KR20000037208A - Method of making amino acid liquid fertilizer - Google Patents

Method of making amino acid liquid fertilizer Download PDF

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KR20000037208A
KR20000037208A KR1020000019146A KR20000019146A KR20000037208A KR 20000037208 A KR20000037208 A KR 20000037208A KR 1020000019146 A KR1020000019146 A KR 1020000019146A KR 20000019146 A KR20000019146 A KR 20000019146A KR 20000037208 A KR20000037208 A KR 20000037208A
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keratin
mixing
stirring
temperature
amino acid
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KR1020000019146A
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Korean (ko)
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민춘식
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민춘식
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    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05CNITROGENOUS FERTILISERS
    • C05C11/00Other nitrogenous fertilisers

Abstract

PURPOSE: A method for preparing a liquid fertilizer of amino acids is provided which prevents soil acidification, environmental pollution, and lowering of crop productivity. CONSTITUTION: A method comprises the steps of mixing keratin with water in the ratio of 5:1; mixing the keratin solution with NaOH, Ca(OH)2 or KOH in the ratio of 1:0.15 at the temperature of 65-75°C and stirring the mixture for 3 hours to hydrolyze it; adding HNO3, H2SO4, H3PO4 or organic acids to the mixture to adjust the pH to be 7-8; stirring the mixture at the temperature of 50-55°C; mixing the keratin solution with papain and protease in the ratio of 1:0.02 and stirring the mixed solution to decompose the remained keratin; cooling the solution to the room temperature; mixing the solution with urea, H3PO4, K, Fe, Mn, Cu and Zn, and stirring the solution to prepare the liquid fertilizer.

Description

아미노산 액비 제조방법{Method of making amino acid liquid fertilizer}Method of making amino acid liquid fertilizer

본 발명은 아미노산 액비 제조방법에 관한 것으로, 특히 케라틴(Keratin) 단백질을 분해함에 따른 아미노산(amino acid) 수용액에 비료원료를 혼합하여 아미노산 유기질의 액체비료로 제조하도록 된 아미노산 액비 제조방법에 관한 것이다.The present invention relates to a method for producing amino acid liquid fertilizer, and more particularly, to a method for preparing amino acid liquid fertilizer to prepare a liquid fertilizer of amino acid organic by mixing a fertilizer raw material with an aqueous solution of amino acid according to decomposition of keratin (Keratin) protein.

일반적으로 농업분야에서는 화학비료와 농약사용에 따른 토양의 산성화 및 환경오염이 초래되고 또, 병충해에 대한 농작물의 저항약화로 인한 생산성의 저하 및 화학비료와 농약사용에 따른 수요자의 불신 등 많은 문제점이 대두되어 왔었다.In general, the agricultural field causes acidification and environmental pollution of the soil due to the use of chemical fertilizers and pesticides. Also, there are many problems such as lower productivity due to the weakening of crops against pests, and distrust of consumers due to the use of chemical fertilizers and pesticides. It has been emerging.

따라서, 이러한 문제를 해결하기 위한 대체비료로서 부각되고 있는 농작물에 이롭고 환경오염예방을 고려한 유기질 비료의 사용이 점차 증가하고 있는 추세이며, 이러한 유기질 비료는 식물의 성장조절제로 식물성 아미노산이 주류를 이루고 있었다.Therefore, the use of organic fertilizers in consideration of environmental pollution prevention and environmental pollution has been gradually increasing as an alternative fertilizer to solve this problem, these organic fertilizers were the main ingredient of vegetable amino acids as a growth regulator of plants. .

최근에는 인분과 축산분에 톱밥과 음식찌꺼기를 섞어 발효시킨 유기질 비료가 개시되기도 하였으나, 유기질 비료의 사용증가에 대비하여 저렴한 비용이 소요되면서도 다양한 유기질 비료의 개발이 시급한 현안과제이다.Recently, organic fertilizers fermented by mixing sawdust and food waste in servings and livestock meals have been disclosed, but it is an urgent problem to develop various organic fertilizers at a low cost in order to increase the use of organic fertilizers.

이는 화학비료와 농약의 과다사용에 따른 환경오염의 심각한 위기의식과, 먹거리인 농작물의 불신풍토가 팽배해짐에 기인한다.This is attributable to the serious crisis of environmental pollution caused by the overuse of chemical fertilizers and pesticides, and the unbelief of food crops.

따라서, 동물성 단백질을 이용한 유기질 비료가 각광받는 시대적 흐름이 예상된다.Therefore, the trend of the times when organic fertilizers using animal proteins are in the spotlight is expected.

동물성 단백질에서 경(硬)단백질인 모발, 손발톱, 피부 등 소위 각질(角質)이라는 케라틴(Keratin) 단백질은 화장품원료, 흡착제, 영양보강제, 조미료 등에 일부 이용되고 있기도 하나, 물과 중성용매에 잘 녹지 않아 펩신, 트립신 등의 단백질 분해효소의 작용도 잘 받지 않으므로 완전분해가 어렵고 소량이어서 제조시 코스트(cost)가 높아지는 문제점이 따른다.The keratin protein called keratin, which is a light protein of animal protein, such as hair, nails, and skin, is used in cosmetics, adsorbents, nutritional supplements, and seasonings, but it is insoluble in water and neutral solvents. Since it does not receive the action of proteolytic enzymes such as pepsin, trypsin, etc., it is difficult to completely dissolve and a small amount is accompanied by a problem in that the cost increases during manufacturing.

본 발명은 전술한 바와 같은 시류에 대처하기 위한 것으로, 동물성 경단백질인 케라틴을 분해하여 아미노산 수용액(amino acid liquid)화한 후, 비료원료를 혼합하므로써 농작물에 이롭고 환경오염예방을 고려한 아미노산 유기질의 액비(液肥:액체비료)로 제조하도록 된 아미노산 액비 제조방법을 제공함에 그 특징이 있다.The present invention is to cope with the currents described above, and after decomposing the keratin, which is an animal light protein, into an aqueous amino acid liquid, and then by mixing the fertilizer raw materials to the agricultural crops and environmental pollution prevention in consideration of environmental pollution (液肥: liquid fertilizer) is characterized by providing an amino acid liquor manufacturing method to be prepared.

상기 목적을 달성하기 위한 본 발명의 아미노산 액비 제조방법은, 동물성 경단백질인 우모(牛毛), 돈모(豚毛) 등의 케라틴 단백질을 알칼리(Alkali) 가수분해하는 알칼리분해공정(S1)과; 중화제를 이용한 중화공정(S2)과; 효소제를 이용한 효소분해공정(S3)과; 요소(N), 인산(P), 카리(K)와 미량의 원소 Fe, Mn, Cu, Zn 을 혼합하여 복합 아미노산 액비로 제조되는 비료혼합공정(S4)으로 이루어짐을 특징으로 한다.Amino acid liquid fertilizer production method of the present invention for achieving the above object, Alkali hydrolysis of the keratin protein, such as animal hair protein hair wool, pig hair (Alkali) hydrolysis (S1); Neutralization step (S2) using a neutralizing agent; Enzymatic digestion step (S3) using an enzyme; Urea (N), phosphoric acid (P), carry (K) and the trace elements Fe, Mn, Cu, Zn by mixing a fertilizer mixing process (S4) made of a complex amino acid liquid ratio.

도 1은 본 발명의 아미노산 액비 제조 공정도.1 is a manufacturing process of the amino acid liquid fertilizer of the present invention.

* 도면의 주요 부분에 대한 부호의 설명 *Explanation of symbols on the main parts of the drawings

S1 : 알칼리 분해공정S1: alkali decomposition process

S2 : 중화공정S2: neutralization process

S3 : 효소분해공정S3: enzyme digestion process

S4 : 비료혼합공정S4: Fertilizer Mixing Process

이하, 본 발명에 따른 아미노산 액비 제조방법의 바람직한 실시예를 첨부도면에 참조하여 상세히 설명한다.Hereinafter, with reference to the accompanying drawings a preferred embodiment of the amino acid liquor production method according to the present invention will be described in detail.

도 1은 본 발명의 아미노산 액비 제조공정도이다.1 is a manufacturing process of the amino acid liquid ratio of the present invention.

도시된 바와 같이 본 발명의 아미노산 액비 제조공정은, 동물성 경단백질인 우모, 돈모 등의 케라틴 단백질을 이용한다.As shown in the drawing, the amino acid liquor production process of the present invention utilizes keratin proteins, such as wool and pig hair, which are animal light proteins.

경단백질을 단백질 분해효소로 분해하면 케라틴을 얻을 수 있는데, 주요 아미노산은 글루탐산, 알기닌, 시스틴 등이며, 특히 우모(牛毛)중에 함유된 아미노산은 주요 아미노산외에도 다양하다. 그 종류는 아스파라긴산(Aspartic acid), 아르기닌(Arginine), 알리닌(Alanine), 시스틴(Cystine), 글루타민산(Glutamic acid), 글리신(Glycine), 히스티딘(Histidine), 이소루신(Isoleucine), 루신(Leucine), 리신(Lysine), 메티오닌(Methyonine), 플로린(Proline), 페닐알라린(Phenylanine), 세린(Serine), 트레오닌(Threonine), 티로신(Tyrosine), 발린(Valine)이다.Degrading the light protein with proteolytic enzymes can yield keratin, the major amino acids of which are glutamic acid, arginine, cystine, etc. In particular, the amino acids contained in the feathers vary in addition to the main amino acids. Aspartic acid, Arginine, Arginine, Alanine, Cystine, Glutamic acid, Glycine, Histidine, Isoleucine, Leucine ), Lysine (Lysine), Methionine (Methyonine), Florin (Proline), Phenylalanine, Serine, Seronine, Threonine, Tyrosine (Tyrosine), Valine.

이중 시스틴(Cystine), 메티오닌(Methyonine)은 식물의 일조량부족, 설해 등으로 약해진 식물세포의 회복력이 있고 내한, 내병성이 강해지며 과실, 채소의 당도향상과 신선도가 높아진다.Among these, cystine and methionine are resilient to plant cells weakened due to lack of sunshine and snowy plants, cold resistance and disease resistance, and improved sugar and vegetable sweetness.

본 발명에 따른 제조공정의 각 단계는, 상기 우모, 돈모 등의 케라틴 단백질 원료를 물과 혼합한 후, 가열하여 65∼75℃의 온도조건에서 알칼리제로 가성소다 (NAOH), 소석회(CA(OH)2), 가성카리 또는 수산화칼륨(KOH)을 투입해 3시간동안 교반하여 가수분해하는 알칼리분해공정(S1)이 수행된다.In each step of the manufacturing process according to the present invention, the keratin protein raw materials such as feather, pig hair and the like are mixed with water, heated and caustic soda (NAOH), calcined lime (CA (OH) at a temperature condition of 65 ~ 75 ℃ 2 ), caustic or potassium hydroxide (KOH) is added to the alkali decomposition step (S1) is carried out by stirring for 3 hours to hydrolyze.

상기 케라틴 단백질 원료인 우모, 돈모와 물의 혼합비율은 원료:물 = 1:5 이며, 가열은 살균과 균질화를 위한 것이고, 알칼리분해공정(S1)은 1차 분해공정으로 케라틴 조직이 파괴된다.The mixing ratio of feather, pig hair and water, which is the keratin protein raw material, is raw material: water = 1: 5, heating is for sterilization and homogenization, and the alkaline decomposition step (S1) is the primary decomposition step to destroy the keratin tissue.

상기 케라틴 단백질 원료와 알칼리제의 혼합비율은 원료:알칼리제 = 1:0.15 이며, 알칼리분해공정(S1)의 수소이온농도는 11pH 이상이다.The mixing ratio of the keratin protein raw material and the alkali agent is raw material: alkaline agent = 1: 0.15, and the hydrogen ion concentration of the alkali decomposition step (S1) is 11 pH or more.

이어, 전단계인 알칼리분해공정(S1)을 거친 후, 수소이온농도를 7∼8pH 로 조절하고 중화제로 질산(HNO3), 황산(H2SO4), 인산(H3PO4) 또는 유기산을 투입하여 후 공정에서 효소의 작용이 중성을 유지하도록 가열하여 활성이 좋은 50∼55℃의 온도에서 교반하는 중화공정 (S2)을 수행한다.Subsequently, after passing through an alkali decomposition process (S1), the hydrogen ion concentration is adjusted to 7 to 8 pH and neutralized with nitric acid (HNO 3 ), sulfuric acid (H 2 SO 4 ), phosphoric acid (H 3 PO 4 ) or organic acid. After the addition, the neutralization step (S2) of stirring at a temperature of 50 to 55 ° C. with good activity is performed by heating to maintain the neutrality of the enzyme in the subsequent step.

연속해, 전단계인 중화공정(S2)를 거친 후, 50∼55℃의 온도를 유지하면서 효소제로 파파인(Papain), 프로타아제(Protease)를 투입하되, 케라틴 단백질 원료와 효소제의 혼합비율은 원료:효소 = 1:0.02의 비율이며, 1차 알칼리분해후의 잔류하는 미섬유상 케라틴을 단백질 분해효소로 교반하여 2차 완전 분해시키므로써, 2차 가수분해하는 효소분해공정(S3)을 수행한다.Subsequently, after the neutralization step (S2), which is a previous step, papain and protease are added as enzymes while maintaining a temperature of 50 to 55 ° C. The ratio of enzyme = 1: 0.02, and the remaining microfibrous keratin after the first alkaline decomposition was completely decomposed by stirring with proteolytic enzyme to perform the second enzymatic digestion step (S3).

이어, 전단계인 효소분해공정(S3)을 거친 후, 실온으로 냉각하여 요소(N), 인산(P), 카리(K)와 미량의 원소 Fe, Mn, Cu, Zn 을 혼합, 교반하여 용해되게 하므로써, 비료혼합공정(S4)을 수행하는 일련의 단계별 공정을 거쳐 복합 아미노산 액비로서 완성하여 제조되는 것이다.Subsequently, after passing through the enzymatic digestion step (S3), the mixture is cooled to room temperature, and urea (N), phosphoric acid (P), carry (K) and trace elements Fe, Mn, Cu, and Zn are mixed and stirred to dissolve. Therefore, it is completed and manufactured as a complex amino acid liquid ratio through a series of step-by-step processes for carrying out the fertilizer mixing step (S4).

이상 설명한 바와 같이 본 발명의 아미노산 액비 제조방법은, 케라틴 단백질의 완전분해에 따른 제조시의 코스트(cost)를 낮추어 농가의 부담을 줄이며, 이로 인해 유기질 비료의 사용을 권장케 함으로서, 화학비료와 농약사용에 따른 토양산성화 및 환경오염을 방지하고 병충해에 대한 농작물의 저항강화로 인한 생산성 및 실수요자의 신뢰를 향상시키는 뛰어난 효과가 있다.As described above, the method for preparing the amino acid fertilizer of the present invention reduces the burden on the farmhouse by lowering the cost of the preparation due to the complete decomposition of the keratin protein, thereby encouraging the use of organic fertilizers, thereby making chemical fertilizers and pesticides There is an excellent effect to prevent soil acidification and environmental pollution according to use, and to improve productivity and confidence of real users due to enhanced resistance of crops to pests.

Claims (1)

우모, 돈모 등의 케라틴 단백질 원료를 물과 1:5로 혼합한 후, 가열하여 65∼75℃의 온도조건에서 케라틴 단백질 원료와 가성소다(NAOH), 소석회(CA(OH)2), 가성카리 또는 수산화칼륨(KOH)의 알칼리제를 1:0.15의 비율로 투입해 3시간동안 교반하여 가수분해하는 알칼리분해공정(S1)과;After mixing keratin protein raw materials such as wool and pig hair at 1: 5 with water, heating and heating the keratin protein raw materials, caustic soda (NAOH), calcined lime (CA (OH) 2 ), caustic carry at a temperature of 65-75 ° C. Or an alkali decomposition step (S1) in which an alkali agent of potassium hydroxide (KOH) is added at a ratio of 1: 0.15 and stirred for 3 hours to hydrolyze; 전 알칼리분해공정(S1)에서의 수소이온농도를 11pH에서 7∼8pH 로 조절하고 질산(HNO3), 황산(H2SO4), 인산(H3PO4) 또는 유기산 중화제를 투입해 가열하여 50∼55℃의 온도에서 교반하는 중화공정(S2)과;Hydrogen ion concentration in all alkali decomposition process (S1) was adjusted from 11pH to 7-8pH and heated by adding nitric acid (HNO 3 ), sulfuric acid (H 2 SO 4 ), phosphoric acid (H 3 PO 4 ) or organic acid neutralizer A neutralization step (S2) for stirring at a temperature of 50 to 55 ° C; 전 공정에서의 가열온도 50∼55℃를 유지하면서 케라틴 단백질 원료와 파파인(Papain), 프로타아제(Protease)의 효소제를 1:0.02의 혼합비율로 투입해 1차 알칼리분해후의 잔류 미섬유상 케라틴을 단백질 분해효소로 교반하여 2차 완전분해시키므로써, 2차 가수분해하는 효소분해공정(S3)과;While maintaining the heating temperature of 50-55 ° C in the previous step, the keratin protein raw material, the enzyme of papain and protease were added at a mixing ratio of 1: 0.02, and residual microfibrous keratin after primary alkali decomposition was added. Enzymatic digestion step (S3), followed by secondary hydrolysis by stirring with proteolytic enzymes; 전 공정을 거친 후, 실온으로 냉각하여 요소(N), 인산(P), 카리(K)와 미량의 원소 Fe, Mn, Cu, Zn 을 혼합, 교반하여 용해하는 비료혼합공정(S4)으로 제조됨을 특징으로 하는 아미노산 액비 제조방법.After the whole process, the mixture is cooled to room temperature to prepare a fertilizer mixing process (S4) in which urea (N), phosphoric acid (P), carry (K) and trace elements Fe, Mn, Cu, and Zn are mixed, stirred and dissolved. Amino acid liquor manufacturing method characterized in that.
KR1020000019146A 2000-04-12 2000-04-12 Method of making amino acid liquid fertilizer KR20000037208A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100397829B1 (en) * 2001-05-22 2003-09-13 세흥조경산업 (주) Method for restructuring Environment for Peptide
US7776124B2 (en) 2005-10-14 2010-08-17 Archer-Daniels-Midland Company Fertilizer compositions and methods of using
KR101043568B1 (en) * 2010-11-09 2011-06-23 김주대 Method for preparation of organic fertilizer by hydrolysis and fermentation of waste human hair
KR20150043015A (en) * 2013-10-14 2015-04-22 지디켐 주식회사 Composition for processing hair waste of animals and method for processing hair waste of animals
KR101537348B1 (en) * 2014-08-26 2015-07-16 (주)우리비앤비 Disposal Method of Butchery Process By-product
KR102178329B1 (en) 2019-11-01 2020-11-13 (주)우리비앤비 Method of disposing of slaughter by-products

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100397829B1 (en) * 2001-05-22 2003-09-13 세흥조경산업 (주) Method for restructuring Environment for Peptide
US7776124B2 (en) 2005-10-14 2010-08-17 Archer-Daniels-Midland Company Fertilizer compositions and methods of using
US7811352B2 (en) 2005-10-14 2010-10-12 Archer-Daniels-Midland Company Fertilizer compositions and methods of using
KR101043568B1 (en) * 2010-11-09 2011-06-23 김주대 Method for preparation of organic fertilizer by hydrolysis and fermentation of waste human hair
KR20150043015A (en) * 2013-10-14 2015-04-22 지디켐 주식회사 Composition for processing hair waste of animals and method for processing hair waste of animals
KR101537348B1 (en) * 2014-08-26 2015-07-16 (주)우리비앤비 Disposal Method of Butchery Process By-product
KR102178329B1 (en) 2019-11-01 2020-11-13 (주)우리비앤비 Method of disposing of slaughter by-products

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