WO2009023001A1 - Procédé de fabrication en série d'engrais bioactifs organo-minéraux équilibrés - Google Patents

Procédé de fabrication en série d'engrais bioactifs organo-minéraux équilibrés Download PDF

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Publication number
WO2009023001A1
WO2009023001A1 PCT/UA2008/000010 UA2008000010W WO2009023001A1 WO 2009023001 A1 WO2009023001 A1 WO 2009023001A1 UA 2008000010 W UA2008000010 W UA 2008000010W WO 2009023001 A1 WO2009023001 A1 WO 2009023001A1
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WO
WIPO (PCT)
Prior art keywords
mass
compost
during
stage
matter
Prior art date
Application number
PCT/UA2008/000010
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English (en)
Russian (ru)
Other versions
WO2009023001A9 (fr
Inventor
Volodymyr Poupine
Original Assignee
Volodymyr Poupine
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 Volodymyr Poupine filed Critical Volodymyr Poupine
Priority to EA200901465A priority Critical patent/EA015115B1/ru
Publication of WO2009023001A1 publication Critical patent/WO2009023001A1/fr
Publication of WO2009023001A9 publication Critical patent/WO2009023001A9/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/90—Apparatus therefor
    • C05F17/989—Flow sheets for biological or biochemical treatment
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/10—Addition or removal of substances other than water or air to or from the material during the treatment
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/50—Treatments combining two or more different biological or biochemical treatments, e.g. anaerobic and aerobic treatment or vermicomposting and aerobic treatment
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/70—Controlling the treatment in response to process parameters
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/145—Feedstock the feedstock being materials of biological origin
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Definitions

  • the invention relates to agriculture, and more specifically, to a continuous method for the production of balanced organic-mineral bioactive fertilizers.
  • the method can be used for the production of balanced organic-mineral bioactive fertilizers by disposing of chicken manure from industrial poultry farms by composting litter or litterless bird manure with the introduction of the necessary mineral additives and specific microbiocenosis.
  • a known method of producing an organo-mineral mixture based on peat, defecate, sewage sludge, bentonite clay, ash from sunflower husks and buckwheat comprising extracting said mass in a bioreactor at a temperature in the mesophilic mode +25 - +35 0 C, and then at thermophilic fermentation +55 - + 65 ° C, after which the product is fed to a centrifuge, and then for granulation and drying [Ukrainian Patent for invention N ° 56293, IPC (2006) C05G1 / 00, A01C ⁇ / 00. Publication date 05/15/2003, Bull. N ° 3, 2003].
  • the disadvantage of the described method lies in the imbalance of the obtained organo-mineral mixture in terms of the content of basic nutrients, as well as in the absence of funds for organizing the in-line process of fertilizer production, which makes it impossible to organize the utilization of bird droppings in continuous mode throughout the year.
  • the inability to utilize bird droppings in a continuous mode leads to its accumulation and, as a result, to environmental pollution.
  • the method includes mixing operations on a concrete site using a self-propelled mixer of pus and bird droppings with a carrier of organic carbon, laying the resulting mixture in piles and holding in piles for 3-5 days. The mixture is then transferred to an aeration reactor, where it is purged with an ozone-oxygen mixture. After unloading from the reactor, the prepared compost is kept in piles, and after removal of large inclusions from it, it is packed up.
  • the described method does not make it possible to produce fertilizers that would ensure the achievement of stable and high yields of crops on different types of soils.
  • the basis of the invention is the task of creating such a flow method for the production of balanced organic fertilizers, which would create the conditions for obtaining a product with a given content of basic nutrients and a balanced NPK ratio, would ensure stable product quality and reduce the dependence of fertilizer production on climatic conditions, and It would also allow to quickly change the product formulation depending on agronomic needs - for different types of soils biological features of crops.
  • the problem is solved by the proposed method by creating conditions for the optimal course of microbiological processes during the continuous composting process by creating and maintaining optimal temperature and humidity parameters at the stages of fertilizer production.
  • the proposed method makes it possible to adjust the composition of the product depending on the type of plants and soil, by adding to the compost mass a predetermined amount of nutrients, sorbents, ion exchangers, as well as specific microbocenosis at certain stages of the technological process.
  • the proposed, as well as the known in-line method for the production of balanced organic-mineral fertilizers includes a continuous process of composting the compost mass, which is mixed and moved along the premises to obtain organic-mineral fertilizers, and, in accordance with the invention, the method includes three stages. At the first stage, a native carbon carrier (N) is added to the native bird droppings, an organic carbon (C) carrier is added until the ratio C to N is reached from 20 to 30, and exoenzymes and substances designed to bind nitrogen compounds, phosphogypsum, are directly added to the litter of the bird. , manganese sulfate, superphosphate.
  • a collar is formed, the compost mass in the collar is moistened to a moisture content of 55 - 65% and periodically briefly flushed with air for 2 to 3 minutes with an interval of 60 to 90 minutes. Air is supplied through a duct located on the floor of the room.
  • the temperature of the mass in the first three days is adjusted to +65 - + 75 ° C.
  • the filtrate formed during this period is discharged into a separate tank and used to moisten the compost mass in the first three-day cycle, and gradually until the end of the last three-day cycle the temperature of the mass is reduced to +30 - + 35 ° C.
  • a mixture of peat, lime or gypsum pre-mixed in the required proportions is added to the compost mass.
  • a specific microbiocenosis is added to the compost mass, and during the second stage, which includes at least two three-day cycles, the compost mass is mixed and moved, during which ripening of the mass occurs with a specific microbiocenosis, reduce the temperature of the mass to +20 - +25 0 C and reduce humidity to 35 - 40%.
  • the third stage begins - a pre-mixed mixture of mineral additives, sorbents, ion exchangers and trace elements is added to the compost mass to achieve a balance in nutrients and trace elements.
  • the compost mass is mixed and moved until a homogeneous mass of balanced organic fertilizers with a moisture content of 20-30% is obtained.
  • a feature of the proposed method is also that the fertilizers obtained are dried to a moisture content of 16-18%, granulated and then Packed.
  • the proposed method is implemented on the production line shown in the schematic drawing.
  • the production line consists of a composting workshop 1, intended for composting using a composting device installed in workshop 1.
  • the inputs of workshop 1 are connected to the outputs of workshop 2, which is used to prepare components and impurities - mixtures N ° l, N ° 2, N ° 3 and feed them to compost shop 1 at certain stages of the technological process.
  • Workshop 2 is equipped with devices for dispensing components and impurities and mixing mixtures.
  • One exit of workshop 1 is connected to the entrance of the drying and granulating workshop 3, and the second to the entrance of the packaging workshop 4.
  • the finished fertilizers in the form of a homogeneous mass can be directly fed to the packaging workshop 4, where the filling machines are installed, or to the drying and granulation workshop 3, where devices for drying the product and processing it into granules are installed. Finished granules from workshop 3 are fed to workshop 4 for packaging on filling machines in bags or bags.
  • the resulting mixture of NaI is fed into the composting device in the composting shop 1.
  • a collar is formed.
  • the compost mass in the collar is moistened to a moisture content of 55 - 65% and periodically flushed with air for 3 to 5 minutes with an interval of 60 to 90 minutes, which is fed through a duct located on the floor of workshop 1.
  • the filtrate formed during this period is taken to a separate tank (not shown) and used to moisten the compost mass during the first three-day cycle. Gradually, until the end of the last three-day cycle, the temperature is reduced to +30 - +35 0 C and the second stage begins.
  • a mixture of peat, lime or gypsum - a mixture of N ° 2, pre-mixed in the required proportions, is added to the compost mass, and a specific microbiocenosis is added, which are supplied from workshop 2.
  • the compost is mixed and moved mass in workshop 1.
  • the mass ripens with a specific microbiocenosis, its temperature decreases to +20 - +25 0 C and humidity to 40%.
  • the third stage begins - a mixture of mineral additives, sorbents, ion exchangers and, if necessary, trace elements, a mixture of Ns ⁇ , is pre-mixed in the required proportions from workshop 2.
  • the compost is mixed and moved to workshop 1 and the humidity is reduced to 20-30%.
  • the humidity is reduced to 20-30%.
  • three compost lines are installed in parallel, and to increase power, the number of compost lines is increased, a multiple of three.
  • the resulting organo-mineral balanced bioactive fertilizers in the form of a homogeneous mass of dark brown or brown color are non-toxic, environmentally friendly for people and the environment.
  • Fertilizers are sent for packaging in workshop 4 or in workshop 3 to a drying plant, where the processes are carried out according to known technology [see

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Molecular Biology (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Organic Chemistry (AREA)
  • Fertilizers (AREA)

Abstract

L'invention concerne le domaine de l'agriculture et plus précisément un procédé de fabrication en série d'engrais bioactifs organo-minéraux équilibrés, qui se présente comme un processus ininterrompu de compostage d'une masse à composter qui est mélangée et déplacée le long d'un local, et ce en trois étapes. A la première étape, on ajoute à la fiente d'oiseaux native un support de carbone organique (C) jusqu'à ce qu'une proportion C / N de 20 à 30 soit atteinte, et l'on ajoute à la fiente d'oiseaux sur litière des exoferments et des substances destinées à lier les substances azotées, qui sont mélangées, formées en un tas, humidifiées jusqu'à 55-65% d'humidité puits aérées avec de l'air pendant 2-3 minutes avec un intervalle de 60-90 minutes. La température de la masse pendant les trois premiers jours est portée à 65-75°C. Pendant les premiers trois ou cinq cycles de trois jours on effectue le mélangeage et le déplacement de la masse obtenue. Le filtrat formé pendant cette période est utilisé pour humidifier la masse de compost pendant un premier cycle de trois jours. Graduellement et jusqu'à la fin du dernier cycle de trois jours, on abaisse la température du cycle jusqu'à 30-35°C. Après la fin de la première étape on ajoute à la masse de compost un mélange de tourbe, de chaux ou de plâtre de manière à provoquer une microbiocénose spécifique et, pendant la deuxième étape, on effectue le mélangeage et le déplacement de la masse de compost jusqu'à 20-25°C et l'on réduit l'humidité jusqu'à 35-40%. A la troisième étape on ajourne à la masse de compost un mélange d'additifs minéraux, de sorbants, d'échangeurs d'ions et de micro-éléments. Lors des deux cycles suivants on effectue le mélangeage et le déplacement de la masse de composte jusqu'à ce que l'on obtienne une masse d'engrais homogène avec une humidité de 20-30 %, qui est séchée jusqu'à 16-18%, granulée et conditionnée. Le procédé proposé dans l'invention permet d'obtenir un produit possédant une teneur désirée en éléments de base biogènes et un rapport équilibré d'azote, de phosphore et de sodium (NPK), assure une qualité stable du produit et l'indépendance de fabrication par rapport aux conditions climatiques ainsi que de faire varier rapidement la composition des produits en fonction des besoins agronomiques.
PCT/UA2008/000010 2007-08-10 2008-03-12 Procédé de fabrication en série d'engrais bioactifs organo-minéraux équilibrés WO2009023001A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EA200901465A EA015115B1 (ru) 2007-08-10 2008-03-12 Поточный способ производства сбалансированных органо-минеральных биоактивных удобрений

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
UAU200709173 2007-08-10
UAU200709173U UA26649U (en) 2007-08-10 2007-08-10 Stream method for production of balanced organomineral bioactive fertilizers

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WO2009023001A1 true WO2009023001A1 (fr) 2009-02-19
WO2009023001A9 WO2009023001A9 (fr) 2010-06-17

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UA (1) UA26649U (fr)
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011019329A1 (fr) * 2009-08-11 2011-02-17 Pupin Volodymyr Chaîne de transformation de déchets organiques en engrais organo-minéral
CN104311288A (zh) * 2014-10-10 2015-01-28 安徽万利生态园林景观有限公司 一种废弃床垫料制成的茄子苗圃基肥及其制备方法
RU2653083C1 (ru) * 2017-03-06 2018-05-07 Олег Анатольевич Фильченков Способ переработки птичьего помета в органоминеральное удобрение (варианты)
RU2784389C1 (ru) * 2021-12-10 2022-11-24 Федеральное государственное бюджетное образовательное учреждение высшего образования "Рязанский государственный агротехнологический университет имени П.А. Костычева" Способ обогащения почвы при возделывании овса на черноземах

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1890459A (en) * 1926-06-23 1932-12-13 Wilhelm Von Radowitz Process of making fertilizers from feces or the like
RU2048722C1 (ru) * 1993-02-02 1995-11-27 Конструкторское бюро "Салют" Способ переработки отходов животноводства в удобрение и установка для его осуществления
RU2291136C2 (ru) * 2004-11-09 2007-01-10 ФГОУ ВПО "Мичуринский государственный аграрный университет" Поточный способ производства компоста

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1890459A (en) * 1926-06-23 1932-12-13 Wilhelm Von Radowitz Process of making fertilizers from feces or the like
RU2048722C1 (ru) * 1993-02-02 1995-11-27 Конструкторское бюро "Салют" Способ переработки отходов животноводства в удобрение и установка для его осуществления
RU2291136C2 (ru) * 2004-11-09 2007-01-10 ФГОУ ВПО "Мичуринский государственный аграрный университет" Поточный способ производства компоста

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011019329A1 (fr) * 2009-08-11 2011-02-17 Pupin Volodymyr Chaîne de transformation de déchets organiques en engrais organo-minéral
CN104311288A (zh) * 2014-10-10 2015-01-28 安徽万利生态园林景观有限公司 一种废弃床垫料制成的茄子苗圃基肥及其制备方法
RU2653083C1 (ru) * 2017-03-06 2018-05-07 Олег Анатольевич Фильченков Способ переработки птичьего помета в органоминеральное удобрение (варианты)
RU2784389C1 (ru) * 2021-12-10 2022-11-24 Федеральное государственное бюджетное образовательное учреждение высшего образования "Рязанский государственный агротехнологический университет имени П.А. Костычева" Способ обогащения почвы при возделывании овса на черноземах

Also Published As

Publication number Publication date
UA26649U (en) 2007-09-25
WO2009023001A9 (fr) 2010-06-17

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