyprotic acid(s); (c) iron(II)sulfate; and (d) alkaline mineral(s).

Description

The present invention relates to composting of organic material, and more particularly to a composition preventing malodour emissions from nitrogen containing organic wastes such as manure.
BACKGROUND OF THE INVENTION io Cattle manure is a natural and very valuable fertilizer in agriculture containing all main nutrients as nitrogen, phosphorus and potassium. Manure has, however, some inconvenient qualities which make its use often nearly impossible between modern communities. These are: bad smell, ammonia emissions, pollution, and colloidal structure.
As you drive through the countryside after the liquid manure has been spread, a disgusting smell seems to penetrate even the most tightly closed car windows. The smell of ammonia in liquid manure is largely responsible for the smell, but manure also includes sulfides and other compounds such as p-cresol and other gases belonging to volatile fatty acid groups.
Gas emissions are one of the greatest challenges facing the poultry industry in the future. Ammonia emission levels per house occasionally exceed the safety limits and ventilation often is the only way to keep the level sufficiently low. Ventilation on cold climate areas, however, because of thermal control is expensive and takes much energy. Gas filtration and purification are too often necessary.
Many gaseous waste emissions from livestock worsen the greenhouse effect. Manure is a byproduct of livestock and it is also a source of many valuable nutrients including nitrogen and phosphorus. These nutrients can become a source of pollution, resulting in water contamination and unwanted air emissions. Agriculture accounts for more than 85% of total ammonia emissions. This comes mainly from livestock urine and manures and also from nitrogen fertilizers. EU is under interna2
20165130 prh 23 -08- 2018 tional legislation to reduce ammonia emissions from agriculture and new innovations will be required to meet future targets. Ammonia gas emissions from manures, sewage sludge and other nitrogen rich wastes increase greatly because of the high pH-value. The emission of nitrogen as ammonia starts at pH 8 and in5 creases exponentially to pH 10. The equilibrium between soluble ammonium and gaseous ammonia: NH4+ = NH 3 + H+ is at pH 9. Microbes that produce ammonium ions from organic nitrogen compounds increase the pH value and the escape of nitrogen as gas is evident. As ammonia escapes more ammonium ions are transformed into ammonia because of equilibrium.
io The need to decrease and prevent harmful emissions from manures is very topical problem and numerous studies have been made all over the world to solve these complicated problems. Ammonia is a large component of the gaseous emissions from manures. Ammonia is generated by bacteria in enzymatic conversation of uric acid via the action of uricase, urease, and other enzymes. Some studies have been concentrated to deactivate the enzyme to reduce the production of ammonia. Introducing an acidogenic material as for instance gypsum, calcium chloride, calcium phosphate, and ammonium benzoate to force protonation of ammonia has resulted in somewhat reduced ammonia emissions in hen manure. A number of managing methods to reduce ammonia emissions have been identified and focus20 es on the areas: Housing, storage and manure application to fields. Methods usually are technical practices for instance no turnover and covering. Windrow composting is used for sewage sludge which in many qualities resembles manures and it also produces great ammonia emissions and smelly gases. Some studies to prevent emissions has been made for instance with covering peat layer. Liquid manures typically have a colloidal structure and this kind of jelly has many unfavorable properties as concerns for instance manure managing. The manure channels easily are blogged, the spreading and soaking into ground are difficult. Additionally, manure spread easily makes a dry cover on fields that may produce a hygienic risk in the feed stuff. If the colloidal structure could be dispersed, it would have many advantageous influences for manure transfer, spreading and use as a fertilizer.
Phosphorus is nutrient that contributes problems for environment because it often
20165130 prh 23 -08- 2018 is limiting nutrient for algae growth in ecosystem. Phosphorus transfers with sediment from fields are advantageous to be demobilized on soil surfaces.
In nitrogen containing organic waste like manure begins a biodegradation process that changes the physical and chemical composition of the matter. Microbes work organic material and develop different produces of which quality greatly depends on the circumstances: Air, pH, humidity, temperature and microorganisms. It has been proved that many minerals also, control the biodegradation process. In unfriendly circumstances the biodegradation often produces more harmful emissions. In anaerobic state there comes bad smelling sulfides and methane. In high pH io state and high temperatures the emission of ammonia is very strong. On the other hand, the well managed aerobic composting of organic wastes, such as municipal slurry, manures and lavatory waste, produce better fertilizer than originals for crop husbandry and for soil improvement. Raw horse manure even is inconvenient matter for cultivated plants without composting because soil microbes take nutrients 15 before plants. Because of high pH, usually the emission of nitrogen during biodegradation is great and the value of manure as nitrogen nutrient is decreased.
Although phosphorus partly can be in insoluble form, orders regarding phosphorus fertilizers mean only total phosphorus. Phosphorus is a necessary nutrient for plants and it is preferable that as much phosphorus as possible is in soluble form.
This is a remarkable problem with municipal sludge, were phosphorus is bound with iron.
In manures the phosphorus contents usually are so great that it limits the amount of manure that is allowed to spread into field. Iron combined with clay minerals, may prevent the phosphorus flow. Phosphates can be bound on the negative charged surfaces of clay/metal systems. Iron II has a disposition to oxidize to iron III and this redox- phenomenon has great influence into nitrogen and phosphorus in manures. Simultaneously iron II reduces ammonia from gas to ammonium ion also.
WO2008125739A1 discloses an aerobic biodegradation accelerant.
As we can see, nitrogen and phosphorus rich wastes, such as manures, are usually problematic materials in advanced world. All methods and innovations which help the manure managing, emission and pollution problems and improve the us4
20165130 prh 23 -08- 2018 ability and value of manures as fertilizers are desirable.
BRIEF DESCRIPTION OF THE INVENTION
It is thus an object of the present invention to provide a composition for treating, e.g. composting nitrogen containing organic wastes, in particular manure.
The objects of the invention are achieved by a composition and uses thereof, which are characterized by what is stated in the independent claims. The preferred embodiments of the invention are disclosed in the dependent claims.
The invention is based on the realization by adjusting and/or buffering the pH value in specific combination with particular components such as certain mineral ma10 terial(s) and redox agents, the nitrogen emissions of nitrogen containing organic wastes as ammonia may be prevented. Also other malodors are de- creased and composting may be carried out without smells and nitrogen escape.
BRIEF DESCRIPTION OF THE DRAWINGS
In the following the invention will be described in greater detail by means of pre15 ferred embodiments with reference to the attached [accompanying] drawings, in which
Figure 1a shows dry composition in a measuring glass;
Figure 1b shows watered composition in a measuring glass;
Figure 2 shows temperature curves of horse manure composts;
Figure 3 shows mixture controls the pH-conditions and reducing of the ammonia emission in horse manure composts; and
Figure 4 shows how the present composition reduces the amount of water soluble phosphorus in horse manure composts.
DETAILED DESCRIPTION OF THE INVENTION
Provided herein is a composition for treatment of nitrogen containing organic wastes, in particular manure, comprising (a) sodium bentonite;
(b) organic polyprotic acid(s);
20165130 prh 23 -08- 2018 (c) iron(ll)sulfate; and (d) alkaline mineral(s).
A key element of the present composition is (a) sodium bentonite. Sodium bentonite has a great ability to adsorb water and performs as an adsorbent in the present composition. Acting together with the (b) organic polyprotic acid(s) comprised in the present composition the presence of sodium bentonite reduces smells. Further the sodium bentonite releases sodium ions into extracellular liquid resulting from the treated nitrogen containing organic wastes having a positive influence for the biodegradation process.
io The amount of sodium bentonite (a) in the present composition is typically from 45 to 80% by weight, preferably from 50 to 70% by weight, more preferably from 55 to 65% by weight, of the total weight of the composition.
As indicated above the present composition further comprises (b) organic polyprotic acid(s). The organic polyprotic acid(s) lower the pH of the nitrogen containing waste material and may act as buffers when the present composition is added to the treated nitrogen containing organic material. The buffer system is formed in situ when the present composition is added to the treated material. The buffer system consists of the organic polyprotic acid and its respective salt formed by a reaction between the acid and an alkaline mineral (d) comprised in the present compo20 sition.
Typically the organic polyprotic acid(s) (b) are selected from a group consisting of C2-10-dicarboxylic acids and C2-10-tricarboxylic acids. Preferably, the organic polyprotic acid(s) are selected from a group consisting of citric acid, tartaric acid and any mixtures thereof. The total amount of organic polyprotic acid(s) (b) in the present composition is typically up to 20% by weight, preferably from 2 to 15% by weight, more preferably from 5 to 10% by weight, of the total weight of the composition. More preferably the amount of citric acid in the present composition is from 3 to 8% by weight of the total weight of the composition and the amount of tartaric acid in the present composition is from 1 to 6% by weight of the total weight of the composition.
The present composition also comprises (c) iron(ll)sulfate (ferrous sulfate,
20165130 prh 23 -08- 2018
FeSCM). FeSCM forms chelates with organic acids and oxidizes with water to Fe(lll), thus advantageously decreasing its solubility into water. Ferrous and ferric ions have an important role as electrolytes in many redox processes resulting in the desired effect of reducing ammonia emissions. Iron participates for instance actively in the redox phenomenon of the biodegradation process and promotes microbial cell respiration and humus catalysis. Iron can reduce ammonia to ammonium and thus reduces smell associated with ammonia. Iron(ll)sulfate combined with other constituents of the present composition decomposes colloidal structure of liquid manures and produces bigger particles which separate in liquid, io This improves managing and the structure of the nitrogen containing organic waste, in particular manure. Advantageously iron also prevents corrosion of the used equipment by satisfying the need of minerals for microorganisms. Additionally iron(ll)sulfate may decrease the solubility of phosphorus and thus de- crease its mobilization into natural waters.
The amount of iron(ll)sulfate (c) in the present composition is typically from 0.5 to 10% by weight, preferably from 5 to 8% by weight, of the total weight of the composition.
The present composition further comprises (d) alkaline mineral(s) for controlling the pH level of the treated nitrogen containing organic waste by allowing in situ formation of a pH buffer system together with the organic polyprotic acid(s) (b) as explained above, and for further enhancing the biodegradation of the nitrogen containing organic waste.
A particular example of suitable alkaline mineral (d) is silicate limestone. Silicate limestone is a bi product in lime industry and is typically used as a soil improve25 ment to increase pH of fields. As a weakly alkaline rock it is suitable combination with the organic polyprotic acid(s) as buffer. Additionally, silicate mineral surfaces may function as surface catalysts. Silicate surfaces can participate in electron exchange and offer active operation environments and substrates for microbes. Silicates work as biogeochemical particles, bind carbon dioxide and other emissions and form new stabile humus compounds. As a mixture with sodium bentonite (a) and organic polyprotic acid(s) (b) it starts when added to nitrogen containing organic waste sludge, such as manure, a reaction which produces carbon dioxide
20165130 prh 23 -08- 2018 decreasing pH under the limit where ammonia can be emitted and the smell of the waste fades within in some minutes.
The amount of alkaline mineral(s) (d) in the present composition is typically from 5 to 35% by weight, preferably from 10 to 30% by weight, more preferably from 15 to
25% by weight, of the total weight of the composition.
The present composition may further comprise (e) mineral carrier(s). The mineral carrier(s) may function as a base and carrier of the composition mixture and may have further buffering, surface catalyst, ion exchange and/or molecular sieve effects. Preferably the mineral carries (e) is talc.
io When present in the composition the amount of mineral carrier(s) (e) in the present composition is typically from up to 20% by weight, preferably up to 15% by weight, more preferably from 5 to 10% by weight, of the total weight of the composition.
The present composition may be used for treating nitrogen containing organic wastes, such as manure. In particular the present composition is suitable for composting nitrogen containing organic wastes, such as manure. The present composition may be further used for preventing and/or decreasing ammonia emissions from nitrogen containing organic wastes, such as manure. It may also be used for preventing and/or decreasing malodor emissions from nitrogen containing organic wastes, such as manure. Furthermore, the present composition may be used for dispersing colloidal sludge in nitrogen containing organic wastes, such as manure.
The present composition may be provided by mixing the components of the composition. The composition is typically in powder or granular form.
EXAMPLES
Composition 1
60% sodium bentonite
20% silicate limestone
5% talc
8% ferrous sulfate
5% citric acid
2% tartaric acid by weight of the total weight of the composition.
Example 1.
Composition 1 when brought into contact with water began to swell and produce carbon dioxide bubbles. Figure 1a shows 10 ml of dry Composition 1 in a measuring glass. 1b. Figure 1b illustrate how the watered system fills whole measuring glass by bubbles when bentonite swells. This property renders ability to immediately remove smells from malodor objects when spread on their surface. This has io been tested with numerous cases by sense perceptions.
Example 2.
Manure and urine mixtures usually have high pH-value, which is the principal reason for ammonia emissions and composting problems. The present composition has a positive influence to pH-value. The Composition 1 has pH 4.9 and efficient buffer ability. When watered, bubbling and separation of carbon dioxide starts resulting also into pH effects. Table 1 represents pH of four most usual manures in 10% liquid states. The liquid manures are alkaline and pH usually increases quickly by microbes. When 1% of Composition 1 was added, pH decreased clearly. It is interesting that in three cases pH stabilized near 6 caused by the buffer capacity of mixture.
Table 1.
20165130 prh 23 -08- 2018
Manure pH in liquid pH in liquid treated with Composition 1
Pig manure 7.2 6.1
Bovine manure 8.6 6.2
Horse manure 7.6 5.6
Chicken manure 7.2 6.3
In liquid manures malodor is very strong. When Composition 1 in powder form was added, strong bubbling started, bad smells of all manures decreased soon and the color of the liquids darkened. The structure of the colloidal slurry was dispersed
20165130 prh 23 -08- 2018 and small dark flakes were separated. This is due to the electrochemical influences of the mixture. This effect improves the spreading and use as fertilizer of liquid manures. Absorption of fertilizers into land is better and there forms no typical skincover of manure. This is an important hygienic factor in the use of liquid manures.
Example 3.
For a reference ammonia measurement small wood chips were added into a bottle equipped with 50 ml syringe and side hose pipe that was placed into violet 4% boric acid solution with indicator. The wood chips were watered by 20 ml of water, io Then 3 x 5 ml of 6 M ammonia solution (1260 mg N) was added. During 30 minutes the ammonia vapors were pumped into acid solution changing the color to yellow. The temperature of the bottle was increased at the end to 40 Celsius by water bath. The evaporated ammonia was titrated by 0.1 M HCI solution. During this period the amount of 10.5 mg of ammonia (8.7 mg N) had escaped from wood chip bed.
Another experiment was made with the Composition 1. Otherwise the test was performed as above, but 2 g of Composition 1 was added on the wood chip bed. Now the ammonia evaporation result was only 2.1 mg of ammonia (1.7 mg N). The amount of escaped ammonia had decreased dramatically, about 80%.
Example 4.
kg of dry chicken manure, with straw and wood chips as litter, was packed into a Compomate composter and composted three days when temperature increased to 40°C. The smell of ammonia was very strong. The pH of mixture then was sufficiently high, 9.01.
The activated carbon filters in the cover were replaced by corks and a pipe equipped with 300 ml syringe was installed through the cover. The syringe was filled ten times by gas from composter and emptied into boric acid liquid with indicator. The color of liquid was turned already after two pumping times from violet to yellow. Ammonia in composting vapor reacts with boric acid and may be titrated with HCI. The liquid was titrated with a HCI solution as above. During the analysis the amount of ammonia, NH3, in 3 dm^ of composter gas was 2.97 mg (2.45 mg
20165130 prh 23 -08- 2018
N). The measurement was repeated after an hour and the result was exactly same.
Then 50 g of Composition 1 was spread quickly on the surface of manure and the cover was closed. After an hour the compost gas was analyzed as above. Now the amount of ammonia in 3 dm^ was only 0.34 mg (0.28 mg N). The pH in surface layer of manure bed (3 cm) was lowered to 7.17 and the smell of ammonia disappeared. The product was capable to decrease the amount of ammonia over 88 % in air above the manure according to this experiment.
Example 5.
io Horse manure, sawdust as litter, was composted in four 15 dm^ Compomate composters indoors composter equipped with activated carbon filters by two pairs, where into composters HPa1 and HPa2 1% of Composition 1 was added. Composters HPc1 and HPc2 did not contain any additive.
The temperature curves in Figure 2 describe the microbiological activity of com15 posted horse manure. The temperature usually rises quickly in horse manure heaps, which promotes the escape of nitrogen as ammonia, when simultaneously the microbes produce more ammonium and pH increases. High ammonium concentration can work as an inhibitor for biodegradation and temperature drops. This phenomenon can be seen also in these curves after seven days. The stabilization takes time and compost finally may be nitrogen poor product. In Figure 2 we can see that the curves of composts with Composition 1 (HPa1 and HPa2) go all the time above the comparatives. The temperature sums during the measuring period between the comparative examples differ by 10%.
pH-values during the active period are shown in Figure 3. Composition 1 controls the pH-conditions and reduces the ammonia emission in compost, as can be seen from the curves of HPa1 and HPa2 versus the curves of HPc1 and HPc2. Worthy of consideration is that both curves of comparatives HPc1 and HPc2 are in the pH range, where the balance of NH4+/NH3 is on the side of ammonia and the emission of nitrogen is great. Simultaneously the curves with Composition 1 HPa1 and
HPa2 settle on advantageous pH area. It is easy to foresee, that we can get more nitrogen rich fertilizer by the present composition.
Solubility of phosphorus in the horse manure composts is represented in Figure 4.
Manures are phosphorous rich products and they are important sources of this base nutrient for plants. Composting usually decreases the water solubility of phosphorus binding it into humus structures. Microbes can remove phosphorus from many organic and inorganic compounds and work it usable for plants. Roots of the plant then can remove phosphorus from humus store in soil.
From raw manure phosphorus can easily transfer into natural waters with sediments. This phosphorus binding phenomenon is also seen in the Figure 4 where solubility of phosphorus decreases when the composting process proceeds. The io Composition 1 reduces the amount of water soluble phosphorus in the compost. In
Figure 4 we can see that the Composition 1 has clear acceleration potency to the binding of phosphorus in horse manure compost.
It will be obvious to a person skilled in the art that, as the technology advances, the inventive concept can be implemented in various ways. The invention and its embodiments are not limited to the examples described above but may vary within the scope of the claims.

Claims (15)

1. Koostumus typpeä sisältävien orgaanisten jätteiden, erityisesti lannan, käsittelemiseksi, käsittäen:Composition for the treatment of nitrogenous organic wastes, in particular manure, comprising: a. natriumbentoniittia;a. Sodium bentonite; b. orgaanista polyproottista happoa (happoja);b. organic polypeptic acid (s); c. rauta(ll)sulfaattia; jac. iron (II) sulfate; and d. alkalista mineraalia (mineraaleja).d. alkaline mineral (s). 2. Patenttivaatimuksen 1 mukainen koostumus, jossa natriumbentoniitin (a) määrä esillä olevassa koostumuksessa on välillä 45—80 paino-% koostumuksen kokonaispainosta.The composition of claim 1, wherein the amount of sodium bentonite (a) in the present composition is between 45 and 80% by weight of the total weight of the composition. 3. Patenttivaatimuksen 1 tai 2 mukainen koostumus, jossa orgaaninen polyproottinen happo (hapot) valitaan ryhmästä, jossa ovat C2-10dikarboksyylihapot ja C2-io-trikarboksyylihapot.The composition according to claim 1 or 2, wherein the organic polypeptic acid (s) is selected from the group consisting of C 2-10 dicarboxylic acids and C 2-10 tricarboxylic acids. 4. Minkä tahansa patenttivaatimusten 1-3 mukainen koostumus, jossa polyproottisen hapon (happojen) (b) kokonaismäärä esillä olevassa koostumuksessa on korkeintaan 20 paino-% koostumuksen kokonaispainosta.A composition according to any one of claims 1 to 3, wherein the total amount of polypeptic acid (s) in the present composition is up to 20% by weight of the total weight of the composition. 5. Minkä tahansa patenttivaatimusten 1-4 mukainen koostumus, jossa orgaaninen polyproottinen happo (hapot) valitaan ryhmästä, jossa ovat sitruunahappo, viinihappo, ja näiden mitkä tahansa seokset.The composition of any one of claims 1 to 4, wherein the organic polypeptic acid (s) is selected from the group consisting of citric acid, tartaric acid, and any mixtures thereof. 6. Patenttivaatimuksen 5 mukainen koostumus, jossa esillä olevassa koostumuksessa sitruunahapon määrä on 3—8 paino-% koostumuksen kokonaispainosta ja esillä olevassa koostumuksessa viinihapon määrä on 1—6 paino-% koostumuksen kokonaispainosta.The composition of claim 5, wherein the present composition comprises citric acid in an amount of 3 to 8% by weight of the total composition and tartaric acid in the present composition is in the range of 1 to 6% by weight of the total composition. 7. Minkä tahansa patenttivaatimusten 1-6 mukainen koostumus, jossa rauta(ll)sulfaatin (c) määrä esillä olevassa koostumuksessa on 0,5—10 paino-% koostumuksen kokonaispainosta.The composition of any one of claims 1 to 6, wherein the amount of iron (II) sulfate (c) in the present composition is 0.5 to 10% by weight of the total weight of the composition. 8. Minkä tahansa patenttivaatimusten 1-7 mukainen koostumus, jossa alkalisen mineraalin (mineraalien) (d) määrä esillä olevassa koostumuksessa on 5—35 paino-% koostumuksen kokonaispainosta.The composition of any one of claims 1 to 7, wherein the amount of alkaline mineral (s) (d) in the present composition is from 5% to 35% by weight of the total weight of the composition. 9. Minkä tahansa patenttivaatimusten 1-8 mukainen koostumus, jossa alkalinen mineraali (d) on silikaatti-kalkkikivi.The composition of any one of claims 1 to 8, wherein the alkaline mineral (d) is a silicate-limestone. 10. Minkä tahansa patenttivaatimusten 1-9 mukainen koostumus, jossa koostumuksessa on lisäksi (e) mineraali-kantajaa (-kantajia), edullisesti talkkia.The composition according to any one of claims 1 to 9, wherein the composition further comprises (e) a mineral carrier (s), preferably talc. 11. Minkä tahansa patenttivaatimusten 1-10 mukainen koostumus, jossa koostumus on jauhe- tai granulaarisessa muodossa.A composition according to any one of claims 1 to 10, wherein the composition is in powder or granular form. 12. Minkä tahansa patenttivaatimusten 1-11 mukaisen koostumuksen käyttö kompostoimaan typpeä sisältäviä orgaanisia jätteitä, kuten lantaa.Use of a composition according to any one of claims 1 to 11 for composting nitrogenous organic wastes such as manure. 13. Minkä tahansa patenttivaatimusten 1-11 mukaisen koostumuksen käyttö estämään ja/tai vähentämään ammoniakkipäästöjä typpeä sisältävistä orgaanisista jätteistä, kuten lannasta.Use of a composition according to any one of claims 1 to 11 for preventing and / or reducing ammonia emissions from nitrogenous organic wastes such as manure. 14. Minkä tahansa patenttivaatimusten 1-11 mukaisen koostumuksen käyttö estämään ja/tai vähentämään pahanhajuisia päästöjä typpeä sisältävistä orgaanisista jätteistä, kuten lannasta.Use of a composition according to any one of claims 1 to 11 for preventing and / or reducing bad odor emissions from nitrogen-containing organic wastes such as manure. 15. Minkä tahansa patenttivaatimusten 1-11 mukaisen koostumuksen käyttö dispergoimaan kolloidista lietettä typpeä sisältävissä orgaanisissa jätteissä, kuten lannassa.Use of a composition according to any one of claims 1 to 11 for dispersing a colloidal slurry in nitrogen-containing organic waste such as manure.
FI20165130A 2016-02-19 2016-02-19 Compositions for treating nitrogen containing organic wastes FI127616B (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
FI20165130A FI127616B (en) 2016-02-19 2016-02-19 Compositions for treating nitrogen containing organic wastes
EP17707938.1A EP3416931A1 (en) 2016-02-19 2017-02-15 Compositions for treating nitrogen containing organic wastes
PCT/FI2017/050090 WO2017140947A1 (en) 2016-02-19 2017-02-15 Compositions for treating nitrogen containing organic wastes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FI20165130A FI127616B (en) 2016-02-19 2016-02-19 Compositions for treating nitrogen containing organic wastes

Publications (2)

Publication Number Publication Date
FI20165130A FI20165130A (en) 2017-08-20
FI127616B true FI127616B (en) 2018-10-31

Family

ID=58191483

Family Applications (1)

Application Number Title Priority Date Filing Date
FI20165130A FI127616B (en) 2016-02-19 2016-02-19 Compositions for treating nitrogen containing organic wastes

Country Status (3)

Country Link
EP (1) EP3416931A1 (en)
FI (1) FI127616B (en)
WO (1) WO2017140947A1 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4133984A1 (en) * 1991-10-14 1993-04-15 Rudolf Prof Dr Kuerner METHOD FOR BIOLOGICAL DIGESTION OF MINERALS
JP2002253076A (en) * 2001-02-28 2002-09-10 Daiki:Kk Granular excrement disposal material and method for producing the same
FI20070298A0 (en) * 2007-04-17 2007-04-17 Pekka Pohjola Accelerator for aerobic biodegration

Also Published As

Publication number Publication date
WO2017140947A1 (en) 2017-08-24
FI20165130A (en) 2017-08-20
EP3416931A1 (en) 2018-12-26

Similar Documents

Publication Publication Date Title
Guo et al. The role of biochar in organic waste composting and soil improvement: A review
Barthod et al. Composting with additives to improve organic amendments. A review
Cáceres et al. Nitrification within composting: A review
Wong et al. Improving compost quality by controlling nitrogen loss during composting
Li et al. Ammonia volatilization mitigation in crop farming: A review of fertilizer amendment technologies and mechanisms
Banegas et al. Composting anaerobic and aerobic sewage sludges using two proportions of sawdust
Zhu et al. Reducing odor emissions from feces aerobic composting: additives
Insam et al. Control of GHG emission at the microbial community level
KR20130123276A (en) Method for treating wastewater and composting of organic wastes
Hao et al. Nitrogen transformation and losses during composting and mitigation strategies
JP5791728B2 (en) Manufacturing method of organic fertilizer
RU2645901C1 (en) Method for utilization and disinfection of chicken manure
Ivanov et al. Iron-containing clay and hematite iron ore in slurry-phase anaerobic digestion of chicken manure
Bong et al. Integrating compost and biochar towards sustainable soil management
Xiang-dong et al. Nitrogen loss and its control during livestock manure composting.
Logan et al. The alkaline stabilization with accelerated drying process (N‐Viro): An advanced technology to convert sewage sludge into a soil product
Maleki et al. Release kinetics of carbon, nitrogen, phosphorus, and potassium during co-composting of poultry manure mixed with different ratios of wheat straw and zeolite
Aboutayeb et al. Effect of carbon to nitrogen ratio and aeration rate on phosphorus and exchangeable cation contents and their leaching in the soil during olive pomace and turkey manure co-composting
CN111925240A (en) Nitrogen-preserving deodorant for high-temperature composting of livestock and poultry manure
Luo et al. Phosphorus transformations in swine manure during continuous and intermittent aeration processes
WO2008125739A1 (en) Aerobic biodegradation accelerant
FI127616B (en) Compositions for treating nitrogen containing organic wastes
RU2505512C1 (en) Method of production of humus-containing component of organo-mineral fertilisers and soil substrates
Nakasaki et al. Effect of bulking agent on the reduction of NH3emissions during thermophilic composting of night-soil sludge
Gondek et al. Compost produced with addition of sewage sludge as a source of Fe and Mn for plants

Legal Events

Date Code Title Description
FG Patent granted

Ref document number: 127616

Country of ref document: FI

Kind code of ref document: B