KR100901799B1 - Manufacturing method of fertilizer based on aminosan - Google Patents

Manufacturing method of fertilizer based on aminosan Download PDF

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KR100901799B1
KR100901799B1 KR20070119678A KR20070119678A KR100901799B1 KR 100901799 B1 KR100901799 B1 KR 100901799B1 KR 20070119678 A KR20070119678 A KR 20070119678A KR 20070119678 A KR20070119678 A KR 20070119678A KR 100901799 B1 KR100901799 B1 KR 100901799B1
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amino acid
fertilizer
fermentation
water
liquid fertilizer
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KR20070119678A
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Korean (ko)
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KR20090053050A (en
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정정철
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대은엠비코(주)
정정철
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    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F11/00Other organic fertilisers
    • C05F11/08Organic fertilisers containing added bacterial cultures, mycelia or the like
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F5/00Fertilisers from distillery wastes, molasses, vinasses, sugar plant or similar wastes or residues, e.g. from waste originating from industrial processing of raw material of agricultural origin or derived products thereof
    • 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
    • C05G1/00Mixtures of fertilisers belonging individually to different subclasses of C05
    • 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
    • C05G5/00Fertilisers characterised by their form
    • C05G5/20Liquid fertilisers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Abstract

본 발명은 탈지강, 콩박, 피마자박, 밀기울, 대두박 등 당류를 혐기성 미생물인 바실러스, 사카라마이세스균 등으로 발효시켜 아미노산화 시킨 후에 붕소, 몰리브덴을 혼합하여 침전시킨 상등수에 휴믹산, 키토산, 효소, 미네랄을 첨가하여 친환경 제제로 생산하거나 질소(N), 인산(P), 칼리(K)를 첨가시켜 4종 복합 아미노산 액체 비료로 제조할 수 있는 아미노산 액체비료 제조 방법에 관한 것으로 본 발명에 따라 제조되는 아미노산 액체 비료는 엽면시비로 식물에 직접 뿌리면 아미노산이 식물에 직접 흡수되어 식물의 성장을 빠르게 하면서 키토산, 효소, 미네랄, 붕소 등의 미량 영양요소가 식물에 작용하여 식물의 면역력을 증가시켜 질병예방에 효과가 있다.The present invention fermented sugars such as skim steel, soybean meal, castor meal, wheat bran, soybean meal, etc. by anaerobic microorganisms Bacillus, Saccharomyces, etc. The present invention relates to a method for preparing an amino acid liquid fertilizer, which can be produced as an eco-friendly preparation by adding minerals, or can be prepared as four complex amino acid liquid fertilizers by adding nitrogen (N), phosphoric acid (P), and Kali (K). Amino acid liquid fertilizer, which is a foliar fertilizer, is sprayed directly on a plant and amino acids are directly absorbed by the plant to accelerate plant growth, while micronutrients such as chitosan, enzymes, minerals, and boron act on the plant to increase plant immunity and prevent disease. Is effective.

아미노산, 액체비료, 당류, 혐기성 미생물, 휴믹산, 키토산, 효소 Amino acids, liquid fertilizers, sugars, anaerobic microorganisms, humic acid, chitosan, enzymes

Description

아미노산 액체비료 제조 방법{MANUFACTURING METHOD OF FERTILIZER BASED ON AMINOSAN}Amino acid liquid fertilizer manufacturing method {MANUFACTURING METHOD OF FERTILIZER BASED ON AMINOSAN}

본 발명은 아미노산 액체비료 제조방법에 관한 것으로써, 보다 상세하게는 탈지강, 콩박, 피마자박, 밀기울, 대두박 등 당류를 가진 유박을 혐기성 미생물인 바실러스균, 사카라마이세스균으로 완전 발효시켜 아미노산화 한 후 수용성붕소, 수용성몰리브덴을 혼합하여 침전시킨 상등수에 키토산, 효소, 미네랄 등을 첨가하여 친환경 액제로 생산하고, N, P, K 성분을 첨가하여 4종 복합 아미노산 액체비료로 제조할 수 있는 아미노산 액체비료 제조 방법에 관한 것이다.The present invention relates to a method for preparing an amino acid liquid fertilizer, and more specifically, amino acid with sugars such as skimmed steel, soybean meal, castor meal, bran, soybean meal, and fermented completely with anaerobic microorganisms Bacillus and Saccharomyces. Then, chitosan, enzymes, minerals, etc. are added to the precipitated supernatant mixed with water-soluble boron and water-soluble molybdenum to produce eco-friendly liquids, and N, P, K components can be prepared as four complex amino acid liquid fertilizers. It relates to a liquid fertilizer manufacturing method.

종래의 액체비료 제조방법은 비료공정 규격이 제시하는 질소, 인산, 칼리 및 붕소, 마그네슘, 철등 등의 무기 화합물과 미네랄 등의 미량 영양요소를 물에 녹여서 액체 비료로 제조하고 있다.Conventional liquid fertilizer manufacturing method has been prepared in liquid fertilizer by dissolving micronutrients such as inorganic compounds and minerals such as nitrogen, phosphoric acid, kali and boron, magnesium, iron and the like proposed in the fertilizer process specifications.

한편, 대한민국 공개특허 제10-1999-0084097호(혈분 분해액을 기초로 한 액체비료 제조방법)에서는 혈분 분해액을 기초로 한 액체비료 제조방법이 제시되고 있다.On the other hand, Korean Patent Laid-Open Publication No. 10-1999-0084097 (the liquid fertilizer manufacturing method based on blood breakdown liquid) has been proposed a liquid fertilizer manufacturing method based on blood breakdown liquid.

그러나, 상기한 종래의 액체비료는 식물에 필요한 영양소를 공급하는 것은 되지만 식물이 장기간 영양분으로 사용할 수 있는 아미노산이 없기 때문에 계속적으로 비료를 살포하여야 하는 단점이 있으며,However, the above-mentioned conventional liquid fertilizer is to supply the nutrients necessary for the plant, but there is a disadvantage that the fertilizer must be continuously sprayed because there is no amino acid that can be used as a nutrient for a long time,

또한, 상기 혈분 분해액을 기초로 한 액체비료 제조방법에서는, 혈분을 분해한 단백질 분해물은 식물이 흡수하는데 시간이 걸리며 혈분분해 과정에서 가스 및 악취문제가 발생하여 주변환경 및 농작물에 피해를 줄 수 있는 단점이 있었다.In addition, in the liquid fertilizer manufacturing method based on the blood breakdown liquid, the protein breakdown product that decomposes the blood takes time for the plant to absorb and may cause gas and odor problems during the blood breakdown process, which may damage the surrounding environment and crops. There was a disadvantage.

또한, 대부분의 복합액체 비료는 그 모재를 단당류나 다당류를 사용하고 있으나, 단당류나 다당류는 분해가 쉬워서 식물이 빨리 흡수하므로 빠른 성장을 하지만 뿌리가 약하여 식물의 수명이 짧고 병충해에 견디는 힘이 약해진다.In addition, most compound liquid fertilizers use monosaccharides or polysaccharides, but monosaccharides and polysaccharides are easily decomposed and absorbed quickly by plants, so they grow quickly, but the roots are weak, and the plant life is short and the strength to withstand pests is weakened. .

따라서, 식물이 병충해에 견디는 면역력을 키우려면 필수 아미노산의 지속적인 공급 및 미량원소의 투입이 필연적이라 할 수 있다. Therefore, the continuous supply of essential amino acids and the input of trace elements is inevitable in order for plants to develop immunity to withstand pests.

상기와 같은 종래기술의 문제점을 해결하기 위하여, 본 발명에 의한 아미노산 액체비료 제조방법은,In order to solve the problems of the prior art as described above, the amino acid liquid fertilizer manufacturing method according to the present invention,

당분공급원에 혐기성 발효균을 투입하고, 밀폐된 탱크에서 발효시키는 발효단계와; 상기 발효단계에서 발효된 발효액을 추출하는 추출단계와; 상기 추출단계를 거친 발효액에 수용성붕소와 수용성몰리브덴을 첨가하고, 침전시키는 침전단계 와; 효소를 혼합하고 교반하는 교반단계와; 상기 침전단계를 거친 발효액에 질소, 인산, 칼리 비료를 추가하여 N:P:K의 비율을 조절하는 비료성분조절단계;를 갖는다.A fermentation step of putting anaerobic fermentation bacteria into the sugar supply source and fermenting in a closed tank; An extraction step of extracting the fermentation broth fermented in the fermentation step; A precipitation step of adding water-soluble boron and water-soluble molybdenum to the fermentation broth after the extraction step, and precipitating; A stirring step of mixing and stirring the enzyme; Fertilizer component control step of adjusting the ratio of N: P: K by adding nitrogen, phosphoric acid, kali fertilizer to the fermentation broth after the precipitation step.

상기 발효단계에서, 상기 당분공급원은, 탈지강, 콩박, 피마자박, 밀기울, 대두박 중 어느 하나 또는 둘 이상을 포함하며, 상기 혐기성 발효균은, 바실러스속 또는 사카라마이세스속에 속하는 미생물이며, 상기 혐기성 발효균의 투입량은, 상기 당분공급원 1톤당 10 내지 30g인 것이 바람직하다.In the fermentation step, the sugar source, skim steel, soybean meal, castor meal, bran, soybean meal, any one or two or more, the anaerobic fermentation bacteria, belong to the genus Bacillus or Saccharomyces genus, the anaerobic fermentation bacteria The dose of is preferably 10 to 30 g per tonne of sugar source.

상기 침전단계에서, 상기 수용성붕소는 상기 추출단계의 발효액 전체 중량의 0.5~1중량% 이며, 상기 수용성몰리브덴은 0.1~0.5중량%이며, 상기 수용성붕소와 수용성몰리브덴을 첨가한 발효액 전체 중량의 40~60% 중량에 해당하는 물을 혼합하는 것이 바람직하다.In the precipitation step, the water-soluble boron is 0.5 to 1% by weight of the total weight of the fermentation broth of the extraction step, the water-soluble molybdenum is 0.1 to 0.5% by weight, 40 ~ of the total weight of the fermentation broth added with the water-soluble boron and water-soluble molybdenum It is preferable to mix water corresponding to 60% weight.

상기 비료성분조절단계에서, N:P:K의 비가 3.5~4.5 : 1.5~2.5 : 1.5~2.5가 되도록 하는 것이 바람직하다.In the fertilizer component adjustment step, N: P: K ratio is preferably 3.5 to 4.5: 1.5 to 2.5: 1.5 to 2.5.

상기 교반단계는, 휴믹산, 키토산, 미네랄을 추가하고, 2~3시간 교반시키는 것이 바람직하다.In the stirring step, it is preferable to add humic acid, chitosan, mineral, and stirred for 2-3 hours.

상기 휴믹산, 키토산, 효소, 미네랄은, 각각 상기 침전단계를 거친 발효원액 중량의 0.05~2%, 0.05~2%, 1~3%, 0.05~2%인 것이 바람직하다.The humic acid, chitosan, enzymes, and minerals are preferably 0.05 to 2%, 0.05 to 2%, 1 to 3%, and 0.05 to 2% of the weight of the fermentation stock solution, which has undergone the precipitation step.

여기서, 본 발명에서 "효소"는 단백질 분해효소(프로테아제)로서 식물에서 추출한 트립신을 사용하는 것이 바람직하다. "미네랄"은 통상적으로 광물질에서 유산으로 추출한 용액(ion)의 액체상태로, 칼슘, 칼륨, 마그네슘, 철, 아연, 셀렌(셀레늄), 망간, 규소, 리튬, 게르마늄, 붕소등을 포함하며, 본 발명에서 사용하는 미네랄 용액은 Ca, K, Mg, Fe, Zn, Se, Mn, Si, Li, Ge, B가 각각 52, 300, 300, 500, 600, 20, 150, 20, 200, 20, 100ppm이상이다. "수용성붕소"는 물에 녹는 붕소로서 다양한 형태의 붕소화합물(붕산 등)이며, "수용성몰리브덴"은 물에 녹는 다양한 형태의 몰리브덴화합물(몰리브덴산, 몰리브덴산염, 몰리브덴산암모늄 등)을 의미한다.Here, in the present invention, "enzyme" is preferably used as trypsin extracted from plants as protease (protease). "Mineral" is usually in the liquid state of mineral (ion) extracted from minerals and includes calcium, potassium, magnesium, iron, zinc, selenium (selenium), manganese, silicon, lithium, germanium, boron, etc. The mineral solution used in the invention is Ca, K, Mg, Fe, Zn, Se, Mn, Si, Li, Ge, B is 52, 300, 300, 500, 600, 20, 150, 20, 200, 20, It is more than 100ppm. "Water-soluble boron" is boron soluble in water and various forms of boron compounds (boric acid, etc.), and "water-soluble molybdenum" means various forms of molybdenum compounds (molybdate, molybdate, ammonium molybdate, etc.).

이상과 같이 본 발명은, 식물의 당류를 혐기성균인 바실러스,균 사카라마이세스균으로 발효시킨 발효액에 붕소, 몰리브덴 및 휴믹산, 키토산, 효소, 미네랄을 첨가시켜 친환경 액제로 제조한 후 질소, 인산, 칼리를 첨가하여 4종 복합비료 성분을 충족시키는 아미노산 액체비료의 제조방법으로, 질소, 인산, 칼리가 식물의 빠른 성장을 유도하고 휴믹산, 키토산, 효소, 미네랄 성분 등이 식물의 면역성을 증가시키면서 아미노산이 식물에게 지속적인 영양물질을 공급해 줌으로써 엽면 시비로도 식물의 완전한 성장을 유도할 수가 있어서 향후 점진적으로 확산될 수경재배 농산물 생산에 크게 기여할 수 있다.As described above, the present invention is prepared by adding boron, molybdenum and humic acid, chitosan, enzymes, minerals to fermentation broth fermented with saccharides of plant anaerobes, Bacillus and bacterium Saccharomyces, and then preparing nitrogen, phosphoric acid, and kali. A method for preparing amino acid liquid fertilizer that meets the four complex fertilizer components by adding the nitrogen, phosphoric acid, and Kaliga induces rapid growth of plants and humic acid, chitosan, enzymes, minerals, etc. By supplying nutrients to plants continuously, foliar fertilization can induce complete growth of plants, which can greatly contribute to the production of hydroponic agricultural products that will gradually spread in the future.

이하 실시예를 통하여 본 발명을 상세하게 설명한다. 그러나, 이들 실시예 는 예시적인 목적일 뿐 본 발명이 이에 한정되는 것은 아니다.The present invention will be described in detail through the following examples. However, these examples are for illustrative purposes only and the present invention is not limited thereto.

[실시예1]Example 1

상기 목적을 달성하기 위한 본 발명은,The present invention for achieving the above object,

탈지강, 피마자박, 밀기울, 대두박을 중량비로 40%, 20%, 20%, 20% 비율로 혼합한 후, 상기 혼합물에 혐기성 미생물인 바실러스균(바실러스 서브틸리스)을 혼합물 1톤에 20g을 투입한 후 밀폐된 탱크 내에서 35일간 발효시켰다.After mixing the degreasing steel, castor foil, bran, and soybean meal in 40%, 20%, 20%, and 20% by weight, 20 g of Bacillus subtilis, an anaerobic microorganism, is added to the mixture. It was fermented for 35 days in a closed tank after the addition.

발효시킨 후, 탱크의 하부에 발생한 발효액을 추출하였다.After fermentation, the fermentation broth generated at the bottom of the tank was extracted.

탱크하부에서 채취한 발효액에 중량비로 붕수용성붕소 0.7%, 수용성몰리브덴 0.3%를 첨가시켜 첨가 발효액으로 제조한 후, 첨가 발효액 중량비로 물을 2:1 비율로 혼합한 후 4일 침전시켜 첨가 발효액내의 유해성분인 중금속, 타르, 식물기름 성분이 침전시키고, 상등수를 채취하여 미생물 발효원액을 생성하였다.To the fermentation broth obtained from the bottom of the tank, 0.7% boron-soluble boron and 0.3% water-soluble molybdenum were added to prepare the fermentation broth, followed by mixing the water in a 2: 1 ratio by weight of the addition fermentation broth. Noxious components such as heavy metals, tars, and plant oils were precipitated, and supernatant was collected to produce microbial fermentation stock solution.

미생물 발효원액에 전체중량 대비 휴믹산을 1%, 키토산을 1%, 효소를 2%, 미네랄을 1% 혼합한 후 교반기로 2.5시간 교반시켜 친환경 액제를 생산하였다.1% of humic acid, 1% of chitosan, 2% of enzyme, and 1% of minerals were mixed in the fermentation broth of microorganisms, followed by stirring for 2.5 hours with a stirrer to produce an environment-friendly liquid.

이렇게 생성된 친환경 액제에 질소, 인산, 칼리 비료를 N : P : K 비가 4 : 2 : 2가 되도록 혼합하여 4종 복합비료 성분인 아미노산 액체 비료를 제조하였다.Nitrogen, phosphoric acid, and calibrated fertilizer were mixed in such a manner that the N: P: K ratio was 4: 2: 2 to prepare an amino acid liquid fertilizer, which is a four-component fertilizer component.

상기 탈지강, 피마자박, 밀기울, 대두박을 분쇄하여 사용하면 더욱 효율이 높아진다.If the crushed steel, castor foil, bran, soybean meal is used to grind more efficient.

[실시예2]Example 2

[실시예1]에서, 탈지강, 피마자박, 밀기울, 대두박을 상기 비율과 다르게 하 거나 이들 중 어느 하나 또는 둘이상을 서로 다른 비율로 혼합하여 당분공급원으로 사용하였다.In [Example 1], degreasing steel, castor foil, bran, soybean meal was used as a sugar source by varying the ratio or any one or two or more of these in different ratios.

최종적으로 생산된 아미노산 액체 비료의 성분이나 효능에는 큰 차이가 없었다.There was no significant difference in the composition and efficacy of the finally produced amino acid liquid fertilizer.

[실시예3]Example 3

[실시예1]~[실시예2]에서, 바실러스 서브틸리스 대신 같은 속의 다른 종, 사카로마이세스 세르비지아(Saccharomyces cerevisiae)나 같은 속에 속하는 다른 종, 락토바실러스(Lactobacillus)속, 셀룰로모나스(Cellulomonas)속, 클로스트리듐(Clostridium)속, 트라이코데마(Trichoderma)속, 아스퍼질러스(Aspergillus)속, 라이조푸스(Rhizopus)속, 페니실륨(Penicillium)속, 칸디다(Candida)속, 스테렙토코커스(Streptococcus)속, 마이크로비스포라(Microbispora)속 중 어느 하나 또는 둘 이상을 혼합물 1톤당 10~30g이 되도록 투입하였다.In Examples 1 to 2, instead of Bacillus subtilis, other species of the same genus, Saccharomyces cerevisiae or other species belonging to the same genus, Lactobacillus genus, cellulose Genus Cellulomonas, Genus Clostridium, Genus Trichoderma, Genus Aspergillus, Genus Lyzopus, Genus Penicillium, Genus Candida, Genus Genus One or two or more of Streptococcus genus and Microbispora genus were added to 10 to 30 g per ton of the mixture.

최종적으로 생산된 아미노산 액체 비료의 성분이나 효능에는 큰 차이가 없었다.There was no significant difference in the composition and efficacy of the finally produced amino acid liquid fertilizer.

[실시예4]Example 4

[실시예1]~[실시예3]에서, 밀폐된 탱크 내에서 발효되는 시간을 25~40일 사이에 1일 간격으로 변화시켰다.In Examples 1 to 3, the time of fermentation in a closed tank was changed at daily intervals between 25 and 40 days.

최종적으로 생산된 아미노산 액체 비료의 성분이나 효능에는 큰 차이가 없었 다.There was no significant difference in the composition or efficacy of the finally produced amino acid liquid fertilizer.

[실시예5]Example 5

[실시예1]~[실시예4]에서, 탱크하부에서 채취한 발효액에 첨가하는 붕산의 양을 0.5~1%로 변화시켰다.In Examples 1 to 4, the amount of boric acid added to the fermentation broth collected from the bottom of the tank was changed to 0.5 to 1%.

최종적으로 생산된 아미노산 액체 비료의 성분이나 효능에는 큰 차이가 없었다.There was no significant difference in the composition and efficacy of the finally produced amino acid liquid fertilizer.

[실시예6]Example 6

[실시예1]~[실시예5]에서, 침전시키는 시간을 4일에서 3~5일로 변화시켰다.In Examples 1 to 5, the time for precipitation was changed from 4 days to 3 to 5 days.

최종적으로 생산된 아미노산 액체 비료의 성분이나 효능에는 큰 차이가 없었다.There was no significant difference in the composition and efficacy of the finally produced amino acid liquid fertilizer.

[실시예7]Example 7

[실시예1]~[실시예6]에서, 미생물 발효원액에 혼합하는 휴믹산, 키토산, 효소, 미네랄을 각각 0.05~2%, 0.05~2%, 1~3%, 0.05~2%까지 변화시켰다.In Examples 1 to 6, humic acid, chitosan, enzyme, and minerals mixed in the microbial fermentation stock solution were changed to 0.05-2%, 0.05-2%, 1-3%, and 0.05-2%, respectively. .

최종적으로 생산된 아미노산 액체 비료의 성분이나 효능에는 큰 차이가 없었다.There was no significant difference in the composition and efficacy of the finally produced amino acid liquid fertilizer.

[실시예8]Example 8

[실시예1]~[실시예7]에서, 미생물 발효원액에 휴믹산, 키토산, 효소, 미네랄을 혼합하고, 교반시키는 시간을 2~3시간까지 변화시켰다.In Examples 1 to 7, the time for mixing and stirring the humic acid, the chitosan, the enzyme, and the mineral with the microbial fermentation stock solution was changed to 2-3 hours.

최종적으로 생산된 아미노산 액체 비료의 성분이나 효능에는 큰 차이가 없었다.There was no significant difference in the composition and efficacy of the finally produced amino acid liquid fertilizer.

효소의 양을 줄이는 경우에는 교반시간을 증가시키는 것이 바람직하다.When reducing the amount of enzyme, it is desirable to increase the stirring time.

[실시예9]Example 9

[실시예1]~[실시예8]에서, 생성된 친환경 액제에 질소, 인산, 칼리 비료를 N : P : K 비를 3.5~4.5 : 1.5~2.5 : 1.5~2.5가 되도록 혼합하였다.In Example 1 to Example 8, nitrogen, phosphoric acid, and cartilage were mixed in the resulting environmentally friendly liquid so that the N: P: K ratio was 3.5 to 4.5: 1.5 to 2.5: 1.5 to 2.5.

최종적으로 생산된 아미노산 액체 비료의 성분은 첨가한, 질소, 인산, 칼리 비료의 비율에 따라 차이가 있으나, 효능에는 큰 차이가 없었다.The components of the finally produced amino acid liquid fertilizer were different depending on the ratio of added nitrogen, phosphoric acid and kali fertilizer, but there was no significant difference in efficacy.

N : P : K 비는 필요에 따라 적절히 변경할 수 있다.N: P: K ratio can be changed suitably as needed.

Claims (8)

아미노산 액체비료 제조방법에 있어서,In the amino acid liquid fertilizer manufacturing method, 당분공급원에 발효균을 투입하고, 밀폐된 탱크에서 발효시키는 발효단계;A fermentation step of adding fermentation bacteria to the sugar source and fermenting in a closed tank; 상기 발효단계에서 발효된 발효액을 추출하는 추출단계;An extraction step of extracting the fermentation broth fermented in the fermentation step; 상기 추출단계를 거친 발효액에 수용성붕소와 수용성몰리브덴을 첨가하고, 침전시키는 침전단계;Precipitating step of adding the water-soluble boron and water-soluble molybdenum to the fermentation broth after the extraction step, and to precipitate; 휴믹산, 키토산, 효소, 미네랄을 혼합하고 교반하는 교반단계;A stirring step of mixing and stirring humic acid, chitosan, enzymes and minerals; 상기 침전단계를 거친 발효액에 질소비료, 인산비료, 칼리비료를 추가하여 질소(N):인산(P):칼리(K)의 비율을 조절하는 비료성분조절단계;를 갖되,By adding nitrogen fertilizer, phosphate fertilizer, califer fertilizer to the fermentation broth after the precipitation step, a fertilizer component adjusting step of adjusting the ratio of nitrogen (N): phosphoric acid (P): Kali (K); 상기 교반단계의 교반시간은 2~3시간이며, 상기 휴믹산, 키토산, 효소, 미네랄은, 각각 상기 침전단계를 거친 발효원액 중량의 0.05~2%, 0.05~2%, 1~3%, 0.05~2%인 것을 특징으로 하는 아미노산 액체비료 제조방법.The stirring time of the stirring step is 2 to 3 hours, the humic acid, chitosan, enzymes, minerals, respectively 0.05 ~ 2%, 0.05 ~ 2%, 1 ~ 3%, 0.05 ~ Amino acid liquid fertilizer manufacturing method characterized in that 2%. 제1항에 있어서,The method of claim 1, 상기 발효단계에서,In the fermentation step, 상기 당분공급원은, 탈지강, 콩박, 피마자박, 밀기울, 대두박 중 어느 하나 또는 둘 이상을 포함하며,The sugar source, any one or two or more of skim steel, soybean meal, castor meal, bran, soybean meal, 상기 발효균은, 바실러스속 또는 사카라마이세스속에 속하는 미생물이며,The fermentation bacteria are microorganisms belonging to the genus Bacillus or Saccharomyces, 상기 발효균의 투입량은, 상기 당분공급원 1톤당 10 내지 30g인 것을 특징으로 하는 아미노산 액체비료 제조방법.The amount of the fermentation bacteria is amino acid liquid fertilizer manufacturing method characterized in that 10 to 30g per ton of sugar source. 제1항에 있어서,The method of claim 1, 상기 침전단계에서,In the precipitation step, 상기 수용성붕소는, 상기 추출단계의 발효액 전체 중량의 0.5~1%이며,The water-soluble boron is 0.5 to 1% of the total weight of the fermentation broth of the extraction step, 상기 수용성몰리브덴은, 상기 추출단계의 발효액 전체 중량의 0.1~0.5%이며,The water-soluble molybdenum is 0.1 ~ 0.5% of the total weight of the fermentation broth of the extraction step, 상기 수용성붕소와 수용성몰리브덴을 첨가한 발효액 전체 중량의 40~60%에 해당하는 물을 혼합하는 것을 특징으로 하는 아미노산 액체비료 제조방법.A method for producing an amino acid liquid fertilizer, characterized in that for mixing water corresponding to 40 to 60% of the total weight of the fermentation broth added with the water-soluble boron and water-soluble molybdenum. 제1항 내지 제3항 중 어느 한 항에 있어서,The method according to any one of claims 1 to 3, 상기 비료성분조절단계에서,In the fertilizer component control step, 질소(N):인산(P):칼리(K)의 비가 3.5~4.5 : 1.5~2.5 : 1.5~2.5가 되도록 하는 것을 특징으로 하는 아미노산 액체비료 제조방법.A method for producing an amino acid liquid fertilizer, characterized in that the ratio of nitrogen (N): phosphate (P): cali (K) is 3.5 to 4.5: 1.5 to 2.5: 1.5 to 2.5. 삭제delete 삭제delete 삭제delete 삭제delete
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