WO2019117650A1 - Controlled release fertilizer - Google Patents

Controlled release fertilizer Download PDF

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Publication number
WO2019117650A1
WO2019117650A1 PCT/KR2018/015866 KR2018015866W WO2019117650A1 WO 2019117650 A1 WO2019117650 A1 WO 2019117650A1 KR 2018015866 W KR2018015866 W KR 2018015866W WO 2019117650 A1 WO2019117650 A1 WO 2019117650A1
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WO
WIPO (PCT)
Prior art keywords
fertilizer
vinyl acetate
weight
fine particles
inorganic fine
Prior art date
Application number
PCT/KR2018/015866
Other languages
French (fr)
Korean (ko)
Inventor
김찬중
이준석
장일
이상려
김지연
최재훈
Original Assignee
주식회사 엘지화학
주식회사 팜한농
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
Priority claimed from KR1020180160288A external-priority patent/KR102510340B1/en
Application filed by 주식회사 엘지화학, 주식회사 팜한농 filed Critical 주식회사 엘지화학
Priority to US16/646,681 priority Critical patent/US11427514B2/en
Priority to CN201880054387.5A priority patent/CN111094214A/en
Priority to JP2020519767A priority patent/JP7146331B2/en
Priority to AU2018385840A priority patent/AU2018385840B2/en
Publication of WO2019117650A1 publication Critical patent/WO2019117650A1/en
Priority to PH12020550880A priority patent/PH12020550880A1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G3/00Mixtures of one or more fertilisers with additives not having a specially fertilising activity

Definitions

  • the present invention relates to a dissolution-controlled fertilizer, and more particularly, to a dissolution-control-type fertilizer having a high stability against moisture, a solid structure, and an easily controlling dissolution period of a fertilizer and realizing excellent photodissociation efficiency.
  • Controlled release fertilizers such as nitrogen, phosphorus and potassium
  • Conventional fertilizers that are sprayed in water or sprayed in powder form usually do not last for more than 20 days once sprayed. This is due to the fact that the crops are not able to sustain the fertilizer composition because they are washed away in the rain or deeply penetrated into the soil.
  • the controlled release type fertilizer lowers the release rate of the fertilizer component with the polymer capsules so that it is released over a long period of time.
  • the polymer capsules are made of olefin resin, urethane resin, latex, acrylic resin, etc. After the water vapor penetrates through the capsules, the fertilizer components are melted, and the capsules are permeated and released by the osmotic principle. The penetration rate of water and fertilizer components varies depending on the ingredients and the thickness of the capsules. This can be used to control the rate at which the fertilizer component is released. The period of release of the fertilizer component from the capsule can be adjusted from a minimum of 30 days to a maximum of 2 years. However, after release of the fertilizer, 2019/117650 1 » (: 1 ⁇ 1 ⁇ 2018/015866
  • biodegradable polymer As a capsule material. Since the biodegradable polymer is rapidly permeated by water and decomposed by microorganisms within 1 month to 6 months, It was not suitable for use in controlled-release fertilizers that had to be released over two years.
  • the present invention provides a controlled-release fertilizer having a high stability against water and a solid structure, capable of easily controlling the dissolution period of 10 of the fertilizer, and capable of realizing excellent photodegradation efficiency.
  • polyolefin and ethylene vinyl acetate binder resin containing the copolymer and (co) including a repeating unit selected at least one from the 15 group consisting of ethylene repeating units and vinyl acetate repeating units of the polymer, the surface of the agglomerates of the inorganic fine particles Or a photocatalytic composite comprising a photocatalyst composite and a photocatalytic composite, the photocatalytic composite comprising a photocatalytic composite and a photocatalytic composite, the photocatalytic composite comprising:
  • the (co) polymer is meant to include both a polymer and a copolymer.
  • the polyolefin and ethylene vinyl acetate binder resin including co-polymer; of and ethylene repeating units and vinyl including repeating units of at least one member selected from the group consisting of acetate repeating units (co) polymer, the inorganic fine particles the photocatalyst composite material bonded to the surface or interior of the aggregates; a dissolution-controlled fertilizer comprising the fertilizer contained in the space 30 surrounded by the photodegradable capsules and the capsules containing photodegradable can be provided.
  • a release-controlled fertilizer having a photocatalytic capsule containing the above-described photocatalytic composite together with a binder resin containing a polyolefin and an ethylene vinyl acetate copolymer has a high stability against moisture and a rigid structure and can easily control the duration of a fertilizer And it is possible to realize excellent photodecomposition efficiency.
  • the above-mentioned dissolution-controlled fertilizer is also characterized in that the photocatalytic composite is uniformly dispersed in the above-mentioned binder resin.
  • the (co) polymer containing at least one repeating unit selected from the group consisting of the ethylene repeating unit and the vinyl acetate repeating unit is bound to the surface or inside of the agglomerate of the inorganic fine particles, Or the inorganic fine particles can be uniformly dispersed in the leaching control type fertilizer, so that the agglomerate of the inorganic fine particles can have a large particle size.
  • the agglomerates of the inorganic fine particles are uniformly dispersed in the binder resin while having a small particle size, so that photodegradation reaction is locally caused when the photodegradable capsules are exposed to light, thereby preventing degradation of photodecomposition efficiency So that the photodegradable capsules do not remain in the soil.
  • the lanyard-controlled fertilizer can realize excellent photodegradation efficiency. More specifically, when light of a wavelength of 300 11111 to 800 is irradiated at a strength of 400 for 224 hours, the weight of the photodegradable capsule
  • the decomposition ratio of the binder resin to be derived may be 40% or more, or 50% or more.
  • the inorganic fine particles may serve as a photocatalyst.
  • the lance-controlled fertilizer of the embodiment is characterized in that the photocatalytic composite is uniformly dispersed in the binder resin in order to solve the problem that the photodegradable capsule remains in the soil.
  • the photocatalytic complex acts as a catalyst only during the light receiving period, the photocatalytic capsule is slowly decomposed while the photocatalytic capsule is not decomposed while the fertilizer is released in the soil where the light is blocked.
  • the photodegradable capsule may be decomposed by light.
  • the inorganic fine particle may comprise primary particles having a cross-sectional diameter of 5 to 50 nm.
  • Cross-sectional diameter of the primary particles of said inorganic fine particles are conventionally known method, for example, verification by the TEM image and, BET Measurement and so on.
  • the degree of crystallization can be the photocatalytic efficiency is lowered away. Further, the cross-sectional diameter of the primary particles is too large, the photocatalytic particles contained in the inorganic fine particle The specific surface area is lowered and the photocatalytic efficiency may be lowered.
  • the agglomerates of the inorganic fine particles contained in the dissolution-controlled fertilizer of the above embodiment may have a particle size not so large.
  • the cross-sectional diameter and the diameter of the agglomerate of the inorganic fine particles can be confirmed by a commonly known method, for example, SEM or TEM microtome.
  • the cross-sectional diameter or overall size of the aggregates of the inorganic fine particles 25 is too large, there is a localized photolytic reaction in the photodegradable capsule can be up or decrease the efficiency of photolysis reaction, due to the inefficient photolysis reaction entire photodegradable capsule It may not be decomposed and residues may remain.
  • inorganic fine particles include titanium dioxide ( TiO2), zinc oxide (ZnO), and mixtures thereof.
  • the binder resin may be a main material forming the outer structure of the photodegradable capsule, and as described above, the binder resin may include a polyolefin and an ethylene vinyl acetate copolymer.
  • polystyrene resin examples include, but are not limited to, high density or low density polyethylene, linear low density polyethylene, polypropylene, ethylene-propylene copolymer, polybutene, butene-ethylene copolymer, butene- Mixtures thereof, or copolymers of two or more thereof.
  • the ethylene vinyl acetate copolymer contained in the binder resin is not particularly limited.
  • an ethylene vinyl acetate copolymer containing 1 to 45% by weight of vinyl acetate repeating units may be used.
  • the ethylene vinyl acetate copolymer has a melt index of 0.5 / 10 11 to 5.0 / 10 11 or 1.0 / 10 11 to 3.0 ⁇ measured at 190 and 2.161 ⁇ load, / 10 1 can be 11 days.
  • the binder resin may include a polyolefin: ethylene vinyl acetate copolymer in a weight ratio of 1: 1 to 6: 1 have.
  • the dissolution rate of the fertilizer can be more easily controlled as the binder resin contains the polyolefin resin equal to or more than the ethylene vinyl acetate copolymer.
  • the photocatalytic composite may have a structure in which a (co) polymer containing at least one repeating unit selected from the group consisting of ethylene repeating units and vinyl acetate repeating units is bonded to the surface or inside of aggregates of inorganic fine particles.
  • the agglomerate of the inorganic fine particles can act as a photocatalyst, and when the dissolution-controlled fertilizer is exposed to the surface of the soil or the like, the photolytic reaction can be started in the photodegradable capsule.
  • the (co) polymer containing at least one repeating unit selected from the group consisting of the ethylene repeating unit and the vinyl acetate repeating unit is preferably a 2019/117650 1 » (: 1 ⁇ 1 ⁇ 2018/015866
  • the inorganic fine particles are prevented from excessively growing in size and have higher compatibility with the binder resin so that the photocatalytic composite is uniformly dispersed in the binder resin, .
  • ethylene repeating units and vinyl acetate repeating units one or more kinds selected from the group consisting of repeating units of the (co) polymer can contain both an ethylene vinyl acetate repeating units, or repeating units thereof.
  • Examples of the above ethylene repeating units and vinyl acetate (co) including a repeating unit selected at least one from the group consisting of repeating units of the polymer is 10 and the number of the ethylene vinyl acetate copolymers, and vinyl acetate repeating units from 1% to by weight 45 may be used an ethylene-vinyl acetate copolymer containing by weight%.
  • the ethylene-vinyl acetate copolymer shows ⁇ 1) on by 1901 1238: and 2.16 ⁇ 3 ⁇ 4 load a melt index of 0.5 for a / 10 to 5.0 for a / 10 1 or / 101 11 - / 10 per 3.0 1.0 measured at ⁇ Can be.
  • the photocatalyst composite may be prepared through the step of dispersing (co) polymer containing a repeating unit at least one selected from the group consisting of the inorganic fine particles and the ethylene repeating units and vinyl acetate repeating units in the organic solvent.
  • the weight ratio of the inorganic fine particles (co) polymer is not limited to a great extent, and the weight ratio can be controlled by controlling the amount of the organic fine particles dispersed in the organic solvent according to the characteristics of the dissolution control type fertilizer. It can be contained in 100 parts by weight of the aggregate compared to the ethylene repeating units and 25 vinyl (co) polymer, from 1 to 500 parts by weight of a repeating unit including at least one selected from the group consisting of acetate repeating units, or from 20 to 200 parts by weight. On the other hand, 0.1 to 8 parts by weight of 30 aggregates of the inorganic fine particles may be included relative to 100 parts by weight of the binder resin. 2019/117650 1 » (: 1 ⁇ 1 ⁇ 2018/015866
  • the photolysis reaction efficiency may be lowered, and the entire photodegradable capsule may not be decomposed due to insufficient photolysis reaction, .
  • the agglomerate of the inorganic fine particles may grow to a large extent, thereby causing a local photodegradation reaction in the photodegradable capsule, The efficiency of the photolysis reaction is lowered, so that the entire photodegradable capsule is not decomposed and the residue may remain.
  • the release-controlled fertilizer may further comprise a filler to be dispersed in the binder resin but are not the kind of the filler largely limited, and for example the filler is talc, bentonite, yellow earth, diatomaceous earth, silica-alumina Silicate, kaolite, starch, carbon, or a mixture of two or more thereof.
  • the content of the filler is not limited, but the lumber-controlling type fertilizer may contain 25 to 75 % by weight of the filler in relation to the total weight of the photodegradable capsule in consideration of the mechanical properties and structural stability of the photodegradable capsule
  • the fertilizer may be any of a variety of known fertilizers, such as urea or compound fertilizer.
  • the fertilizer may be a granular core fertilizer having a granular form in order to be easily contained in the photodegradable capsule.
  • the specific kind of the above-mentioned fertilizer is not limited, and conventionally known fertilizers can be used. Preferred examples are urea, aldehyde condensation element
  • 25 isobutylaldehyde condensation element, formaldehyde condensation element guanyl ureasulfate, and nitrogen containing organic compounds such as oxamide, ammonium nitrate, ammonium dihydrogenphosphate, ammonium dihydrogenphosphate, ammonium sulfate ammonium chloride, and ammonium nitrate such as sodium nitrate And potassium salts such as potassium nitrate, potassium nitrate, potassium nitrate, potassium phosphate, potassium sulfate, and potassium chloride, calcium phosphate, calcium sulfate, calcium nitrate,
  • magnesium nitrate magnesium chloride
  • magnesium phosphate and Iron salts such as ferric chloride, ferric nitrate, ferric phosphate, ferric phosphate, ferrous sulfate, ferric sulfate, ferrous chloride and ferric chloride, and their double salts or a mixture of two or more thereof.
  • the content of the fertilizer in the leaching control type fertilizer is not limited to a great extent.
  • 100 parts by weight of the photodegradable capsule may contain 200 to 3000 parts by weight of the fertilizer.
  • the photocatalytic composite may have a specific degree of dispersion in the photodegradable capsule. More specifically, the photocatalytic composite can be produced by dispersing (co) polymer containing the inorganic fine particles and one or more repeating units selected from the group consisting of ethylene repeating units and vinyl acetate repeating units in an organic solvent ,
  • a high-shear mixer or a bead mill may be used to disperse the inorganic fine particles and the (co) polymer in an organic solvent to transfer strong energy to the (co) polymer May be bonded to the surface or inside of the aggregate of the inorganic fine particles.
  • the photocatalytic composite thus produced can be dispersed very uniformly in the binder resin, and the decomposition efficiency of the photocatalyst can be remarkably increased.
  • the lanyard-controlled fertilizer may further comprise a component included in a known line-controlled fertilizer.
  • such components include, but are not limited to, amphipathic polymers.
  • the leaching control type fertilizer can be provided through various manufacturing methods.
  • the dispersion of inorganic fine particles is dispersed in an organic solvent to which an ethylene vinyl acetate copolymer is added to prepare a dispersion of the photocatalytic composite.
  • Preparing a coating composition by mixing a polyolefin, an ethylene vinyl acetate copolymer, a dispersion of the photocatalytic composite, and optionally a filler; And coating the surface of the granular fertilizer core with the coating composition.
  • organic solvent are not limited, 2019/117650 1 » (: 1 ⁇ 1 ⁇ 2018/015866
  • a dispersion can be prepared by using a strong energy such as a 5-ultrasonic wave ( 11 ratio 1 011 ) or a bead mill For example, ultrasonic waves ( 3011 ratio 31 ; 1 is 1 ), etc.
  • the dissolution-controlled fertilizer prevents the photodegradable capsule or the hydrophilic polymer from remaining in the soil, thereby preventing soil contamination.
  • Fig. 1 is a table photograph of each of the agglomerates of inorganic fine particles and the agglomerates of fine particles contained in the coated fertilizer of Comparative Example 2 in Example 1 and the photocatalytic composite contained in the dissolution-controlled fertilizer.
  • Figure 2 schematically depicts the photodegradation mechanism of a dissolution-controlled fertilizer
  • Ultrasonic waves were applied to prepare 5 dispersions of the photocatalytic composite coated with ethylene vinyl acetate copolymer.
  • the coating solution was applied to the nitrogen fertilizer particles using a fluidized bed dryer to prepare dissolution-controlled coated fertilizers (Examples 1 to 5 ).
  • 1613 ⁇ 4 load shows ⁇ 1) 1238): about 1.8 I / 10 1 11, I) (density): 0.94 ⁇ / 011 3) about 20% by weight vinyl acetate content, a melting point 85 ° 0], And talc were mixed with tetrachlorethylene at a mixing ratio of 100: 1 at a mixing ratio of 100: 1 by using the ingredients as shown in Table 1, and a coating liquid was prepared so that the solid concentration was 5% by weight.
  • the coating film was irradiated with light having a wavelength of 800 1 L at an intensity of 40 (1 ⁇ 2 / 111 2 ).
  • the degradation rate of the binder resin which is also reduced by the weight change of the coating film upon irradiation with light for 224 hours under the above conditions, was determined by the following general formula 1, and the results are shown in Table 1 below.
  • the z-average dispersion particle size of the TiO 2 of the dispersion containing the photocatalytic composite of Example 1 and the Ti3 ⁇ 4 of Comparative Example 2 was measured using Dynamic Light Scatterin g (M arvern Ze tasizer Nano ZS 90 ). The results are shown in Table 3 below.

Abstract

The present invention relates to a controlled release fertilizer comprising: a photodegradable capsule comprising a binder resin inclusive of polyolefin and ethylene vinyl acetate copolymer; and a photocatalyst composite in which a (co)polymer including at least one repeat unit selected from an ethylenic repeat unit and a vinyl acetate repeat unit is coupled to the surface or inside of an aggregate of inorganic microparticles; and a fertilizer contained within a space surrounded by the photodegradable capsule.

Description

【발명의 명칭】  Title of the Invention
용출제어형 비료  Controlled release fertilizer
【기술분야】  TECHNICAL FIELD
관련출원 (들)과의 상호인용  Cross-reference with related application (s)
본 출원은 2017년 12월 14일자 한국특허출원 제 10-2017-0172272호 및 2018년 12월 12일자 한국특허출원 제 10-2018-0160288호 에 기초한 우선권의 이익을 주장하며, 해당 한국 특허 출원들의 문헌에 개시된 모든 내용은본명세서의 일부로서 포함된다.  This application claims the benefit of priority based on Korean Patent Application No. 10-2017-0172272, dated December 14, 2017, and Korean Patent Application No. 10-2018-0160288, dated December 12, 2018, The entire contents of which are incorporated herein by reference.
본 발명은 용출 제어형 비료에 관한 것으로, 보다 상세하게는 수분에 대한 높은 안정성과 견고한 구조를 가지며 비료의 용출 기간을 용이하게 조절할 수 있고 아울러 우수한 광분해 효율을 구현할 수 있는 용출제어형 비료에 관한것이다.  The present invention relates to a dissolution-controlled fertilizer, and more particularly, to a dissolution-control-type fertilizer having a high stability against moisture, a solid structure, and an easily controlling dissolution period of a fertilizer and realizing excellent photodissociation efficiency.
【발명의 배경이 되는기술】  TECHNICAL BACKGROUND OF THE INVENTION
시비 (¾SE)의 생력화 내지는 식물의 생육에 따른 비료의 효과를 발현시킬목적으로각종용출제어형 비료가개발되어 있다.  Various leaching control type fertilizers have been developed for the purpose of harvesting fertilizer (SESE) or manifesting the effect of fertilizer according to the growth of plants.
이러한 용출제어형 비료 (Control led release fert i l i zers, CRF)는 질소 ·인 ·칼륨 등 비료 성분이 오랫동안 서서히 작물에 공급된다. 물에 타서 살포하거나분말형태로뿌리는기존비료는보통한번뿌리면 효과가 20일 이상 지속되기 어렵다. 비에 씻겨나가거나 땅속 깊이 스며들어 작물이 비료 성분을 톱수하기 어렵기 때문인데, 이러한 문제점 때문에 비료를과량으로자주뿌릴수밖에 없었다.  Controlled release fertilizers (CRFs), such as nitrogen, phosphorus and potassium, are slowly supplied to crops for a long time. Conventional fertilizers that are sprayed in water or sprayed in powder form usually do not last for more than 20 days once sprayed. This is due to the fact that the crops are not able to sustain the fertilizer composition because they are washed away in the rain or deeply penetrated into the soil.
용출제어형 비료는 이런 일반 비료 단점을보완하기 위하여 고분자 캡슐로 비료 성분의 방출 속도를 저하시켜 장기간 동안 방출되도록 한다 . 고분자캡슐은올레핀계 수지, 우레탄계 수지, 라텍스, 아크릴수지 등으로 만들어지며 캡슐을 통하여 수증기가 침투하면서 비료 성분이 녹은 후, 삼투압 원리에 의해 캡슐을 투과하여 방출된다. 캡슐을 어떤 성분으로, 어느정도두께로만드느냐에 따라물과비료성분의 침투속도가달라지게 된다. 이를 이용해 비료 성분이 밖으로 나오는 속도를 제어할 수 있다. 비료성분이 캡슐에서 방출되는기간은최소 30일에서 최대 2년까지 조절할 수 있다. 하지만 비료 방출 후 캡슐고분자는 분해되지 않고 토양이나 2019/117650 1»(:1^1{2018/015866 In order to compensate for these disadvantages of general fertilizer, the controlled release type fertilizer lowers the release rate of the fertilizer component with the polymer capsules so that it is released over a long period of time. The polymer capsules are made of olefin resin, urethane resin, latex, acrylic resin, etc. After the water vapor penetrates through the capsules, the fertilizer components are melted, and the capsules are permeated and released by the osmotic principle. The penetration rate of water and fertilizer components varies depending on the ingredients and the thickness of the capsules. This can be used to control the rate at which the fertilizer component is released. The period of release of the fertilizer component from the capsule can be adjusted from a minimum of 30 days to a maximum of 2 years. However, after release of the fertilizer, 2019/117650 1 » (: 1 ^ 1 {2018/015866
하천에 남아 있게 되는문제가 있다. There is a problem that remains in the river.
이 문제를 해결하기 위하여 생분해성 고분자를 캡슐소재로 이용하고자 하는 시도들이 이루어 졌으나, 생분해성 고분자는 수분침투가 빠르고 1달에서 6개월 사이에 미생물에 의하여 분해되기 때문에 비료성분이 5 최소 한 달에서 2년에 걸쳐 방출되어야 하는 용출 제어형 비료에 사용되기 적합하지 않았다. In order to solve this problem, attempts have been made to use a biodegradable polymer as a capsule material. Since the biodegradable polymer is rapidly permeated by water and decomposed by microorganisms within 1 month to 6 months, It was not suitable for use in controlled-release fertilizers that had to be released over two years.
【발명의 내용】  DISCLOSURE OF THE INVENTION
【해결하고자하는과제】  [Problem to be solved]
본 발명은수분에 대한높은 안정성과 견고한구조를 가지며 비료의 10 용출 기간을 용이하게 조절할수 있고 아울러 우수한 광분해 효율을구현할 수 있는용출 제어형 비료를 제공하기 위한 것이다. The present invention provides a controlled-release fertilizer having a high stability against water and a solid structure, capable of easily controlling the dissolution period of 10 of the fertilizer, and capable of realizing excellent photodegradation efficiency.
【과제의 해결 수단】  MEANS FOR SOLVING THE PROBLEMS
본 명세서에서는, 폴리올레핀 및 에틸렌비닐아세테이트 공중합체를 포함한 바인더 수지;및 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 15 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체가무기 미세 입자의 응집체의 표면 또는 내부에 결합된 광촉매 복합체;를 포함하는 광분해성 캡슐과, 상기 광분해성 캡슐로 둘러싸인 공간에 포함된 비료를 포함하는용출 제어형 비료가제공된다. In the present specification, polyolefin and ethylene vinyl acetate binder resin containing the copolymer, and (co) including a repeating unit selected at least one from the 15 group consisting of ethylene repeating units and vinyl acetate repeating units of the polymer, the surface of the agglomerates of the inorganic fine particles Or a photocatalytic composite comprising a photocatalyst composite and a photocatalytic composite, the photocatalytic composite comprising a photocatalytic composite and a photocatalytic composite, the photocatalytic composite comprising:
이하 발명의 구체적인 구현예에 따른 용출 제어형 비료에 관하여 20 보다상세하게 설명하기로 한다. 본 명세서에서, (공)중합체는 중합체와 공중합체를 모두 포함하는 의미이다. About dissolution-controlled fertilizer according to the specific implementation of the invention will be hereinafter described in detail than 20. In the present specification, the (co) polymer is meant to include both a polymer and a copolymer.
25 발명의 일 구현예에 따르면 폴리올레핀 및 에틸렌비닐아세테이트 공중합체를 포함한 바인더 수지;및 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체가 무기 미세 입자의 응집체의 표면 또는 내부에 결합된 광촉매 복합체;를 포함하는 광분해성 캡슐과, 상기 광분해성 캡슐로 둘러싸인 30 공간에 포함된 비료를포함하는용출 제어형 비료가제공될수 있다. 2019/117650 1»(:1^1{2018/015866 According to one embodiment of the 25 invention, the polyolefin and ethylene vinyl acetate binder resin, including co-polymer; of and ethylene repeating units and vinyl including repeating units of at least one member selected from the group consisting of acetate repeating units (co) polymer, the inorganic fine particles the photocatalyst composite material bonded to the surface or interior of the aggregates; a dissolution-controlled fertilizer comprising the fertilizer contained in the space 30 surrounded by the photodegradable capsules and the capsules containing photodegradable can be provided. 2019/117650 1 »(: 1 ^ 1 {2018/015866
본 발명자들은 폴리올레핀 및 에틸렌비닐아세테이트 공중합체를 포함한 바인더 수지와 함께 상술한 광촉매 복합체를 포함하는 광분해성 캡슐이 형성된 용출 제어형 비료가 수분에 대한 높은 안정성과 견고한 구조를가지며 비료의 용줄기간을용이하게 조절할수 있고아울러 우수한 광분해 효율을 구현할 수 있다는 점을 실험을 통하여 확인하고 발명을 완성하였다. The present inventors have found that a release-controlled fertilizer having a photocatalytic capsule containing the above-described photocatalytic composite together with a binder resin containing a polyolefin and an ethylene vinyl acetate copolymer has a high stability against moisture and a rigid structure and can easily control the duration of a fertilizer And it is possible to realize excellent photodecomposition efficiency.
상술한 용출 제어형 비료의 특징은 상기 광촉매 복합체를 상술한 바인더 수지에 균일하게 분산시킴에 따른것이기도하다. 구체적으로, 상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체가무기 미세 입자의 응집체의 표면 또는 내부에 결합됨에 따라서, 상기 용출 제어형 비료의 제조 과정이나상기 용출 제어형 비료 내에서 상기 무기 미세 입자가 균일하게 분산될 수 있고, 이에 따라 상기 무기 미세 입자의 응집체는 그리 크지 않은입경을가질수있다.  The above-mentioned dissolution-controlled fertilizer is also characterized in that the photocatalytic composite is uniformly dispersed in the above-mentioned binder resin. Specifically, as the (co) polymer containing at least one repeating unit selected from the group consisting of the ethylene repeating unit and the vinyl acetate repeating unit is bound to the surface or inside of the agglomerate of the inorganic fine particles, Or the inorganic fine particles can be uniformly dispersed in the leaching control type fertilizer, so that the agglomerate of the inorganic fine particles can have a large particle size.
이처럼 상기 무기 미세 입자의 응집체가 그리 크지 않은 입경을 가지면서 상기 바인더 수지에 균일하게 분산되어, 상기 광분해성 캡슐이 빛에 노출시 국지적으로 광분해 반응이 일어나서 광분해 효율이 저하되는 현상을 방지할 수 있으며 광분해성 캡슐이 토양에 잔류하지 않게 할 수 있다.  The agglomerates of the inorganic fine particles are uniformly dispersed in the binder resin while having a small particle size, so that photodegradation reaction is locally caused when the photodegradable capsules are exposed to light, thereby preventing degradation of photodecomposition efficiency So that the photodegradable capsules do not remain in the soil.
이는또한상기 무기 미세 입자의 응집체의 표면 또는내부에 상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종이상의 반복단위를포함한(공)중합체가결합됨에 따른것일수있다. 즉, 상기 (공)중합체가 상기 무기 미세 입자의 응집체 표면 또는 내부에 결합됨에 따라서 상기 무기 미세 입자의 응집체의 성장을조절할수 있으며, 또한상기 (공)중합체의 특성상상기 바인더 수지와높은상용성을 가지게 되어 상기 광촉매 복합체가상기 바인더 수지에 균일하게 분포할수 있게 한다.  This may be due to the incorporation of a (co) polymer containing one or more repeating units selected from the group consisting of ethylene repeating units and vinyl acetate repeating units on the surface or inside of the aggregate of the inorganic fine particles. That is, as the (co) polymer is bonded to the surface or inside of the agglomerate of the inorganic fine particles, the growth of agglomerates of the inorganic fine grains can be controlled, and the compatibility of the inorganic fine particles with the binder resin So that the photocatalytic composite can be uniformly distributed in the binder resin.
상술한바와 같이, 상기 용줄 제어형 비료는우수한광분해 효율을 구현할 수 있다. 보다 구체적으로, 30011111 내지 800™의 파장의 빛을 400 의 강도로 224시간동안밫을조사시 상기 광분해성 캡슐의 무게 변화로 도출되는 상기 바인더 수지의 분해율이 40%이상,또는 50%이상일 수 있다. 상기 무기 미세 입자는 광촉매 역할을 할 수 있다.상기 구현예의 용줄제어형 비료는 광분해성 캡슐이 토양에 잔류하는 문제를 해결하기 위하여 상기 바인더 수지에 상기 광촉매 복합체을 균일하게 분산하는 것을 5 특징으로 한다.상기 광촉매 복합체는 빛을 받는 동안에만촉매로 작용하게 되므로 빛이 차단되는 토양 내에서 비료가 방출되는 동안에는 광분해성 캡슐이 분해되지 않은 상태에서 용줄 기간 동안 서서히 비료를 방줄하게 된다.그리고,비료가 용출된 후 상기 용출 제어형 비료가 밭갈음 등으로 표토에 노출되면 빛에 의하여 상기 광분해성 캡슐이 분해될 수 있다. As described above, the lanyard-controlled fertilizer can realize excellent photodegradation efficiency. More specifically, when light of a wavelength of 300 11111 to 800 is irradiated at a strength of 400 for 224 hours, the weight of the photodegradable capsule The decomposition ratio of the binder resin to be derived may be 40% or more, or 50% or more. The inorganic fine particles may serve as a photocatalyst. The lance-controlled fertilizer of the embodiment is characterized in that the photocatalytic composite is uniformly dispersed in the binder resin in order to solve the problem that the photodegradable capsule remains in the soil. Since the photocatalytic complex acts as a catalyst only during the light receiving period, the photocatalytic capsule is slowly decomposed while the photocatalytic capsule is not decomposed while the fertilizer is released in the soil where the light is blocked. When the leaching control type fertilizer is exposed to the topsoil by plowing or the like, the photodegradable capsule may be decomposed by light.
10 상기 무기 미세 입자는 5 내지 50 nm의 단면 직경을 갖는 일차 입자를 포함할 수 있다.상기 무기 미세 입자의 일차 입자의 단면 직경은 통상적으로 알려진 방법, 예를 들어 TEM사진을 통한 확인이나, BET측정 등을통하여 확인할수 있다. 10, the inorganic fine particle may comprise primary particles having a cross-sectional diameter of 5 to 50 nm. Cross-sectional diameter of the primary particles of said inorganic fine particles are conventionally known method, for example, verification by the TEM image and, BET Measurement and so on.
상기 무기 미세 입자에 포함되는 일차 입자의 단면 직경이 너무 15 작으면, 결정화도가 떨어져서 광촉매 효율이 저하될 수 있다.또한, 상기 무기 미세 입자에 포함되는 일차 입자의 단면 직경이 너무 크면, 광촉매 입자의 비표면적이 낮아져서 광촉매 효율이 저하될 수 있다. If the cross-sectional diameter of the primary particles is too 15 less contained in the inorganic fine particle, the degree of crystallization can be the photocatalytic efficiency is lowered away. Further, the cross-sectional diameter of the primary particles is too large, the photocatalytic particles contained in the inorganic fine particle The specific surface area is lowered and the photocatalytic efficiency may be lowered.
한편, 상기 구현예의 용출 제어형 비료에 포함되는 상기 무기 미세 입자의 응집체가 그리 크지 않은 입경을 가질 수 있는데, 구체적으로 상기
Figure imgf000006_0001
On the other hand, the agglomerates of the inorganic fine particles contained in the dissolution-controlled fertilizer of the above embodiment may have a particle size not so large. Specifically,
Figure imgf000006_0001
의 단면 직경을 가질 수 있다.상기 무기 미세 입자의 응집체의 단면 직경 또한 직경은 통상적으로 알려진 방법, 예를 들어 SEM 또는 TEM microtome을통하여 확인할수 있다. The cross-sectional diameter and the diameter of the agglomerate of the inorganic fine particles can be confirmed by a commonly known method, for example, SEM or TEM microtome.
상기 무기 미세 입자의 응집체의 단면 직경 또는 전체적인 크기가 25 너무 커지면,상기 광분해성 캡슐에서 국지적인 광분해 반응이 일어나거나 또는 광분해 반응의 효율이 저하될 수 있고,비효율적인 광분해 반응으로 인하여 광분해성 캡슐 전체가분해되지 않고 잔류물이 남게 될 수 있다. The cross-sectional diameter or overall size of the aggregates of the inorganic fine particles 25 is too large, there is a localized photolytic reaction in the photodegradable capsule can be up or decrease the efficiency of photolysis reaction, due to the inefficient photolysis reaction entire photodegradable capsule It may not be decomposed and residues may remain.
상기 무기 미세 입자의 구체적인 예로는 이산화티탄(Ti02), 산화아연(ZnO),또는 이들의 혼합물을들수 있다. Specific examples of the inorganic fine particles include titanium dioxide ( TiO2), zinc oxide ( ZnO), and mixtures thereof.
30 \¥0 2019/117650 1»<그171012018/015866 30 \ ¥ 0 2019/117650 1 »<171012018/015866
한편, 상기 바인더 수지는 상기 광분해성 캡슐의 외부 구조를 형성하는 주된 재료일 수 있으며, 상술한 바와 같이 상기 바인더 수지는 폴리올레핀및에틸렌비닐아세테이트공중합체를포함할수있다. Meanwhile, the binder resin may be a main material forming the outer structure of the photodegradable capsule, and as described above, the binder resin may include a polyolefin and an ethylene vinyl acetate copolymer.
상기 폴리올레핀의 예가 크게 한정되는 것은 아니나, 예를 들어 고밀도 또는 저밀도 폴리에틸렌, 선형 저밀도 폴리에틸렌, 폴리프로필렌, 에틸렌-프로필렌 공중합체, 폴리부텐, 부텐-에틸렌 공중합체, 부텐_ 프로필렌 공중합, 이들의 2종 이상의 혼합물 또는 이들의 2종 이상의 공중합체를포함할수있다.  Examples of the polyolefin include, but are not limited to, high density or low density polyethylene, linear low density polyethylene, polypropylene, ethylene-propylene copolymer, polybutene, butene-ethylene copolymer, butene- Mixtures thereof, or copolymers of two or more thereof.
상기 바인더 수지에 포함되는 에틸렌비닐아세테이트 공중합체 또한 크게 한정되는 것은 아니나, 예를 들어 비닐아세테이트 반복 단위 1중량% 내지 45중량%를포함하는에틸렌비닐아세테이트공중합체를사용할수 있다. 또한, 상기 에틸렌비닐아세테이트 공중합체는쇼 ¾1 1)1238에 의하여 190 및 2.161¾하중에서 측정한 용융 지수가 0.5 은/101 11 내지 5.0 요/10 11, 또는 1.0용/101 11내지 3.0 §/101 11일수있다. The ethylene vinyl acetate copolymer contained in the binder resin is not particularly limited. For example, an ethylene vinyl acetate copolymer containing 1 to 45% by weight of vinyl acetate repeating units may be used. The ethylene vinyl acetate copolymer has a melt index of 0.5 / 10 11 to 5.0 / 10 11 or 1.0 / 10 11 to 3.0 § measured at 190 and 2.161 하 load, / 10 1 can be 11 days.
상기 바인더 수지에 포함되는 폴리올레핀 및 에틸렌비닐아세테이트 공중합체 간의 중량비가 크게 한정되는 것은 아니나, 예를 들어 상기 바인더 수지는폴리올레핀 : 에틸렌비닐아세테이트공중합체를 1 : 1내지 6 : 1 의 중량비로 포함할 수 있다. 상기와 같이 상기 바인더 수지가 폴리올레핀 수지를에틸렌비닐아세테이트공중합체와동등하거나보다많이 포함함에 따라서, 비료의 용출속도를보다용이하게조절할수있다. 한편, 상기 광촉매 복합체는 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체가무기 미세 입자의 응집체의 표면 또는 내부에 결합된 구조를 가질수있다.  Although the weight ratio between the polyolefin and the ethylene vinyl acetate copolymer contained in the binder resin is not particularly limited, for example, the binder resin may include a polyolefin: ethylene vinyl acetate copolymer in a weight ratio of 1: 1 to 6: 1 have. As described above, the dissolution rate of the fertilizer can be more easily controlled as the binder resin contains the polyolefin resin equal to or more than the ethylene vinyl acetate copolymer. On the other hand, the photocatalytic composite may have a structure in which a (co) polymer containing at least one repeating unit selected from the group consisting of ethylene repeating units and vinyl acetate repeating units is bonded to the surface or inside of aggregates of inorganic fine particles.
상술한바와같이 , 상기 무기 미세 입자의 응집체는 광촉매 역할을 할 수 있으며, 상기 용출 제어형 비료가 토양의 표면 등으로 노출되면 광분해성 캡슐에서 광분해 반응을시작될수있게 한다.  As described above, the agglomerate of the inorganic fine particles can act as a photocatalyst, and when the dissolution-controlled fertilizer is exposed to the surface of the soil or the like, the photolytic reaction can be started in the photodegradable capsule.
상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체는 상기 무기 2019/117650 1»(:1^1{2018/015866 The (co) polymer containing at least one repeating unit selected from the group consisting of the ethylene repeating unit and the vinyl acetate repeating unit is preferably a 2019/117650 1 » (: 1 ^ 1 {2018/015866
미세 입자의 응집체의 표면 또는내부에 결합되는데, 이에 따라상기 무기 미세 입자의 응집체가 크기가 과도하게 성장하는 것을 방지하며 상기 바인더 수지와보다높은상용성을가지게 하여 상기 광촉매 복합체가상기 바인더 수지에 균일하게분포하게 한다. The inorganic fine particles are prevented from excessively growing in size and have higher compatibility with the binder resin so that the photocatalytic composite is uniformly dispersed in the binder resin, .
5 상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체는 에틸렌 반복 단위 비닐아세테이트반복단위 또는이들모두를포함할수 있다. 상기 상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체의 구체적인 예로는 10 에틸렌비닐아세테이트 공중합체를 들 수 있고, 또한 비닐아세테이트 반복 단위 1중량% 내지 45중량%를 포함하는 에틸렌비닐아세테이트 공중합체를 사용할 수도 있다. 또한 상기 에틸렌비닐아세테이트 공중합체는 쇼況 1)1238에 의하여 1901: 및 2.16}¾하중에서 측정한용융지수가 0.5용/10 내지 5.0용/10 1, 또는 1.0용/101 11내지 3.0당/10 ^ 일수있다. 5, including the ethylene repeating units and vinyl acetate repeating units one or more kinds selected from the group consisting of repeating units of the (co) polymer can contain both an ethylene vinyl acetate repeating units, or repeating units thereof. Examples of the above ethylene repeating units and vinyl acetate (co) including a repeating unit selected at least one from the group consisting of repeating units of the polymer is 10 and the number of the ethylene vinyl acetate copolymers, and vinyl acetate repeating units from 1% to by weight 45 may be used an ethylene-vinyl acetate copolymer containing by weight%. In addition, the ethylene-vinyl acetate copolymer shows況1) on by 1901 1238: and 2.16} ¾ load a melt index of 0.5 for a / 10 to 5.0 for a / 10 1 or / 101 11 - / 10 per 3.0 1.0 measured at ^ Can be.
15  15
상기 광촉매 복합체는 상기 무기 미세 입자와 상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체를 유기 용매에 분산하는 단계를 통하여 제조될 수 있다. The photocatalyst composite may be prepared through the step of dispersing (co) polymer containing a repeating unit at least one selected from the group consisting of the inorganic fine particles and the ethylene repeating units and vinyl acetate repeating units in the organic solvent.
20 상기 광촉매 복합체에서 상기 무기 미세 입자의 응집체와 상기 20. The photocatalytic composite of claim 1,
(공)중합체의 중량비가 크게 한정되는 것은 아니며, 상기 용출제어형 비료의 특성에 따라서 상기 유기 용매에 분산하는 양을 조절하여 상기 중량비 등도 조절 가능하다.예를 들어, 상기 광촉매 복합체는 상기 무기 미세 입자의 응집체 100중량부 대비 상기 에틸렌 반복 단위 및 25 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체 1내지 500중량부 또는 20 내지 200중량부를 포함할수 있다. 한편, 상기 바인더 수지 100중량부 대비 상기 무기 미세 입자의 30 응집체 0.1내지 8중량부를포함할수 있다. 2019/117650 1»(:1^1{2018/015866 The weight ratio of the inorganic fine particles (co) polymer is not limited to a great extent, and the weight ratio can be controlled by controlling the amount of the organic fine particles dispersed in the organic solvent according to the characteristics of the dissolution control type fertilizer. It can be contained in 100 parts by weight of the aggregate compared to the ethylene repeating units and 25 vinyl (co) polymer, from 1 to 500 parts by weight of a repeating unit including at least one selected from the group consisting of acetate repeating units, or from 20 to 200 parts by weight. On the other hand, 0.1 to 8 parts by weight of 30 aggregates of the inorganic fine particles may be included relative to 100 parts by weight of the binder resin. 2019/117650 1 » (: 1 ^ 1 {2018/015866
상기 광분해성 캡슐에서 상기 바인더 수지 대비 무기 미세 입자의 응집체의 함량이 너무 낮으면 광분해 반응의 효율이 저하될 수 있으며, 충분하지 않은 광분해 반응으로 인하여 광분해성 캡슐 전체가 분해되지 않고 잔류물이 남게 될 수 있다. 또한, 상기 광분해성 캡슐에서 상기 5 바인더 수지 대비 무기 미세 입자의 응집체의 함량이 너무 크면, 상기 무기 미세 입자의 응집체가 크게 성장할 수 있고, 이에 따라 상기 광분해성 캡슐에서 국지적인 광분해 반응이 일어나거나 또는 광분해 반응의 효율이 저하되어 광분해성 캡슐 전체가분해되지 않고 잔류물이 남게 될 수 있다. If the content of the aggregate of the inorganic fine particles relative to the binder resin in the photodegradable capsule is too low, the photolysis reaction efficiency may be lowered, and the entire photodegradable capsule may not be decomposed due to insufficient photolysis reaction, . Also, in the photodegradable capsule, if the content of the aggregate of the inorganic fine particles relative to the 5-binder resin is too large, the agglomerate of the inorganic fine particles may grow to a large extent, thereby causing a local photodegradation reaction in the photodegradable capsule, The efficiency of the photolysis reaction is lowered, so that the entire photodegradable capsule is not decomposed and the residue may remain.
10 한편, 상기 용출제어형 비료는 상기 바인더 수지에 분산되는 필러를 더 포함할 수 있다.상기 필러의 종류가 크게 한정되는 것은 아니나, 예를 들어 상기 필러는 탈크, 벤토나이트, 황토, 규조토, 실리카 알루미노실리케이트, 카올라이트, 전분, 카본, 또는 이들의 2종 이상의 혼합물을들수 있다. 10 On the other hand, the release-controlled fertilizer may further comprise a filler to be dispersed in the binder resin but are not the kind of the filler largely limited, and for example the filler is talc, bentonite, yellow earth, diatomaceous earth, silica-alumina Silicate, kaolite, starch, carbon, or a mixture of two or more thereof.
15 상기 필러의 함량이 크게 한정되는 것은 아니나, 상기 광분해성 캡슐의 기계적 물성이나 구조적 안정성을 고려하여 상기 용줄제어형 비료는 상기 광분해성 캡슐 전체 중량 대비 상기 필러 25내지 75중량%를 포함할 수 있다 15 The content of the filler is not limited, but the lumber-controlling type fertilizer may contain 25 to 75 % by weight of the filler in relation to the total weight of the photodegradable capsule in consideration of the mechanical properties and structural stability of the photodegradable capsule
20 상기 비료는 다양한 공지의 비료, 예를 들어 요소 또는 복합비료일 수 있다. 바람직한 양태에서 상기 비료는 광분해성 캡슐 내에 포함되기 용이하기 위하여, 입상 형태를 갖는 입상코어 비료일 수 있다. 20 The fertilizer may be any of a variety of known fertilizers, such as urea or compound fertilizer. In a preferred embodiment, the fertilizer may be a granular core fertilizer having a granular form in order to be easily contained in the photodegradable capsule.
상기 비료의 구체적인 종류가 한정되지 않으며, 통상적으로 공지된 비료를 사용할 수 있다. 바람직한 예는 요소(尿素), 알데히드축합 요소 The specific kind of the above-mentioned fertilizer is not limited, and conventionally known fertilizers can be used. Preferred examples are urea, aldehyde condensation element
25 이소부틸알데히드축합 요소, 포름알데히드축합 요소 구아닐우레아 술페이트, 및 옥사미드와 같은 질소함유 유기화합물, 질산암모늄, 인산이수소암모늄, 인산수소이암모늄, 황산암모늄 염화암모늄, 및 질산나트륨과 같은 암모늄 및 질산 화합물, 질산칼륨 인산칼륨, 황산칼륨, 및 염화칼륨과 같은 칼륨염, 인산칼슘 황산칼슘 질산칼슘, 및 염화칼슘과 25 isobutylaldehyde condensation element, formaldehyde condensation element guanyl ureasulfate, and nitrogen containing organic compounds such as oxamide, ammonium nitrate, ammonium dihydrogenphosphate, ammonium dihydrogenphosphate, ammonium sulfate ammonium chloride, and ammonium nitrate such as sodium nitrate And potassium salts such as potassium nitrate, potassium nitrate, potassium phosphate, potassium sulfate, and potassium chloride, calcium phosphate, calcium sulfate, calcium nitrate,
30 같은 칼슘염, 질산마그네슘 염화마그네슘 인산마그네슘 및 황산마그네슘과 같은 마그네슘염 , 질산제일철, 질산제이철, 인산제일철, 인산제이철, 황산제일철, 황산제이철, 염화제일철, 및 염화제이철과 같은 철염, 및 이들의 이중염,또는이들의 2이상의혼합물이다. 30 calcium salts, magnesium nitrate, magnesium chloride, magnesium phosphate, and Iron salts such as ferric chloride, ferric nitrate, ferric phosphate, ferric phosphate, ferrous sulfate, ferric sulfate, ferrous chloride and ferric chloride, and their double salts or a mixture of two or more thereof.
상기 용출제어형 비료에서 비료의 함량이 크게 한정되는 것은 아니며, 예를들어 상기 광분해성 캡슐 100중량부대비 상기 비료 200내지 3000중량부를포함할수있다. 상기 광촉매복합체는상기 광분해성 캡슐에서 특유의 분산도를가질 수 있다. 보다구체적으로, 상기 광촉매 복합체는 상기 무기 미세 입자와 상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종이상의 반복단위를포함한(공)중합체를유기 용매에 분산하는 단계를통하여 제조될수있는데,  The content of the fertilizer in the leaching control type fertilizer is not limited to a great extent. For example, 100 parts by weight of the photodegradable capsule may contain 200 to 3000 parts by weight of the fertilizer. The photocatalytic composite may have a specific degree of dispersion in the photodegradable capsule. More specifically, the photocatalytic composite can be produced by dispersing (co) polymer containing the inorganic fine particles and one or more repeating units selected from the group consisting of ethylene repeating units and vinyl acetate repeating units in an organic solvent ,
상기 무기 미세 입자와 (공)중합체를 유기 용매에 분산한상태에서 초음파, 고전단 믹서(High-Shear Mixer) 또는 비드 밀(Bead mi l l) 등을 아용하여 강한 에너지를 전달함으로서, 상기 (공)중합체가 무기 미세 입자의 응집체의 표면 또는 내부에 결합될 수 있다. 이와 같이 제조된 광촉매 복합체는 상기 바인더 수지에 아주 균일하게 분산될 수 있으며, 이에 따라광촉매의 분해효율이 현저하게 증가될수있다.  A high-shear mixer or a bead mill may be used to disperse the inorganic fine particles and the (co) polymer in an organic solvent to transfer strong energy to the (co) polymer May be bonded to the surface or inside of the aggregate of the inorganic fine particles. The photocatalytic composite thus produced can be dispersed very uniformly in the binder resin, and the decomposition efficiency of the photocatalyst can be remarkably increased.
상기 용줄제어형 비료는공지의 용줄제어형 비료에 포함되는성분을 추가적으로 더 포함할 수 있다. 예를 들어, 이러한 성분은 양친매성 고분자등이 있으나이에 제한되는것은아니다. 한편, 상기 용출 제어형 비료는 다양한 제조 방법을 통해서 제공 가능하며, 예를 들어 에틸렌비닐아세테이트 공중합체가 첨가된 유기용매에 무기 미세 입자를분산시켜 상기 광촉매 복합체의 분산액을제조하는단계; 폴리올레핀, 에틸렌비닐아세테이트공중합체, 상기 광촉매 복합체의 분산액 및 선택적으로 필러를 혼합하여 코팅 조성물을 제조하는 단계; 및 상기 코팅 조성물로 입상 비료 코어의 표면을 피복하는 단계;를 포함하는 제조 방법을통하여 제공할수있다.  The lanyard-controlled fertilizer may further comprise a component included in a known line-controlled fertilizer. For example, such components include, but are not limited to, amphipathic polymers. The leaching control type fertilizer can be provided through various manufacturing methods. For example, the dispersion of inorganic fine particles is dispersed in an organic solvent to which an ethylene vinyl acetate copolymer is added to prepare a dispersion of the photocatalytic composite. Preparing a coating composition by mixing a polyolefin, an ethylene vinyl acetate copolymer, a dispersion of the photocatalytic composite, and optionally a filler; And coating the surface of the granular fertilizer core with the coating composition.
상기 유기 용매의 구체적인 예가 한정되는 것은 아니나, 2019/117650 1»(:1^1{2018/015866 Although specific examples of the organic solvent are not limited, 2019/117650 1 » (: 1 ^ 1 {2018/015866
테트라클로로에틸렌 0€ , 사이클로핵센((:■), 다이클로로메탄 0X1), 또는 1,2 ,4 -트리클로로벤젠 01¾)등을사용할수있다. Tetrachlorethylene 0, cyclone nucleus ((:), dichloromethane 0X1), or 1,2,4 - trichlorobenzene 01 ¾ ).
상기 에틸렌비닐아세테이트 공중합체가 첨가된 유기용매에 무기 미세 입자를분산시켜 상기 광촉매 복합체의 분산액을제조하는단계에서는 5 초음파( 11比 1011) 또는 비드 밀 등과 같은 강한 에너지를 사용하여 분산액을제조할수 있으며 , 예를들어 초음파(301131;1이1)등과같은강한
Figure imgf000011_0001
In the step of dispersing the inorganic fine particles in the organic solvent to which the ethylene vinyl acetate copolymer is added to prepare the dispersion of the photocatalytic composite, a dispersion can be prepared by using a strong energy such as a 5-ultrasonic wave ( 11 ratio 1 011 ) or a bead mill For example, ultrasonic waves ( 3011 ratio 31 ; 1 is 1 ), etc.
Figure imgf000011_0001
갖는분산액을제조할수있다.  Can be prepared.
【발명의 효과】  【Effects of the Invention】
10 본 발명에 따르면 수분에 대한 높은 안정성과 견고한 구조를 가지며 비료의 용출 기간을 용이하게 조절할수 있고 아울러 우수한광분해 효율을구현할수 있는용출제어형 비료가제공될 수 있다. 10 According to the present invention, it is possible to provide a controlled-release fertilizer having a high stability against moisture, a solid structure, and a controllability of a dissolution period of the fertilizer and an excellent photodegradation efficiency.
상기 용출 제어형 비료는 광분해성 캡슐 또는 친수성 고분자 등이 토양에 잔류하지 않게 하여 토양오염 등을방지할수 있다.  The dissolution-controlled fertilizer prevents the photodegradable capsule or the hydrophilic polymer from remaining in the soil, thereby preventing soil contamination.
15 【도면의 간단한설명】 15 [Brief Description of Drawings]
1은 실시예 1와 용출 제어형 비료에 포함된 광촉매 복합체에서 무기 미세 입자의 응집체와 비교예2의 피복 비료에 포함된 미세 입자의 응집체 각각의 표 사진이다. Fig. 1 is a table photograph of each of the agglomerates of inorganic fine particles and the agglomerates of fine particles contained in the coated fertilizer of Comparative Example 2 in Example 1 and the photocatalytic composite contained in the dissolution-controlled fertilizer.
2은 용출제어형 비료의 광분해 메커니즘을 개략적으로 나타낸Figure 2 schematically depicts the photodegradation mechanism of a dissolution-controlled fertilizer
20 것이다. 20 .
【발명을실시하기 위한구체적인내용】  DETAILED DESCRIPTION OF THE INVENTION
발명을 하기의 실시예에서 보다 상세하게 설명한다. 단, 하기의 실시예는본발명을 예시하는 것일 뿐, 본 발명의 내용이 하기의 실시예에 의하여 한정되는것은아니다.  The invention will be described in more detail in the following examples. However, the following examples are illustrative of the present invention, and the present invention is not limited by the following examples.
25  25
[실시예 : 용출제어형 비료의 제조]  [Example: Preparation of dissolution-controlled fertilizer]
실시예 1내지 3  Examples 1 to 3
1)광촉매복합체의 제조 ( 1 ) Production of photocatalytic composite
에틸렌비닐아세테이트 공중합체 [¾0(용융지수, 1901: , 2.161¾하중, 2019/117650 1»(:1^1{2018/015866
Figure imgf000012_0001
Ethylene Vinyl Acetate Copolymer [ū 0 (Melt Index, 1901: 2.161 ¾ load, 2019/117650 1 » (: 1 ^ 1 {2018/015866
Figure imgf000012_0001
초음파를가하여 에틸렌비닐아세테이트공중합체가코팅된 광촉매 복합체의 5 분산액을제조하였다.  Ultrasonic waves were applied to prepare 5 dispersions of the photocatalytic composite coated with ethylene vinyl acetate copolymer.
(2)용출제어형 비료의 제조  (2) Production of dissolution-controlled fertilizer
상기 제조된 광촉매 복합체의 분산액, 폴리에틸렌比^¾, (용융지수, 190 , 2.161¾하중, 쇼況 1)1238) : 약 8 §/10111111, 1)(밀도) : 0.925용/011 3], 에틸렌비닐아세테이트 공중합체 [ (용융지수, 19010 ,Dispersion of the above-prepared photocatalyst composite, polyethylene比^ ¾, (melt index, 190, 2.161 ¾ load, shows況1) 1238): about 8 § / 10111111, 1) (density): 0.925 / 0 11 3] for, Ethylene vinyl acetate copolymer [(Melt Index, 19010,
10 2.161¾하중, 쇼況 1)1238) : 약 1.8 용/10 미 , 1)(밀도) : 0.94융/刷3, 비닐아세테이트함량 약 20중량%, 녹는점 85°0] , 및 탈크를하기 표 1에 따른함량으로 사용하여 조성와혼합비로 테트라클로로에틸렌과 1001:에서 균일하게 교반 혼합하고 고형분 농도가 5 중량%가 되도록 코팅액을 제조하였다. To 0.94 Melting /刷3, about 20% by weight vinyl acetate content, a melting point 85 ° 0], and talc: 10 2.161 ¾ load, shows況1) 1238): about 1.8 / 10 mi, 1) for the (density) Using the contents as shown in Table 1, the mixture was homogeneously mixed with tetrachlorethylene at a mixing ratio of 100: 1 in terms of composition and mixing ratio to prepare a coating solution having a solid concentration of 5% by weight.
15 그리고, 유동층 건조기를사용하여 질소 비료 입자에 상기 코팅액을 도포하여 용출제어형 피복비료(실시예 1내지 5)를제조하였다. 15 Then, the coating solution was applied to the nitrogen fertilizer particles using a fluidized bed dryer to prepare dissolution-controlled coated fertilizers (Examples 1 to 5 ).
[비교예 1및 2:피복비료의 제조] [Comparative Examples 1 and 2: Preparation of coated fertilizer]
비교예 1  Comparative Example 1
20 폴리에틸렌比^¾, (용융지수, 1901:, 2.161¾하중, 쇼況¾1 1)1238) : 약 8 용/101 11, IX밀도) : 0.925요/011 3] , 에틸렌비닐아세테이트 공중합체 [ (용융지수, 190 , 2.16용하중, 요況¾1 1)1238) : 약 1.8 은/ !, 20 polyethylene比^ ¾, (melt index, 1901 :, 2.161 ¾ load, shows況¾1 1) 1238): about 8/10 1 11, IX for density): 0.925 I / 0 11 3], ethylene vinyl acetate copolymer [(Melt index, 190, 2.16, 1) 1238): about 1.8 is /!,
1)(밀도) : 0.94§八: , 비닐아세테이트 함량 약 20 중량%, 녹는점 85ᅤ], 및 탈크를 하기 표 1에 따른 함량으로 사용하여 조성의 혼합비로 25 테트라클로로에틸렌과 100°(:에서 균일하게 교반혼합하고 고형분 농도가 5 중량%가되도록코팅액을제조하였다. 1) (density): 0.94 §八:, vinyl acetate content about 20 wt%, a melting point of 85 yae], and to the talc by using a content according to Table 1 25 tetrachlorethylene and 100 ° to the mixing ratio of composition (: , And a coating solution was prepared so that the solid content concentration became 5% by weight.
그리고, 유동층 건조기를 사용하여 질소 비료 입자에 상기 코팅액을 도포하여 피복비료(비교예1)를 제조하였다. Then, the coating liquid was applied to the nitrogen fertilizer particles using a fluidized bed dryer to prepare coated fertilizer (Comparative Example 1 ).
30 비교예 2 2019/117650 1»(:1^1{2018/015866 02(일차입자의 평균입경: 21■), 폴리에틸렌比卵民
Figure imgf000013_0001
(용융지수, 190 °0 , 2. 16뇨은하중, 쇼況¾1 1)1238) : 약 8 용/1001 , 1)(밀도) : 0.925당八 ], 에틸렌비닐아세테이트 공중합체 1(용융지수, 1901〕, 2. 161¾하중, 쇼況 1)1238) : 약 1.8요/101 11 , I)(밀도) : 0.94§/011 3) 비닐아세테이트 함량 약 20중량%, 녹는점 85°0], 및 탈크를하기 표 1에 따른함량으로사용하여 조성의 혼합비로 테트라클로로에틸렌과 1001:에서 균일하게 교반 혼합하고 고형분농도가 5중량%가되도록코팅액을제조하였다.
30 Comparative Example 2 (Average particle diameter of primary particles: 21 ■) of 2019/117650 1 (: 1 ^ {2018/015866 0 2 ), polyethylene
Figure imgf000013_0001
(Density): 0.925 dl), Ethylene Vinyl Acetate Copolymer 1 (Melt Index, Melt Index, Melt Index, 190 ° 0, 1901], 2. 161¾ load, shows況1) 1238): about 1.8 I / 10 1 11, I) (density): 0.94 § / 011 3) about 20% by weight vinyl acetate content, a melting point 85 ° 0], And talc were mixed with tetrachlorethylene at a mixing ratio of 100: 1 at a mixing ratio of 100: 1 by using the ingredients as shown in Table 1, and a coating liquid was prepared so that the solid concentration was 5% by weight.
그리고, 유동층건조기를사용하여 질소비료 입자에 상기 코팅액을 도포하여 피복비료(비교예 1)를제조하였다.  Then, the coating liquid was applied to the nitrogen fertilizer particles using a fluidized bed dryer to prepare coated fertilizer (Comparative Example 1).
[실험예] [Experimental Example]
실험예 1: 광분해특성 비교시험 Experimental Example 1: Comparison test of photodegradation characteristics
Figure imgf000013_0002
Figure imgf000013_0002
취하여 한 알씩 바늘로 핀홀을 낸 후 내부 비료를 완전히 용출한후 남은 피복막으로분해평가를진행하였다. After taking out the pinholes with one needle each, the internal fertilizer was completely eluted and the degradation evaluation was carried out with the remaining coating film.
Figure imgf000013_0003
장비를이용하여 50ᅤ의 온도에서 300™내지
Figure imgf000013_0003
Equipment at temperatures of 50 ° C to 300 ° C
8001패의 파장의 빛을 40(½/111 2의 강도로상기 피복막에 조사하였다. The coating film was irradiated with light having a wavelength of 800 1 L at an intensity of 40 (½ / 111 2 ).
그리고, 상기 조건으로 224시간동안 빛을 조사 시 상기 피복막의 무게 변화로도줄되는 바인더 수지의 분해율을 하기 일반식 1로구하고, 그 결과를표 1에 나타내었다.  The degradation rate of the binder resin, which is also reduced by the weight change of the coating film upon irradiation with light for 224 hours under the above conditions, was determined by the following general formula 1, and the results are shown in Table 1 below.
[일반식 1]  [Formula 1]
바인더수지의분해쿨  Cool down the binder resin
X: 100엿
Figure imgf000013_0004
X: 100 candles
Figure imgf000013_0004
【표 1]
Figure imgf000013_0005
2019/117650 1»(:1^1{2018/015866
Figure imgf000014_0002
상기 표 1에 나타난바와같이, 실시예의 용출제어형 비료에 대하여 300·내지 800™의 파장의 빛을 400 / 의 강도로 224시간동안빛을조사 시 바인더 수지의 분해율이 40%이상, 또는 55%이상이라는점이 확인되며, 이에 반하여 비교예의 피복 비료는 35%이하의 바인더 수지의 분해율을 나타낸다는점이 확인되었다. 실험예 2: 비료용출특성평가
[Table 1]
Figure imgf000013_0005
2019/117650 1 » (: 1 ^ 1 {2018/015866
Figure imgf000014_0002
Wherein, as shown in Table 1, the embodiment of dissolution-controlled fertilizer to about 300, to the light having a wavelength of 800 ™ to a 400 / strength than the 40% decomposition of the binder resin when irradiated with light for 224 hours, and 55% , Whereas the coated fertilizer of the comparative example showed a decomposition rate of the binder resin of 35% or less. EXPERIMENTAL EXAMPLE 2 Evaluation of Dissolution Characteristics of Fertilizer
상기 실시예의 용출 제어형 비료 및 비교예의 피복 비료 각각
Figure imgf000014_0001
The release-controlled fertilizer of the above-mentioned example and the coated fertilizer of the comparative example
Figure imgf000014_0001
【표 2]
Figure imgf000014_0003
상기 표2에 나타난 바와 같이, 실시예의 용출 제어형 비료는 20일 이후에 50%이상의 용출율을 나타내며 50일 이후에는 90%이상의 용출율을 나타낸다는 점이 확인되는데, 이에 반하여 비교예의 피복 비료는 20일이 지나도 40%이하의 용출율을 나타내며 50일의 시점에도 70%이하의 용출율을 나타낸다는 점이 확인되었다. 실험예 3: Ti어의 z-평균분산입도측정
[Table 2]
Figure imgf000014_0003
As shown in Table 2 , it was confirmed that the dissolution-controlled type fertilizer of the Example exhibited a dissolution rate of 50% or more after 20 days and showed a dissolution rate of 90% or more after 50 days, whereas the coated fertilizer of Comparative Example showed that after 20 days It showed a dissolution rate of 40% or less and showed a dissolution rate of 70% or less even at 50 days. Experimental Example 3: Measurement of z-average dispersion particle size of Ti
실시예 1의 광촉매 복합체의 분산액과 비교예 2의 Ti¾가 포함된 분산액의 Ti02의 z-평균 분산 입도를 Dynamic Light Scattering (Marvern Zetasizer Nano ZS90)을 사용하여 측정하였다. 그 결과를 하기 표 3에 나타내었다. The z-average dispersion particle size of the TiO 2 of the dispersion containing the photocatalytic composite of Example 1 and the Ti¾ of Comparative Example 2 was measured using Dynamic Light Scatterin g (M arvern Ze tasizer Nano ZS 90 ). The results are shown in Table 3 below.
【표 3】 02 _평균분산입도
Figure imgf000015_0003
상기 표 2에 나타난 바와 같이 , 실시예 1의 광촉매 복합체의
Figure imgf000015_0001
[Table 3] 0 2 _ Average dispersed particle size
Figure imgf000015_0003
As shown in Table 2 , the photocatalytic composite of Example 1
Figure imgf000015_0001
균질하게 분산되어 상대적으로 작은 평균 입경을 갖는 무기 미세 입자의 응집체가 형성되었다는 점이 확인되고, 이는 況 ¾13(: , 3-4800)을 사용하여 실시예 1의 광촉매 복합체를 관찰한 도 1의 況 ¾伴 사진에서도 확인된다. It is dispersed homogeneously, and that the check point is relatively formed with a agglomerates of the inorganic fine particles having a small average particle diameter, which況¾1 control 3: the embodiment in Figure 1 observed in the photocatalytic composite 1 using (3-4800)況is confirmed by ¾伴photos.
이에 반하여, 비교예 2의 02가포함된 분산액의 02는 약 10,000 ^ 이상의 2 -평균 분산 입도를 가져서 상대적으로 큰 평균 입경을 갖는 무기 미세 입자의 응집체가 형성되었다는 점이 확인되며, 이는 비교예 2
Figure imgf000015_0002
On the other hand, Comparative Example 2 0 2 0 2 of the saturable also the dispersion is at least about 10,000 ^ 2 - is confirmed that that form aggregates of the inorganic fine particles having an average particle diameter of relatively large gajyeoseo the average dispersed particle size, which is the comparative example 2 of
Figure imgf000015_0002
확인된다.  Is confirmed.

Claims

2019/117650 1»(:1^1{2018/015866 2019/117650 1 » (: 1 ^ 1 {2018/015866
【청구범위】 Claims:
【청구항 1]  [Claim 1]
폴리올레핀 및 에틸렌비닐아세테이트 공중합체를 포함한 바인더 수지 및 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 5 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체가 무기 미세 입자의 응집체의 표면 또는 내부에 결합된 광촉매 복합체 를 포함하는 광분해성 캡슐과 A polyolefin, and (co) polymers, including ethylene vinyl acetate binder resin, and ethylene repeating units and vinyl acetate repeating unit repeating unit at least one selected from the 5 group consisting of containing a copolymer bonded to the surface or inside of the agglomerates of the inorganic fine particles Photodegradable capsules comprising a photocatalytic composite and
상기 광분해성 캡슐로 둘러싸인 공간에 포함된 비료를 포함하는, 용출제어형 비료.  And a fertilizer contained in a space surrounded by the photodegradable capsule.
1010
【청구항 2]  [Claim 2]
제 1항에 있어서,  The method according to claim 1,
300™ 내지 800·의 파장의 빛을 400 / 의 강도로 224시간동안 빛을 조사시 상기 광분해성 캡슐의 무게 변화로 도출되는 상기 바인더 15 수지의 분해율이 40%이상인, 용출제어형 비료. Wherein the decomposition rate of the binder 15 resin derived from the weight change of the photodegradable capsule is 40% or more upon irradiation with light having a wavelength of 300 to 800 占 at an intensity of 400/224 hours.
【청구항 3[Claim 3 ]
제 1항에 있어서,  The method according to claim 1,
상기 무기 미세 입자는 5 내지 50 11111의 단면 직경을 갖는 일차 20 입자를포함하는, 용출제어형 비료. Wherein said inorganic microparticles comprise primary 20 particles having a cross-sectional diameter of from 5 to 50 &lt; RTI ID = 0.0 &gt; 11111. &lt; / RTI &gt;
【청구항 4] [4]
제 1항에 있어서,  The method according to claim 1,
상기 무기 미세 입자의 응집체는 1 이하의 단면 직경을갖는, 용출 25 제어형 비료. The aggregate of the inorganic fine particles having the cross-sectional diameter of less than 1, the elution of 25-regulating fertilizer.
【청구항 5[Claim 5 ]
제 1항에 있어서,  The method according to claim 1,
상기 무기 미세 입자의 응집체는 0.05 m 내지 0.5 !!의 단면 30 직경을갖는, 용출제어형 비료. 2019/117650 1»(:1^1{2018/015866 Wherein the agglomerates of the inorganic fine particles have a cross section 30 diameter of from 0.05 m to 0.5 mu m. 2019/117650 1 »(: 1 ^ 1 {2018/015866
【청구항 6】 [Claim 6]
제 1항에 있어서,  The method according to claim 1,
상기 무기 미세 입자는 이산화티탄:( 02), 산화아연( ), 또는 이들의 혼합물인것인, 용출제어형 비료. Wherein the inorganic fine particles are titanium dioxide: (0 2 ), zinc oxide (), or a mixture thereof.
【청구항 7] [7]
제 1항에 있어서,  The method according to claim 1,
상기 광촉매 복합체는 상기 무기 미세 입자의 응집체 100중량부 대비 상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체 1 내지 500 중량부를포함하는, 용줄제어형 비료.  Wherein the photocatalytic composite comprises 1 to 500 parts by weight of a (co) polymer containing at least one repeating unit selected from the group consisting of ethylene repeating units and vinyl acetate repeating units, with respect to 100 parts by weight of aggregates of the inorganic fine particles. .
【청구항 8】 8.
제 1항에 있어서,  The method according to claim 1,
상기 바인더 수지 100중량부 대비 상기 무기 미세 입자의 응집체 0.1내지 8중량부를포함하는, 용출제어형 비료.  And 0.1 to 8 parts by weight of aggregates of inorganic fine particles relative to 100 parts by weight of the binder resin.
【청구항 9] 9]
제 1항에 있어서,  The method according to claim 1,
상기 바인더 수지 중 상기 폴리올레핀 : 에틸렌비닐아세테이트 공중합체의 중량비는 1 : 1내지 6 : 1인 것인, 용출제어형 비료.  Wherein the weight ratio of the polyolefin: ethylene vinyl acetate copolymer in the binder resin is 1: 1 to 6: 1.
【청구항 10】 Claim 10
제 1항에 있어서,  The method according to claim 1,
상기 폴리올레핀은 고밀도 또는 저밀도 폴리에틸렌, 선형 저밀도 폴리에틸렌, 폴리프로필렌, 에틸렌-프로필렌 공중합체, 폴리부텐, 부텐- 에틸렌 공중합체 및 부텐-프로필렌 공중합체로 이루어진 군으로부터 선택되는하나이상인, 용출제어형 비료. 2019/117650 1»(:1^1{2018/015866 Wherein the polyolefin is at least one selected from the group consisting of high density or low density polyethylene, linear low density polyethylene, polypropylene, ethylene-propylene copolymer, polybutene, butene-ethylene copolymer and butene-propylene copolymer. 2019/117650 1 » (: 1 ^ 1 {2018/015866
【청구항 11Claim 11
제항에 있어서  In the provision of
상기 에틸렌비닐아세테이트 공중합체는 비닐아세테이트 반복 단위 1중량%내지 45중량%를포함하는, 용출제어형 비료. Wherein said ethylene vinyl acetate copolymer comprises from 1 % to 45 % by weight of vinyl acetate repeat units.
55
【청구항 12Claim 12
제 1항에 있어서,  The method according to claim 1,
상기 에틸렌 반복 단위 및 비닐아세테이트 반복 단위로 이루어진 군에서 선택된 1종 이상의 반복 단위를 포함한 (공)중합체는 10 에틸렌비닐아세테이트공중합체를포함하는, 용줄제어형 비료. Wherein the (co) polymer comprising at least one repeating unit selected from the group consisting of ethylene repeat units and vinyl acetate repeat units comprises 10 ethylene vinyl acetate copolymers.
【청구항 13Claim 13
제 1항에 있어서,  The method according to claim 1,
상기 바인더 수지에 분산되는필러를더 포함하는, 용출제어형 비료. 15 And a filler dispersed in the binder resin. 15
【청구항 ½】  (Ii)
제 13항에 있어서,  14. The method of claim 13,
상기 필러는 탈크, 벤토나이트, 황토, 규조토, 실리카, 알루미노실리케이트, 카올라이트, 전분 및 카본으로 구성된 군에서 선택된 20 하나이상인것인, 용출제어형 비료. Wherein the filler is at least 20 selected from the group consisting of talc, bentonite, loess, diatomaceous earth, silica, aluminosilicate, kaolite, starch and carbon.
【청구항 15 15.
13항에 있어서, 14. The method of claim 13 ,
상가 광분해성 캡슐 전체 중량 대비 상기 필러 25 내지 75중량%를 25 포함하는, 용출제어형 비료. Photodegradable additive, based on the weight of the entire capsule, dissolution-controlled fertilizer to 25 containing the filler 25 to 75% by weight.
【청구항 16Claim 16
제 1항에 있어서, 상기 비료는입상의 비료인, 용출제어형 바료.  2. The leaching control type fertilizer according to claim 1, wherein the fertilizer is a granular fertilizer.
30 【청구항 17】 0 2019/117650 1>( /1 技018/015866 30 [Claim 17 ] 0 2019/117650 1> (/ 1 technique 018/015866
제 1항에 있어서, The method according to claim 1,
상기 광분해성 캡슐 100중량부 대비 상기 비료 200 내지 3000 중량부를포함하는, 용출제어형 비료.  And 200 to 3000 parts by weight of the above-mentioned fertilizer with respect to 100 parts by weight of the photodegradable capsule.
PCT/KR2018/015866 2017-12-14 2018-12-13 Controlled release fertilizer WO2019117650A1 (en)

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US16/646,681 US11427514B2 (en) 2017-12-14 2018-12-13 Controlled-release fertilizers
CN201880054387.5A CN111094214A (en) 2017-12-14 2018-12-13 Controlled release fertilizer
JP2020519767A JP7146331B2 (en) 2017-12-14 2018-12-13 Elution controlled fertilizer
AU2018385840A AU2018385840B2 (en) 2017-12-14 2018-12-13 Controlled-release fertilizers
PH12020550880A PH12020550880A1 (en) 2017-12-14 2020-06-11 Controlled-release fertilizers

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1143391A (en) * 1997-07-24 1999-02-16 Asahi Chem Ind Co Ltd Decomposable coated granular fertilizer and its production
KR20000071159A (en) * 1997-02-19 2000-11-25 야마모토 카즈모토 Granular fertilizer coated with decomposable coating film and process for producing the same
KR101179469B1 (en) * 2009-12-16 2012-09-07 동부팜한농 주식회사 Release-controlled coating fertilizer with bulk blending and preparation method thereof
KR101331454B1 (en) * 2013-08-07 2013-11-26 수산고분자 주식회사 Slow released fertilizer and preparation method thereof
KR20140039288A (en) * 2011-06-13 2014-04-01 인비스타 테크놀러지스 에스.에이 알.엘. Aliphatic polyester polyols from cyclohexane oxidation byproduct streams as precursors for polyurethane and polyisocyanurate polymers

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000071159A (en) * 1997-02-19 2000-11-25 야마모토 카즈모토 Granular fertilizer coated with decomposable coating film and process for producing the same
JPH1143391A (en) * 1997-07-24 1999-02-16 Asahi Chem Ind Co Ltd Decomposable coated granular fertilizer and its production
KR101179469B1 (en) * 2009-12-16 2012-09-07 동부팜한농 주식회사 Release-controlled coating fertilizer with bulk blending and preparation method thereof
KR20140039288A (en) * 2011-06-13 2014-04-01 인비스타 테크놀러지스 에스.에이 알.엘. Aliphatic polyester polyols from cyclohexane oxidation byproduct streams as precursors for polyurethane and polyisocyanurate polymers
KR101331454B1 (en) * 2013-08-07 2013-11-26 수산고분자 주식회사 Slow released fertilizer and preparation method thereof

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