WO2014189183A1 - 지효성을 갖는 매트릭스형 입상복합비료의 제조방법 및 이로부터 얻은 매트릭스형 입상복합비료 - Google Patents
지효성을 갖는 매트릭스형 입상복합비료의 제조방법 및 이로부터 얻은 매트릭스형 입상복합비료 Download PDFInfo
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- WO2014189183A1 WO2014189183A1 PCT/KR2013/009337 KR2013009337W WO2014189183A1 WO 2014189183 A1 WO2014189183 A1 WO 2014189183A1 KR 2013009337 W KR2013009337 W KR 2013009337W WO 2014189183 A1 WO2014189183 A1 WO 2014189183A1
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- Prior art keywords
- matrix
- fertilizer
- additive
- composite fertilizer
- granular composite
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C3/00—Fertilisers containing other salts of ammonia or ammonia itself, e.g. gas liquor
- C05C3/005—Post-treatment
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B7/00—Fertilisers based essentially on alkali or ammonium orthophosphates
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C9/00—Fertilisers containing urea or urea compounds
- C05C9/005—Post-treatment
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D1/00—Fertilisers containing potassium
- C05D1/005—Fertilisers containing potassium post-treatment
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F11/00—Other organic fertilisers
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES 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
- C05G5/00—Fertilisers characterised by their form
- C05G5/10—Solid or semi-solid fertilisers, e.g. powders
- C05G5/12—Granules or flakes
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES 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
- C05G5/00—Fertilisers characterised by their form
- C05G5/40—Fertilisers incorporated into a matrix
Definitions
- the present invention relates to a method for producing a matrix granular composite fertilizer having a sustained effect of increasing the utilization of fertilizers and to a matrix granular composite fertilizer obtained therefrom, and more specifically, to improve the utilization of fertilizer nutrient crops, Unlike the conventional coating type, this method is designed to minimize the loss of fertilizer, and it is manufactured in the form of granular matrix using the nutrient absorbing extender that can validate the nutrients for a long time.
- fertilizers such as solid granular fertilizer, liquid fertilizer, fast-acting fertilizer, and slow-fertilizer have been developed and used in agriculture.
- fertilizers coated with the surface of fertilizer particles with a polymer compound or the like are mainly used as a slow-release fertilizer.
- the coating fertilizer has a problem that the film does not decompose in the soil for a long time, and also uses a polymer during the manufacturing process, and uses expensive equipment such as a fluidized bed coating machine and a drum coating machine to supply it at a higher price than general fertilizers.
- the fertilizer component is slowly eluted over a long period of time to reduce the number of fertilizers, it has recently attracted attention as a vital fertilizer corresponding to the reduction of the agricultural population.
- Korean Patent Publication No. 19960022408A proposes a method of reducing the dissolution rate of fertilizer components by mixing the resin and fertilizer and then extruding them through an extruder to coat the fertilizer components in a matrix form.
- the above method has a disadvantage in that expensive resins are used and there is a problem in commercializing a large amount of resin used.
- Korean Patent No. 10-0850186 a plant fertilizer composition including polyaspartic acid as a supplement for improving the fertilizer utilization efficiency of plants and the manufacture of fertilizers to increase the inefficiency by adding 0.1 to 10% of polyaspartic acid in the manufacture of complex fertilizers.
- the method is disclosed.
- the composite fertilizer prepared by the above method has a problem in that the fertilizer utilization is improved due to the effect of inhibiting fertilizer component leaching by polyaspartic acid, but in the case of crops that need to be fertilized, the fertilizer needs to be fertilized.
- US Patent No. 6,749,659 discloses the use of inorganic sulfur and swellable clay as the matrix forming material in a patent using a matrix concept to delay the dissolution rate of ammonium sulfate in water.
- the patent is prepared by melting the inorganic sulfur during the manufacturing process to prepare a liquid clay inorganic sulfur, and mixing and granulating the fertilizer components therein.
- the dissolution rate of the prepared granular fertilizer was determined according to the particle size, and the dissolution time was 1 to 2 mm faster than the 2 to 4 mm particles.
- the patent appears to inhibit release of nutrients to the outside of the particles by electrostatic bonding between negatively charged clay and ammonium ions as a mechanism of sustained release.
- Chinese Patent No. 101857490A discloses a compound fertilizer that can control the release rate of the nutrients.
- the patent proposes a sustained-release fertilizer prepared by melting a fertilizer component and mixing the moisturizing swellable clay mineral called attapulgite with the granules by spraying and dropping the upper granulator.
- the above method can obtain sustainability, there is a problem in that the manufacturing process is complicated and new equipment investment is required.
- US Pat. No. 7,252,697B2 discloses a process for preparing ammonium phosphate fertilizers having sustained release.
- the above method is a slow-release fertilizer prepared by mixing clay minerals such as zeolite and montmorillonite with slurry ammonium phosphate, acidifying by mixing sulfuric acid, and granulating the same.
- clay minerals such as zeolite and montmorillonite
- slurry ammonium phosphate acidifying by mixing sulfuric acid, and granulating the same.
- sustained release there is no information on sustained release and only discloses the effect of improving the utilization of phosphoric acid through the fixed inhibition of phosphoric acid in the soil.
- the present inventors prepare a high nutrient absorbing capacity additives primarily with a high nutrient absorbing capacity and a binder, and then uniformly mixed with additives and a compound fertilizer to produce a granular matrix form, the general compound fertilizer manufacturing facilities can be used as it is.
- the granular matrix-type compound fertilizer prepared by the above method is fertilized and retained for a long time after fertilizing fertilizer nutrients, and the adsorbed fertilizer nutrients, unlike general compound fertilizers, have a reduced loss due to leaching and removal from soil, It was found that the fertilizer utilization rate can be increased for crops, and completed the present invention.
- the problem to be solved by the present invention is to provide a method for producing a matrix granular composite fertilizer having a sustained effectiveness using a nutrient absorption increasing agent.
- Another problem to be solved by the present invention is to provide a matrix granular composite fertilizer obtained from the method for producing a matrix granular composite fertilizer having a sustained effectiveness using the above nutrient absorption and increasing agent.
- It provides a method for producing a matrix granular composite fertilizer having a sustainability comprising the step of uniformly mixing and drying the additives and fertilizer components having the nutrient absorption ability to prepare a matrix granular composite fertilizer.
- the polymer material may be polyacrylamide, polyvinyl acetate, polyvinyl acetate copolymer (-ethylene), polyvinyl alcohol and polyvinyl alcohol.
- Polymer ethyl cellulose, methyl cellulose, hydroxymethyl cellulose, hydroxypropyl cellulose, hydroxymethyl propyl cellulose, carboxylic polymer, polyvinylpyrrolidone, dextrin, maltodextrin, polysaccharide, vinylidene chloride copolymer, Starch, sodium lignosulfate, calcium lignosulfate, alginate and polychloroprene are preferably two or more selected from the group consisting of, as the extender having a nutrient absorption capacity calcium bentonite, silica hydrogel, starch, starch derivative, modified Lignosulfonate, weathered coal, coal, activated carbon, Orlite, Attapulgite, Magnesium Hydrogen Phosphate Trihydrate, Sodium Magnesium Silicate, Synthetic Calcium Silicate, Vermiculite, Humus, Acrylate Copolymer, Silicon Dioxide, Activated Clay, Aluminosilicate, and Sodium A
- the polymer When preparing the additive having a nutrient absorption capacity, the polymer is included in 0.1 to 50% by weight based on the total weight of the additive, it is preferable that the extender having a nutrient absorption capacity is contained in 50 to 99.9% by weight.
- the extender having a nutrient absorbing ability included in the preparation of the additive having a nutrient absorbing ability is preferably an inorganic extender and an organic extender are mixed in a weight ratio of 3: 7 to 7: 3.
- the drying is preferably dried for 20 minutes to 1 hour at a temperature of 80 to 100 °C, the grinding is preferably pulverized to 150 mesh or less.
- the additive having a food absorption capability and the fertilizer component is mixed, the additive having a food absorption capability is preferably mixed within a range of 5 to 25% by weight based on the weight of the fertilizer component.
- the step of producing the matrix granular composite fertilizer may include the steps of: i) uniformly mixing an additive and a fertilizer component having a nutrient absorption capability; ii) granulating the mixture by granulating the granulator; And iii) drying the granulated granules.
- a drum type or a fan type granulator is used as the granulator, and the drying is preferably dried for 30 to 40 minutes at a temperature of 300 to 450 ° C.
- the present invention is mixed with 0.1 to 50% by weight of the natural or synthetic polymer and 50 to 99.9% by weight of the extender having a nutrient absorbing capacity as a binder, dried and pulverized to prepare an additive having a nutrient absorbing capacity step; It provides a matrix-type granular composite fertilizer having a sustainability prepared by the method comprising the step of uniformly mixing and drying the additives and fertilizer components having a nutrient absorption ability to produce a matrix granular composite fertilizer.
- the compound fertilizer prepared by the present invention is used in the soil to absorb the fertilizer nutrients to prevent the loss, there is no need for additional preparation during the entire growth period of the crop, it is possible to reduce the labor force in the aging situation, and the fertilization It is a viable sustained fertilizer that can be adapted to mechanization.
- Chemical fermentation fertilizers such as UF, CDU, IBDU, and coating fertilizers that are effective through the existing polymer coatings are complicated by the manufacturing process and the raw materials are expensive.
- the slow-fertilizing fertilizer has the advantage of being able to supply the consumer at a low price because the manufacturing process is simple and the raw materials used are cheap because the manufacturing process can use the general fertilizer manufacturing process as it is.
- Figure 1 is a photograph taken with an optical microscope divided into a general surface ratio (a) and the cutting surface of the particles of the composite ratio (b) of the present invention divided into untreated and distilled water treatment.
- FIG. 2 is a photograph taken with an optical microscope divided into a general gas ratio (a) and a powder phase of the gas ratio (b) of the present invention divided into untreated and distilled water treatment.
- Method for producing a sustained-release matrix-type granular composite fertilizer comprises the steps of mixing the natural or synthetic polymer and the extender having a nutrient absorption capacity, and drying and grinding to prepare an additive having a nutrient absorption capacity; And uniformly mixing and drying the additive and fertilizer component having the nutrient absorption ability to prepare a matrix granular composite fertilizer.
- the step of preparing an additive having a nutrient absorbing ability is to mix and dry the natural or synthetic polymer having a nutrient absorbing ability and act as a binder in the preparation of fertilizer granules, and an extender having a nutrient absorbing ability, and then milled.
- the natural or synthetic polymer serves to form a matrix with an extender having a nutrient absorption capacity
- specific examples thereof include, but are not limited to, polyacrylamide, polyvinyl acetate, polyvinyl acetate copolymer (-ethylene) Copolymers of polyvinyl alcohol and polyvinyl alcohol, ethyl cellulose, methyl cellulose, hydroxymethyl cellulose, hydroxypropyl cellulose, hydroxymethyl propyl cellulose, carboxylic polymer, polyvinylpyrrolidone, dextrin, maltodextrin, It is preferably selected from the group consisting of polysaccharides, vinylidene chloride copolymer, starch, sodium lignosulfate, calcium lignosulfate, alginate and polychloroprene.
- the extender having a nutrient absorption capacity is preferably selected from an inorganic extender and an organic extender, and more preferably, an inorganic extender and an organic extender are mixed and used.
- the inorganic and organic extenders include, but are not limited to, calcium bentonite, silica hydrogel, starch, starch derivatives, modified lignosulfonates, weathered charcoal, coal, activated carbon, zeolites, attapulgite, magnesium hydro Two or more selected from the group consisting of gen phosphate trihydrate, sodium magnesium silicate, synthetic calcium silicate, vermiculite, humus, acrylate copolymer, silicon dioxide, activated clay, aluminosilicate, and sodium alumino-silicate desirable.
- the polymer is included in an amount of 0.1 to 50% by weight based on the total weight of the additive, preferably in an amount of 1 to 40% by weight, most preferably in an amount of 10 to 20% by weight.
- the extender is included in the amount of 50 to 99.9% by weight based on the total weight of the additive, preferably 60 to 99% by weight, most preferably included in the amount of 80 to 90% by weight.
- the role of the binder may be insufficient in granulating the fertilizer, and when mixed in excess of 50% by weight, the nutrient absorption capacity may be lowered.
- an inorganic extender and an organic extender may be used alone as the extender, but are preferably used in a mixed state. In this case, it is preferable to mix in the range of 30 to 70 weight% of the inorganic extender and 30 to 70 weight% of the organic extender based on the total weight of the extender.
- the mixture is dried for 20 minutes to 1 hour at a temperature of 80 to 100 °C.
- the drying temperature is less than 80 °C, there is a problem that the raw materials are entangled in the mixing and grinding process over the appropriate moisture, and when the temperature exceeds 100 °C, a portion of the mixture melts to act as a caking agent and agglomeration occurs There may be, and if it is dried in less than 20 minutes, a problem may occur in the uniform mixing by containing more than the appropriate moisture, when the drying for more than 1 hour may cause a problem that the thermal efficiency is lowered.
- the dried polymer and extender mixture that is, the additive is pulverized to 150 mesh or less, preferably pulverized to 100 mesh or less, and most preferably pulverized to 80 mesh or less. Grinding the additive having a nutrient absorbing ability to a predetermined size or less is because the additive having a nutrient absorbing ability is uniformly distributed in the composite fertilizer particles to form a matrix in the particle during the manufacture of the composite fertilizer.
- the additives and fertilizer components are uniformly mixed, granulated by granulation using a drum or fan type granulator, The granulated granules are then dried at 300 to 450 ° C. for 30 to 40 minutes to form a matrix in the form of intramicroparticles.
- the additives and fertilizer components Uniformly mixing the additives and fertilizer components is stirred for 5 to 10 minutes at 50 to 100rpm, homogenized.
- the additive having a nutrient absorption ability is mixed within a range of 5 to 25% by weight based on the weight of the fertilizer component.
- the additive is added in less than 5% by weight, it may be difficult to form the matrix in the particle, when added in excess of 25% by weight, the crop growth is lowered due to insufficient release of nutrients necessary for the initial growth of the crop Problems can arise.
- the additives and fertilizer components mixed uniformly are granulated to granulate.
- the assembly is preferably assembled through a drum or fan type granulator.
- the granules When the granules are sprayed with steam or water to dissolve the polymer and fertilizer nutrients to act as a binder, and the granulation rate and hardness increases as the polymer matrix is formed in the particles by hot air and granulation process after assembly.
- the inorganic and organic extenders of the above-mentioned additives and the matrix forming role of the polymer form a network structure in the particles, thereby improving resistance to impact during packaging and transportation.
- the granulated granules are dried at 300 to 450 ° C. for 30 to 40 minutes to form a matrix in the form of intracellular microcapsules.
- high moisture in the composite fertilizer particles there is a problem that occurs during storage, freezing, and when the drying exceeds 450 °C, the organic extender containing a polymer is carbonized to decrease the nutrient absorption capacity Problems can arise.
- a matrix granular composite fertilizer having sustained release is obtained through a packaging process.
- the fertilizer particles When the sustained-release matrix type granular composite fertilizer according to the present invention is fertilized in soil, the fertilizer particles absorb water, so that the fertilizer component is dissolved in water, and the dissolved fertilizer component has oil-containing ability to absorb nutrients contained in the particles. Absorbed by an electrostatic bond with an inorganic extender. In addition, the fertilizer particles absorb water and decay due to the nutrient retention capacity (electrostatic bonding) and water retention capacity of the polymer itself, soaking into the soil voids and forming a microcapsule-type matrix by the interaction between the soil, fertilizer, extender, and polymer. Done.
- fertilizer component a general fertilizer component in the art may be used, but is not limited thereto.
- Urea, yuan, diammonium phosphate, potassium chloride, siliceous, or the like may be used.
- the sustained-release granular composite fertilizer prepared in the above may be prepared by mixing the sustained-release granular composite fertilizer prepared in the above and the coating fertilizer having a specific elution period in a way that can more accurately meet the nutrient requirements of each crop.
- granular fertilizers having a sustained release prepared in the above manner, coating fertilizers having a specific elution period, and useful microorganisms having a nitrogen solubility and phosphoric acid and potassium solubilizing ability, which can more accurately meet the nutrient demand characteristics of each crop. It can also be prepared by mixing with.
- an inorganic extender vermiculite
- 40 wt% of an organic extender corrosive
- the weight percents were mixed homogeneously at 50 rpm for 10 minutes. This was then dried at approximately 90 ° C. for 40 minutes and then ground to a size of 80 mesh or less.
- Figure 1 is shown by cutting the particles of the general gas ratio (a) and the gas ratio (b) of the present invention
- Figure 2 shows the general gas ratio (a) and the gas ratio (b) of the present invention in powder form It is shown.
- Dissolution Inhibition Test Method Three No. 2 filter papers were laid at the bottom of a cylindrical column of 2.6 cm in diameter and 13.5 cm in length, and 10 g of sand was put therein. Subsequently, one No. 2 filter paper was laid on the sand, and 30 g of soil and the sample of Example 1 or Comparative Example 1 (0.5 g and 1 g, respectively) were mixed and packed. Subsequently, one No. 2 filter paper is laid on the soil layer, and 60 ml of water is gradually added from the top, and when the water reaches the coke portion, the coke is locked. After leaving for 12 hours, the coke was opened to investigate the time for water to elute to the soil layer.
- Example 2 After fertilizing the composite fertilizer of Example 1 and Example 2 4 days before the transfer, so that the fertilizer is evenly treated throughout the soil, the fertilizer application amount is 73.3 kg, based on 10a in Example 1 In Example 2, 61.1 kg of each and 61.1 kg of Comparative Example 1 were treated with a total amount of rice transplantation once. Two growth stages were examined at each growth stage.
- the survey items were grass height, number of grains, and leaf color (SPAD value), and the cultivation management was based on the RDA Capital Cultivation Method.
- Example 1 is a slow-release fertilizer using the composite fertilizers of Examples 1 and 2 as the conventional fertilizer as a result of the 30th and 60th day after transplanting. It showed that the results boil, Example 1 and Example 2 was confirmed that the effect on the rice growth is maintained even if the whole amount of once treatment during the growth of rice.
- Example 1 and Example 2 and the slow-fertilizing fertilizer of Comparative Example 1 was fertilized 7 days before the formulation and then rotary to allow the fertilizer to be uniformly treated throughout the soil, and fertilizer fertilization was carried out based on 10a. 126.6 kg of Example 1, 105.5 kg of Example 2, and 105.5 kg of Comparative Example 1 were each treated with a total amount before the set meal. Three growth stages were examined at different stages of growth, and the final yield at harvest time.
- the survey items were grass height, leaf color (SPAD value), and yields per unit area.
- the overall growth is high in height and leaf color as compared to the fertilizer of Comparative Example 1, which is a slow-release fertilizer used as a conventional fertilizer as a result of the 10th, 20th and 30th investigations as shown in Table 3 below.
- Table 4 the total yield of red pepper was the highest yield index in Example 2.
- Example 1 and Example 2 was confirmed that the effect on the growth and yield increase of the pepper is continuously maintained even if the whole amount of one time during the growth process of pepper.
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- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Pest Control & Pesticides (AREA)
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Abstract
Description
구분 | 흙 | 실시예 1(0.5g) | 실시예 1(1g) | 비교예 1(0.5g) | 비교예 1(1g) |
용탈시간(분) | 100 | 290 | 6,480 | 180 | 660 |
무처리대비 용탈억제율(%) | 0 | 190 | 6,380 | 80 | 560 |
일반복비대비 용탈억제율(%) | 61.1 | 881.8 |
조사항목 | 반복 | 이앙후 30일 | 이앙후 60일 | ||||||
무시비 | 비교예1 | 실시예1 | 실시예2 | 무시비 | 비교예1 | 실시예1 | 실시예2 | ||
시비량(/10a) | 0kg | 61.1kg | 73.3kg | 61.1kg | 0kg | 61.1kg | 73.3kg | 61.1g | |
초장(㎝) | 1 | 31.1 | 35.5 | 36.1 | 36.4 | 61.2 | 70.5 | 69.8 | 73.5 |
2 | 29.5 | 36.5 | 35.3 | 36.1 | 62.5 | 72.6 | 73.2 | 70.6 | |
3 | 32.5 | 36.1 | 35.6 | 35.7 | 62.8 | 73.5 | 71.2 | 71.5 | |
평균 | 31.0 | 36.0 | 35.7 | 36.1 | 62.2 | 72.2 | 71.4 | 71.9 | |
엽색SPAD값 | 1 | 27.5 | 40.5 | 40.8 | 42.6 | 23.4 | 33.5 | 32.9 | 33.5 |
2 | 26.7 | 41.8 | 41.6 | 42.1 | 22.1 | 34.6 | 35.1 | 34.1 | |
3 | 25.6 | 42.1 | 42.5 | 42.7 | 21.5 | 34.1 | 34.8 | 34.2 | |
평균 | 26.6 | 41.5 | 41.6 | 42.5 | 22.3 | 34.1 | 34.3 | 33.9 | |
분얼수(개) | 1 | 14 | 20 | 23 | 22 | 12 | 21 | 22 | 20 |
2 | 13 | 22 | 22 | 20 | 13 | 20 | 20 | 19 | |
3 | 13 | 21 | 21 | 22 | 12 | 20 | 21 | 22 | |
평균 | 13.3 | 21.0 | 22.0 | 21.3 | 12.3 | 20.3 | 21.0 | 20.3 |
항목 | 반복 | 초장(㎝) | 엽색(SPAD값) | ||||||
무시비 | 비교예1 | 실시예2 | 실시예 3 | 무시비 | 비교예1 | 실시예2 | 실시예 3 | ||
시비량(/10a) | 0kg | 105.5kg | 126.6kg | 105.5kg | 0kg | 105.5kg | 126.6kg | 105.5kg | |
정식후10일 | 1 | 13.2 | 16.2 | 17.8 | 17.1 | 28.5 | 45.7 | 47.5 | 47.5 |
2 | 12.5 | 15.9 | 18.2 | 17.6 | 29.4 | 46.5 | 46.7 | 47.1 | |
3 | 12.8 | 15.3 | 18.1 | 17.3 | 28.4 | 46.1 | 46.4 | 47.3 | |
평균 | 12.8 | 15.8 | 18.0 | 17.3 | 28.8 | 46.1 | 46.9 | 47.3 | |
정식후 20일 | 1 | 18.5 | 24.5 | 23.8 | 24.1 | 38.5 | 63.2 | 67.1 | 67.1 |
2 | 17.4 | 23.2 | 23.7 | 22.1 | 38.1 | 62.1 | 65.4 | 66.7 | |
3 | 17.5 | 23.9 | 22.5 | 23.8 | 37.2 | 61.4 | 66.6 | 66.9 | |
평균 | 17.8 | 23.9 | 23.3 | 23.3 | 37.9 | 62.2 | 66.4 | 66.9 | |
정식후 30일 | 1 | 31.2 | 36.8 | 35.7 | 37.5 | 39.4 | 66.7 | 69.4 | 71.1 |
2 | 32.4 | 37.1 | 37.2 | 37.1 | 40.1 | 66.4 | 71.4 | 69.5 | |
3 | 31.6 | 37.4 | 37.3 | 36.5 | 41.8 | 66.5 | 71.4 | 70.1 | |
평균 | 31.7 | 37.1 | 36.7 | 37.0 | 40.4 | 66.5 | 70.7 | 70.2 |
조사항목 | 무시비 | 비교예1 | 실시예2 | 실시예 3 | |
시비량( /10a) | 반복 | 0kg | 105.5kg | 126.6kg | 105.5kg |
붉은고추생체중(kg/30m2) | 1 | 4.1 | 8.4 | 6.2 | 7.5 |
2 | 3.8 | 6.3 | 6.2 | 7.0 | |
3 | 4.7 | 7.2 | 9.0 | 9.5 | |
총수량 | 12.6 | 21.9 | 21.4 | 24.0 |
Claims (11)
- 결합제로서 천연 또는 합성 고분자 0.1중량% 내지 50중량% 및 양분흡수능을 갖는 증량제 50 내지 99.9중량%를 혼합 및 건조한 후 분쇄하여 양분흡수능을 갖는 첨가물을 제조하는 단계; 및상기 양분흡수능을 갖는 첨가물과 비료성분을 균일하게 혼합 및 건조하여 매트릭스형 입상복합비료를 제조하는 단계;를 포함하는 지효성을 갖는 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 고분자 물질로는 폴리아크릴아미드, 폴리비닐 아세테이트, 폴리비닐 아세테이트 코폴리머(-에틸렌), 폴리비닐 알코올과 폴리비닐 알코올의 코폴리머, 에틸셀룰로오스, 메틸셀룰로오스, 히드록시메틸셀룰로오스, 히드록시프로필셀룰로오스, 히드록시프로필메틸셀룰로오스, 카르복실릭 폴리머, 폴리비닐피롤리돈, 덱스트린, 말토덱스트린, 폴리사카라이드, 염화 비닐리덴 코폴리머, 전분, 소듐 리그노설페이트, 칼슘 리그노설페이트, 알기네이트 및 폴리클로로프렌으로 이루어진 군에서 2종 이상 선택되는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 양분흡수능을 갖는 증량제로는 칼슘 벤토나이트, 실리카 히드로겔, 전분, 전분 유도체, 개질된 리그노설포네이트, 풍화탄, 석탄, 활성탄, 제오라이트, 아타펄자이트, 마그네슘 히드로겐 포스페이트 트리히드레이트, 소듐 마그네슘 실리케이트, 합성 칼슘 실리케이트, 버미큘라이트, 부식질, 아크릴레이트 코폴리머, 이산화규소, 활성화된 점토, 알루미노실리케이트, 및 소듐 알루미노-실리케이트로 이루어진 군에서 2종 이상 선택되는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 양분흡수능을 갖는 첨가물 제조시, 고분자는 첨가물 전체 중량에 대해 0.1 내지 50중량%로 포함되며, 양분흡수능을 갖는 증량제는 50 내지 99.9중량%로 포함되는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 양분흡수능을 갖는 첨가물의 제조시 포함되는 양분흡수능을 갖는 증량제는 무기증량제 및 유기증량제가 중량비로 : 3:7 내지 7:3으로 혼합되는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 양분흡수능을 갖는 첨가물의 제조시 건조는 80 내지 100℃의 온도에서 20분 내지 1시간 동안 건조되는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 분쇄는 150메쉬 이하로 분쇄하는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 양분흡수능을 갖는 첨가물은 비료성분의 중량에 대하여 5 내지 25중량%의 범위내에서 혼합되는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 매트릭스형 입상복합비료를 제조하는 단계는 i) 양분흡수능을 갖는 첨가물과 비료성분을 균일하게 혼합하는 단계; ii) 상기 혼합물을 조립기를 이용하여 조립하여 입상화하는 단계; 및 iii) 조립된 입상을 건조하는 단계를 포함하는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항에 있어서,상기 매트릭스형 입상복합비료를 제조하는 단계에서 상기 조립기로는 드럼형 또는 팬형 조립기가 사용되고, 상기 건조는 300 내지 450℃의 온도에서 30 내지 40분 동안 건조되는 것인 매트릭스형 입상복합비료의 제조방법.
- 제1항 내지 제10항중 어느 하나의 항에 따른 방법을 제조된 지효성을 갖는 매트릭스형 입상복합비료.
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JP2016515250A JP2016522150A (ja) | 2013-05-24 | 2013-10-18 | 遅効性を有するマトリックス型粒状複合肥料の製造方法及び該方法により得られたマトリックス型粒状複合肥料 |
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CN104987162A (zh) * | 2014-12-25 | 2015-10-21 | 天津北洋百川生物技术有限公司 | 颗粒肥料及其制备方法 |
CN104987162B (zh) * | 2014-12-25 | 2018-05-11 | 天津北洋百川生物技术有限公司 | 颗粒肥料及其制备方法 |
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US11802097B2 (en) | 2017-04-19 | 2023-10-31 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with urease inhibitor and nitrification separated within the same particle |
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Also Published As
Publication number | Publication date |
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KR20140137872A (ko) | 2014-12-03 |
US20160102028A1 (en) | 2016-04-14 |
CN105358506A (zh) | 2016-02-24 |
MY174203A (en) | 2020-03-14 |
US10287217B2 (en) | 2019-05-14 |
KR101485578B1 (ko) | 2015-01-21 |
JP2016522150A (ja) | 2016-07-28 |
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