WO2012118319A2 - Appareil de production d'un fertilisant liquide constitué d'acides aminés en utilisant du sang - Google Patents

Appareil de production d'un fertilisant liquide constitué d'acides aminés en utilisant du sang Download PDF

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Publication number
WO2012118319A2
WO2012118319A2 PCT/KR2012/001490 KR2012001490W WO2012118319A2 WO 2012118319 A2 WO2012118319 A2 WO 2012118319A2 KR 2012001490 W KR2012001490 W KR 2012001490W WO 2012118319 A2 WO2012118319 A2 WO 2012118319A2
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WO
WIPO (PCT)
Prior art keywords
blood
grinding
tank
pipe
fermentation tank
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/KR2012/001490
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English (en)
Korean (ko)
Other versions
WO2012118319A3 (fr
Inventor
박해성
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Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of WO2012118319A2 publication Critical patent/WO2012118319A2/fr
Publication of WO2012118319A3 publication Critical patent/WO2012118319A3/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F1/00—Fertilisers made from animal corpses, or parts thereof
    • C05F1/02—Apparatus for the manufacture
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F1/00—Fertilisers made from animal corpses, or parts thereof
    • C05F1/005—Fertilisers made from animal corpses, or parts thereof from meat-wastes or from other wastes of animal origin, e.g. skins, hair, hoofs, feathers, blood
    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01C—PLANTING; SOWING; FERTILISING
    • A01C3/00—Treating manure; Manuring
    • A01C3/02—Storage places for manure, e.g. cisterns for liquid manure; Installations for fermenting manure
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/40—Treatment of liquids or slurries
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/145—Feedstock the feedstock being materials of biological origin
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Definitions

  • the present invention relates to an amino acid liquid fertilizer production apparatus using blood, and more specifically, the amino acid liquid fertilizer production using the blood to prepare a liquid fertilizer using the blood of the livestock (cow, pig, poultry, etc.) collected from the slaughterhouse Relates to a device.
  • livestock cow, pig, poultry, etc.
  • the blood of livestock is a livestock by-product produced from slaughterhouses, and although it is a useful resource rich in various proteins, it is regulated as a waste under the current law and has a double side requiring proper treatment.
  • animal blood is mainly used for the production of animal protein feed, which is collected from a slaughterhouse and supplied to a dried, powdered blood meal.
  • the blood collected from the slaughterhouse is not only incidentally mixed with blood vessels, tendons, hairs, etc., but also the collected blood itself is easily coagulated. It proceeds and converts more than 99% to about 20 amino acids. At this time, if the grinding is insufficient, the blood is undecomposed and remains as a protein, which is decomposed, resulting in lower odor as well as amino acid conversion.
  • the conventional amino acid liquor manufacturing apparatus has a problem that the grinding means for pulverizing the blood collected in the slaughterhouse is made of a millstone method, that is, two grinding plates are friction type, so that the generation of noise is large, and the power consumption is excessive.
  • the upper part of the supply tank receiving the blood is open, so the blood of the livestock is scattered around the workplace during blood grinding process, and the workplace is not clean, and bad smell (bloody smell) is generated. Due to the large amount of foam generated by the air flowing in together, the antifoaming agent has to be continuously added and recycled to make perfect grinding. The waste water is generated, the production cost is increased by continuously adding the antifoaming agent, there is a problem that the pure amino acid liquor can not be produced by the use of excessive antifoaming agent.
  • the present invention is to solve the above-mentioned problems, the noise generated when pulverizing the coagulation blood of the livestock to produce the amino acid liquor using the blood of the livestock is less noise, using the blood can reduce the consumption of power It is an object to provide an amino acid liquid fertilizer production apparatus.
  • an object of the present invention is to provide an amino acid liquor production apparatus using blood which can significantly reduce the generation of washing waste water generated during the washing of the grinding means and prevent bubbles from being generated by the air introduced during the grinding process. .
  • an object of the present invention is to provide an amino acid liquor manufacturing apparatus using the blood to prevent the energy is wasted by heating the hot water by installing a heating pipe directly in the hot water layer of the fermenter to maintain or control the internal temperature of the fermentor. It is done.
  • an inlet tank having an opening into which semi-solid blood is introduced, a grinding means for receiving and grinding a semi-solid blood from the inlet tank, and a blood clot pulverized from the grinding means.
  • a fermentation tank for supplying fermentation and vacuum means provided on one side of the fermentation tank to decompress the inside of the fermentation tank to a vacuum state, wherein the grinding means is installed on at least one pipe connected to the fermentation tank in the drawing tank.
  • the grinding means may include a grinding tube coupled to a predetermined position in the longitudinal direction of the pipe, a driving motor having one end coupled to an upper portion of the grinding tube, and installed at an end of a driving shaft of the driving motor, and accommodated in the grinding tube.
  • Amino acid liquid production plant using blood characterized in that it comprises a grinding blade Chi is provided.
  • a strainer filter is provided between the drawing tank in which the crushing means is installed and the pipe to remove foreign substances contained in the blood stored in the crushing means.
  • the fermentation tank is a housing having a triple jacket structure in which a heat insulation layer and a warm water layer are formed on the outside, a stirrer for mixing the pulverized blood and the additive (microbial enzyme) supplied to the inside of the housing, and a height direction of the housing. Accordingly, at least one baffle plate is provided at a predetermined position on the inner surface, and the hot water layer is provided with at least one heating pipe for heating water contained in the hot water layer along the circumferential direction of the housing.
  • the noise generated when grinding the blood of the animal to produce the amino acid liquid fertilizer using the blood of the animal is less noise, there is an effect that can reduce the consumption of power. .
  • the hot water supplied to maintain or control the internal temperature of the fermentation tank is heated by using a heating pipe in the hot water layer of the fermentation tank to prevent the waste of energy.
  • FIG. 1 is a schematic diagram showing a schematic configuration of an amino acid liquid fertilizer production apparatus according to an embodiment of the present invention.
  • FIG. 1 is a schematic diagram showing a schematic configuration of an apparatus for preparing amino acid liquid ratio using blood according to an embodiment of the present invention.
  • the amino acid liquor manufacturing apparatus using the blood comprises an introduction tank 100, grinding means 110, fermentation tank 120, vacuum means 130.
  • the introduction tank 100 has an opening formed at the top of the semi-solid blood storage, and is formed in a square or cylindrical shape.
  • Grinding means 110 is crushed by receiving the semi-solid blood from the intake tank 100, the feed tank 100 and the fermentation tank 120 to supply the bleeding introduced into the intake tank 100 to be described later At least one or more are installed on the pipe 140 to connect the.
  • the grinding means 110 is a grinding tube 112 is coupled to a predetermined position in the longitudinal direction of the pipe 140, a drive motor 114, one end is coupled to the upper portion of the grinding tube 112, the drive motor 114 It is provided at the drive shaft (114a) end of the), and comprises a grinding blade 116 accommodated in the grinding tube (112).
  • a strainer filter 150 is provided between the drawing tank 100 in which the crushing means 110 is installed and the pipe 140 to remove foreign substances contained in the blood stored in the crushing means 110. Do.
  • Fermentation tank 120 receives the additives (microbial enzyme) from the inlet (120a) provided at the upper predetermined position of the fermentation tank 120 is pulverized blood supplied from the grinding means 110, stirred and fermented to produce an amino acid liquid fertilizer .
  • the fermenter 120 includes a housing 122 having a triple jacket structure in which a heat insulation layer 122a and a hot water layer 122b are formed inside, and pulverized blood and additives supplied to the inside of the housing 122. It comprises a stirrer 124 to mix and at least one baffle plate 126 provided at a predetermined position on the inner surface along the height direction of the housing 122.
  • protease microbial protease
  • the protease is an enzyme that hydrolyzes protein and peptide bonds and is widely present in tissues, cells, and microorganisms of plants and animals.
  • the heat insulation layer 122a is preferably formed by foaming and filling of a blowing agent such as urethane so that the internal temperature of the fermentation tank 120 is not affected by external temperature changes.
  • the hot water layer 122b is filled with water to control the internal space temperature of the fermentation tank 120, and the hot water layer 122b is provided with at least one water along the circumferential direction of the housing 122 and filled with the hot water layer. It is heated by the heating pipe 128 for heating.
  • the heating pipe 128 is preferably operated in conjunction with the temperature sensor 160 provided in the lower predetermined position of the housing 122.
  • the water filled in the hot water layer 122b is replenished when the water filled in the hot water layer 122b is insufficient due to a water level sensor (not shown) provided at an upper predetermined position of the housing 122. It is preferable.
  • the stirrer 124 has a stirring motor 124a provided on the upper portion of the housing 122, and one end thereof is coupled to the stirring motor 124a so as to receive a rotational force from the stirring motor 124a, thereby increasing the height direction in the interior of the housing 122.
  • the rotating shaft 124b provided along with the plurality of blades 124c coupled to the outer circumferential surface of the rotating shaft 124b at regular intervals along the longitudinal direction of the rotating shaft 124b.
  • At least one baffle plate 126 is provided at a predetermined position on an inner surface along a height direction of the housing 122, and mixing is performed when mixing the pulverized blood and additives (microbial enzyme) supplied to the inside of the housing 122. It serves to generate the vortex to be easily made.
  • the vacuum means 130 is provided on one side of the fermentation tank 120, the pressure inside the fermentation tank 120 to make a vacuum.
  • the inside of the fermentation tank 120 is reduced in pressure so that the bleeding introduced into the drawing tank 100 can be supplied into the fermentation tank 120 via the grinding means 110.
  • the vacuum means 130 is driven to depressurize the inside of the fermentation tank 120 to make a vacuum state, and then put the blood in the draw tank 100. Thereafter, the bleeding introduced into the intake tank 100 is supplied to the fermentation tank 120 through a pipe 140 connecting the intake tank 100 and the fermentation tank 120.
  • the bleeding is supplied to the fermentation tank 120 through the pipe 140 in the inlet tank 100 is crushed by the grinding means 110 provided at a predetermined position in the longitudinal direction of the pipe 140 is moved.
  • the temperature inside the fermenter 120 is preferably about 50 to 70 degrees
  • the decomposition progress time is preferably about 20 to 24 hours after the start of the reaction.
  • the crushing means 110 for crushing the blood accumulated in the inlet tank 100 is installed on the pipe 140 connecting the inlet tank 100 and the fermentation tank 120 to pipeline the process of grinding the blood accumulation It is possible to prevent the contaminants from being scattered around the workplace during the crushing process of contaminated blood, and to prevent contamination of the workplace, and the washing waste water is generated by introducing the waste water generated during washing of the grinding means (possibly a small amount of washing water) into the fermentation tank 120. There is no effect.
  • the antifoaming agent does not need to be added in order to prevent bubbles from being generated due to the inflow of air during grinding, manufacturing costs are reduced, and there is an effect of producing pure amino acid liquid ratio.
  • the hot water layer (heated through a heating pipe 128 provided in the hot water layer 122b without heating the water with a separate hot water boiler or steam boiler to supply the hot water layer (b)
  • the water filled in 122b) can be heated to save energy.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Soil Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Manufacturing & Machinery (AREA)
  • Biochemistry (AREA)
  • Environmental Sciences (AREA)
  • Fertilizers (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

La présente invention concerne un appareil de production d'un fertilisant liquide constitué d'acides aminés en utilisant du sang. L'appareil de production d'un fertilisant liquide constitué d'acides aminés en utilisant du sang selon la présente invention comprend : un réservoir de sang, dont la surface supérieure comprend une ouverture pour introduire du sang de bétail semi-solide ; un moyen de broyage pour recevoir le sang de bétail semi-solide depuis le réservoir de sang et broyer le sang de bétail semi-solide reçu ; une cuve de fermentation, qui reçoit le sang de bétail broyé depuis le moyen de broyage et qui fermente le sang de bétail reçu ; et un moyen d'évacuation agencé sur un côté de la cuve de fermentation pour réduire la pression dans la cuve de fermentation afin de créer un état de vide à l'intérieur de la cuve de fermentation. Un ou plusieurs moyens de broyage sont installés sur le tube qui relie le réservoir de sang et la cuve de fermentation. Le moyen de broyage comprend : un tube de broyage couplé à une portion prédéterminée du tube dans la direction de la longueur ; un moteur d'entraînement, dont une extrémité est couplée au haut du tube de broyage ; et une lame de broyage installée à une extrémité d'un arbre d'entraînement du moteur d'entraînement et logée dans le tube de broyage.
PCT/KR2012/001490 2011-02-28 2012-02-28 Appareil de production d'un fertilisant liquide constitué d'acides aminés en utilisant du sang Ceased WO2012118319A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020110018073A KR101100850B1 (ko) 2011-02-28 2011-02-28 혈액을 이용한 아미노산 액비 제조장치
KR10-2011-0018073 2011-02-28

Publications (2)

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WO2012118319A2 true WO2012118319A2 (fr) 2012-09-07
WO2012118319A3 WO2012118319A3 (fr) 2012-10-26

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KR (1) KR101100850B1 (fr)
WO (1) WO2012118319A2 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111039704A (zh) * 2020-01-14 2020-04-21 周丹 一种复合微生物有机肥生产装置
EP4288397A4 (fr) * 2021-02-02 2025-02-26 Aminorganix, Corp. Engrais à base d'acides aminés, aliment pour animaux et amendement à base de sang et de plumes

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101170745B1 (ko) 2012-04-17 2012-09-17 (주)자연과이레 도축 혈액을 이용한 액상비료 제조기
KR102212453B1 (ko) 2019-01-15 2021-02-04 주식회사 아미노랩 도축혈액을 이용하여 아미노산 액체비료를 제조하는 친환경 장치 및 이를 이용한 아미노산 액체비료의 제조방법
KR102316776B1 (ko) 2019-06-17 2021-10-26 주식회사 동서화학 가축 혈액의 고농축 아미노산 추출 시스템 및 추출 방법

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KR100202285B1 (ko) * 1997-03-17 1999-06-15 김문수 생쓰레기 처리장치
KR200210057Y1 (ko) * 1998-08-12 2001-04-02 한인열 가축 혈분 처리기
JP2001302374A (ja) * 2000-04-20 2001-10-31 Snow Brand Rolly Co Ltd 動植物残渣廃物の処理方法
KR20050117953A (ko) * 2004-06-11 2005-12-15 권성근 동물성 액비의 제조방법 및 제조장치
KR100936626B1 (ko) * 2009-04-21 2010-01-13 오진열 아미노산 액상비료의 제조장치
KR100973154B1 (ko) * 2009-08-31 2010-07-30 김태영 진공 흡입식 음식물 발효 건조장치

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111039704A (zh) * 2020-01-14 2020-04-21 周丹 一种复合微生物有机肥生产装置
CN111039704B (zh) * 2020-01-14 2022-07-12 韩小荣 一种复合微生物有机肥生产装置
EP4288397A4 (fr) * 2021-02-02 2025-02-26 Aminorganix, Corp. Engrais à base d'acides aminés, aliment pour animaux et amendement à base de sang et de plumes

Also Published As

Publication number Publication date
WO2012118319A3 (fr) 2012-10-26
KR101100850B1 (ko) 2012-01-02

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