KR20140010281A - Animality amino acid organic farming materials using butchery blood recycling and manufacturing method produced thereby - Google Patents

Abstract

The present invention relates to animal amino acid organic farming materials produced by recycling blood from butchered animals and a method for producing the same, especially, completely pulverizing and lysing the blood coagulated in the step of collecting animal blood and cutting processing time for producing a final product, and preventing ring-shaped amino acid from destruction. According to the present invention, the animal blood from butchered animals is collected in a certain container, and then the collected blood is finely pulverized into 0.4-0.9 meshes in particle size. Under the temperature condition of 36-75°C, a lyase lysing the blood particles is mixed with the pulverized blood and the mixture is fermented, and then cooled to room temperature. A preservative preventing decomposition and a deodorizing agent are mixed with the cooled blood, and then the final products, amino acid organic farming materials, are produced. [Reference numerals] (S100) Collecting animal blood from a slaughter house; (S110) Inputting the collected blood in a first tank to be firstly pulverized; (S120) Pumping the blood into a second tank, then pulverizing into 0.4-0.9 meshes in particle size; (S130) Pumping the pulverized blood into a third tank, temporarily pausing, then pumping it into a fermentation tank; (S140) Firstly filtering the blood while transferring from the third tank to the fermentation tank; (S150) Adding a lyase in the blood under the temperature condition of 36-75°C ,fermenting, and cooling the blood; (S160) Adding a preservative and a deodorizing agent to the blood cooled in the fermentation tank into room temperature; (S170) Secondarily filtering the blood while transferring from the fermentation tank to a storage tank; (S180) Pumping the blood from the fermentation tank to the storage tank

Description

Animal amino acid organic material through slaughter blood recycling and its manufacturing method {ANIMALITY AMINO ACID ORGANIC FARMING MATERIALS USING BUTCHERY BLOOD RECYCLING AND MANUFACTURING METHOD PRODUCED THEREBY}

The present invention is excellent in growing growth of crops by completely crushing and decomposing the coagulated blood during the collection of livestock blood, reducing the process time for producing the final product, and preventing the destruction of cyclic amino acids that may occur during the process. It relates to an animal amino acid organic material through the slaughter blood recycling exhibiting efficacy and a method for producing the same.

The present invention is excellent in growing growth of crops by completely crushing and decomposing the coagulated blood during the collection of livestock blood, reducing the process time for producing the final product, and preventing the destruction of cyclic amino acids that may occur during the process. It relates to an animal amino acid organic material through the slaughter blood recycling exhibiting efficacy and a method for producing the same.

Livestock (pigs, cattle, etc.) are livestock by-products produced from slaughterhouses, and although they are useful resources rich in various proteins, they are regulated as waste under current legislation.

In Korea, the blood of these livestock is not used as a resource but is mostly discarded, which is a waste of useful protein resources and environmental hazards.

Currently, 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.

Recently, research on the production of organic materials using live blood, that is, not the form of blood powder, that is, livestock's blood itself has been actively conducted. In order to manufacture organic materials using the blood itself (live blood) as the main raw material, After crushing the blood and adding the enzyme, it is necessary to proceed with the decomposition in the reactor.

If the blood of the livestock collected from the slaughterhouse is directly put into the reactor without undergoing the pulverization process of blood, the decomposition by the enzymatic action of the coagulated blood does not proceed properly.

If the decomposition process is not carried out completely, the final product of the organic material is low in amino acid content and uneven composition, and may have an undesirable smell from the organic material, and if the organic material is used in plants or crops, Gases that adversely affect the growth of plants and the like may be generated from harmful residues, and the plants and the like may be killed.

On the other hand, the Republic of Korea Patent Publication No. 2002-0022416 (Invention name: organic fertilizer manufacturing method based on blood powder) in the slaughterhouse blood powder of livestock collected through the fermentation, drying and grinding steps to produce powdered powder, powder processing A method for producing an organic fertilizer is obtained by mixing and fermenting bioceramic, sawdust, rice bran, fermentation station, and photosynthetic microorganisms into the blood.

In addition, Korean Unexamined Patent Publication No. 2002-0089760 (name of the invention: a method for producing an amino acid fertilizer using zeolite) collects the blood of an animal generated in a slaughterhouse and thermally decomposes it with sterilization to maintain a water content of 15% or less. A method for producing an amino acid liquid fertilizer is disclosed in which powdered blood powder is extracted, the blood powder is decomposed, the main component of the fertilizer is dissolved, and zeolite powder, which is a clay mineral, is mixed again.

However, in order to prepare blood powder from the collected livestock's blood, the above method requires not only a separate process of drying and pulverizing, but also excessive salt remains in the fertilizer manufactured by using the salt due to the high salt concentration of the blood itself. When the fertilizer is used in the crop, there is a problem in that the damage caused by the accumulation of salt in the soil occurs.

In addition, the Republic of Korea Patent Publication No. 10-2004-0065201 (name of the invention: manufacturing method of amino acid organic materials) in the blood or carcasses of animals in the proteolytic enzymes chymotrypsin and nitric acid or sulfuric acid in the conditions of high temperature, high pressure Disclosed is a method for preparing an amino acid liquid fertilizer which is neutralized with calcium oxide after treatment.

However, the above method is a forced hydrolysis of the protein by a strong acid which is carried out under severe conditions of high temperature and high pressure. In the process of decomposition, most of the cyclic amino acids are destroyed and are present only in the form of free amino acids. There is a limit that the content of amino acids is low, uneven and ineffective.

In addition, since the liquid fertilizer as a final product shows a strong acid must be neutralized process, salts are accumulated in the liquid fertilizer during the neutralization process, there is a problem that can cause damage during grinding.

In order to solve the above problems, the slaughtered blood is recycled to completely crush and decompose the coagulated blood of livestock, to reduce the process time for producing the final product, and to prevent the destruction of cyclic amino acids in the process. It is a situation that the implementation of animal amino acid organic materials and a method of manufacturing the same through.

The present invention has been proposed in view of the above points, and an object of the present invention is to prevent cyclic amino acids from being destroyed in the process of pulverizing and decomposing blood, thereby providing an excellent effect on the growth of crops on organic materials, the final product. The present invention provides an organic amino acid organic material and a method of manufacturing the same through slaughter blood recycling composed of high content of environmentally friendly animal amino acids.

Another object of the present invention is animal amino acid organic materials through slaughter blood recycling which can improve the fermentation efficiency and advantageous fertilization of organic materials using a nebulizer by completely grinding and decomposing the coagulated blood during the collection of livestock blood and It provides a method for producing the same.

Still another object of the present invention is to provide a method for preparing animal amino acid organic materials through slaughtered blood recycling, which significantly reduces processing time by improving blood grinding process.

In order to achieve the above object, a method of producing animal amino acid organic material through slaughter blood recycling according to the present invention includes: (a) collecting blood of a livestock generated in a slaughterhouse in a predetermined container; (b) pulverizing the particle size of the collected blood in the range of 0.4 to 0.9 mesh; (c) fermenting by mixing a degrading enzyme that decomposes the blood particles in the blood while maintaining the blood in a temperature range of 36 to 75 ℃; (d) cooling the blood to room temperature; (e) mixing a preservative to prevent corruption and deodorant to remove the odor in the blood; wherein, in the step (e), the preservative is 3 to 10 weight of molasses in 100 parts by weight of the blood It is preferable that the addition is carried out by mixing with the outer layer.

In step (c) of the present invention, the degrading enzyme is composed of 0.2 to 1 part by weight of alcalase (external) of 100 parts by weight of blood, and alkalase is 50 to 55 parts by weight of water and propylene. It is preferably configured to include 0.5 to 5 parts by weight of propylene glycol, 0.5 to 2 parts by weight of protease, 1 to 5 parts by weight of sodium formate, and 1 to 3 parts by weight of sorbitol.

In step (e) of the present invention, the deodorant is preferably composed of 0.1 to 1 parts by weight of stevia, 1 to 10 parts by weight of wood vinegar, and 0.1 to 1 parts by weight of charcoal powder, respectively, in 100 parts by weight of blood.

Step (b) of the present invention, (b-1) the first grinding step of pulverizing the rotary blade by putting the collected blood in the primary tank equipped with a rotary blade inside; And (b-2) secondary pulverization, which is connected to the pipe from the primary tank and pumped into a secondary tank equipped with a cutter and grinder therein, and then finely pulverizes the particle size of blood in the range of 0.4 to 0.9 mesh. It is configured to include.

Step (c) of the present invention includes the steps of: (c-1) pumping the blood, which has undergone the second grinding step, from the secondary tank to the tertiary tank connected to the pipe and temporarily waiting; (c-2) pumping blood held in the tertiary tank into a fermentation tank connected to the tertiary tank by piping; And (c-3) injecting a degrading enzyme into the blood introduced into the fermentation tank.

On the other hand, animal amino acid organic material through slaughter blood recycling according to the present invention is preferably produced by any one of the above-described manufacturing method.

Animal amino acid organic material through the slaughtered blood recycling according to the present invention and a manufacturing method thereof,

First, in the process of crushing and decomposing blood, the cyclic amino acid is prevented from being destroyed, and thus, the organic material, which is the final product, is composed of a high content of cyclic eco-friendly amino acid in the organic material, thereby exerting an excellent effect on the growth of crops.

Second, by introducing the alkalase degrading enzyme into the pulverized blood, efficient decomposition of blood particles is achieved even in the temperature range of 36 ~ 75 ℃ where the amino acids are not destroyed.

Third, the preservatives of molasses-containing preservatives are incorporated into the decomposed blood to improve the shelf life of the final product, and the deodorant consisting of stevia, wood vinegar, and charcoal is mixed into the decomposed blood and usability of the final product Will improve.

Fourth, it is possible to improve the efficiency of fermentation by completely grinding and decomposing the coagulated blood of the livestock.

Fifth, it can be advantageous to fertilize the organic materials using the sprayer.

Sixth, the process time can be significantly reduced by pulverizing and decomposing blood through an improved process divided into a primary tank, a secondary tank, a tertiary tank, a fermentation tank, and a storage tank.

1 is a flow chart of an animal amino acid organic material manufacturing process through slaughter blood recycling according to the present invention,
2 is a schematic configuration diagram of an apparatus for manufacturing animal amino acid organic material through slaughter blood recycling according to the present invention.

Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.

1 is a flowchart of an animal amino acid organic material manufacturing process through slaughter blood recycling according to the present invention, [2] is a schematic configuration of an apparatus for producing animal amino acid organic material through slaughter blood recycling according to the present invention Shows a figure.

Animal amino acid organic material through slaughter blood recycling according to the present invention is prepared through the following process, with reference to [FIG. 1] and [FIG. 2] will be described in detail the manufacturing process of the present invention.

First, slaughter livestock (pork, cattle, etc.) in the slaughterhouse, and then collect the blood of the generated livestock in a certain container (S100).

Preferably, the blood generated during slaughter may be transferred to a low temperature tank lorry and immediately added to the process, and, if necessary, the blood may be stored in a low temperature warehouse of 0 ° C. or lower when stored for a long time.

Since the blood of livestock collected at the slaughterhouse is easily coagulated, it must be crushed before it can be disassembled into the reactor for smooth decomposition.

The grinding process cuts large particles of blood and coagulated blood that are not properly degraded by the action of the enzyme. This pulverization process prevents undesirable odor from the organic material of the present invention, which is the final product, and prevents the generation of gas which is caused by some decay during the fermentation process, that is, adversely affects the growth of crops.

The collected fresh blood is put into the collected blood in the primary tank 10 disposed at a predetermined place to perform primary grinding (S110).

The inside of the primary tank 10 is equipped with a rotary blade, the blood introduced into the primary tank 10 is first pulverized blood particles by the rotary blade.

The primary tank 10 and the secondary tank 20 communicate with each other through a constant pipe, and the blood pulverized primarily from the primary tank 10 is pumped into the secondary tank 20 through the pipe and then particles of blood The secondary grinding is performed to a size of 0.4 to 0.9 mesh or less (S120).

The secondary tank 20 is preferably equipped with a cutter and grinder at the same time. Blood introduced into the secondary tank 20 by the cutting of the cutting machine and the grinding by the grinder is subjected to the secondary grinding step of finely crushing the particle size in the range of 0.4 to 0.9 mesh.

The grinder mounted inside the secondary tank 20 is disposed to be engaged with each other in the upper and lower parts to grind the blood in the form of a millstone, it is possible to efficiently grind the coagulated blood in conjunction with the cutter.

The secondary tank 20 and the tertiary tank 30 communicate with each other through a constant pipe, and the state that the secondary pulverized blood from the secondary tank 20 is pumped to the tertiary tank 30 through the pipe and temporarily waits. After maintaining, the blood in the tertiary tank 30 is pumped to the fermentation tank 40 through the pipe (S130)

The tertiary tank 30 and the fermentation tank 40 communicate with each other through a constant pipe, and a portion of the pipe is disposed with a filter for filtering the blood transferred from the tertiary tank 30 to the fermentation tank 40.

The blood transferred from the tertiary tank 30 to the fermentation tank 40 is subjected to a primary filtration process for filtering particles having a predetermined size or more by the filter (S140). As a result, when the organic material, which is the final product of the present invention, is sprayed through a nozzle equipped with a nozzle, nozzle clogging may be prevented.

The blood in the tertiary tank 30 is pumped to the fermentation tank 40 through a pipe communicating the tertiary tank 30 with the fermentation tank 40, and the fermentation tank 40 maintaining a temperature in the range of 36 to 75 ° C. After fermenting the enzyme into the blood in the) and then cooled to room temperature (S150). Preferably fermentation time is carried out for 5 to 8 hours.

After the reaction of the fermentation in the fermentation tank 40 is finished, it is left in the fermentation tank 40 for about 3 to 4 hours to completely cool to room temperature. This is to naturally sterilize by lowering the blood temperature at the end of the fermentation reaction.

The cooling system may be installed at an adjacent portion of the fermentation tank 40 to quench it within 10 minutes.

This has the effect of reducing the fermentation time of about 3 to 4 hours in the conventional manufacturing process of organic materials using livestock blood.

In the cooling of blood, the blood in the fermentation tank 40 is cooled to room temperature by heat conduction of the body of the fermentation tank 40 by cooling the fermentation tank 40 itself to room temperature.

The degrading enzyme is composed of 0.2 to 1 part by weight of alcalase added to 100 parts by weight of blood, and alkalase is 50 to 55 parts by weight of water and 0.5 to 5 parts by weight of propylene glycol. It is preferably configured to include 0.5 to 2 parts by weight of protease, 1 to 5 parts by weight of sodium formate, and 1 to 3 parts by weight of sorbitol.

When the weight of propylene glycol, protease, sodium formate, and sorbitol, which are constituents of alkalase, is less than the above ratio, the reaction rate is slow because the concentration of alkalase is lower than that of the substrate (protein component of blood). There is a problem that the time of the entire process increases, and the weight of propylene glycol, protease, sodium formate, sorbitol, which are the components of the alkalase, is larger than the above ratio, which is disadvantageous in terms of manufacturing cost due to relatively high cost.

Alcalase, a degrading enzyme, comprises 53 parts by weight of water in 100 parts by weight of blood, 2.5 parts by weight of propylene glycol, 1 part by weight of protease, 2.5 parts by weight of sodium formate, sorbitol most preferably, 2 parts by weight of solbitol.

On the other hand, in the case of the forced decomposition of the harsh conditions (high temperature, high pressure, etc.) by strong acid as in the conventional method, most of the amino acids having a cyclic form among the amino acids essential for the growth of the plant are produced in the organic material, the final product. It is destroyed by the amino acid so that the amino acid is not evenly contained.

Substrate digestion of alkalase, a degrading enzyme of the present invention, is carried out under mild conditions of 36 to 75 ° C. Therefore, the protein component in livestock blood is not only free amino acids but also various peptides such as double peptide type and triple peptide type. Since it is decomposed into amino acids in the form, fertilization is maintained relatively long when fertilizing the organic materials of the present invention.

In addition, during the decomposition of blood by the degrading enzyme alkalase, trace elements such as potassium (K), which are useful for the growth of crops, are chelated with the produced amino acids and absorbed and transferred into the crop body when fertilized in crops. This is very easy, so the advantage is very good.

The process of decomposing blood transferred to the fermentation tank 40 by fermentation proceeds with decomposition while stirring for about 8 to 11 hours. It is about 3 to 4 hours shorter than the existing 12 to 15 hours.

In the case of more than 11 hours, further decomposition is relatively small, leaving no economic benefit. The completion of the decomposition is managed by the pH of the decomposed blood, and after the reaction starts, the pH of the decomposed blood is measured within about 5 to 8 hours, and when the pH reaches the range of 7.5 to 8.0, it is determined that the decomposition is completed. Terminate the reaction.

After the reaction is completed, it is left in the fermentation tank 40 for about 3 to 4 hours to completely cool to room temperature.

In the fermentation tank 40, the blood cooled to room temperature is added and diluted with a preservative to prevent rot and a deodorant to remove odor (S160).

The fermentation tank 40 and the storage tank 50 communicate with each other through a constant pipe, and a portion of the pipe is disposed with a filter for filtering blood transferred from the fermentation tank 40 to the storage tank 50.

Blood transferred from the fermentation tank 40 to the storage tank 50 is subjected to a secondary filtration process to filter out particles of a predetermined size or more by this filter (S170). As a result, when the organic material, which is the final product of the present invention, is sprayed through a nozzle equipped with a nozzle, nozzle clogging may be prevented.

The secondary filtered blood is stored by pumping the storage tank 50 through a pipe communicating the fermentation tank 40 and the storage tank 50 (S180). Blood inside the storage tank 50 is packaged as a finished product through a predetermined distribution process.

The blood decomposition process in the fermentation tank 40 proceeds under anaerobic conditions in which the fermentation tank 40 is sealed. The fermentation tank 40 can be sealed to maintain a temperature suitable for blood decomposition, and furthermore, This will prevent the rot from contacting with air.

In addition, in the fermentation tank 40, by using a preservative mixed with 3 to 10 parts by weight of molasses to 100 parts by weight of blood can be maintained significantly longer than the conventional life of the fermented blood.

In addition, fermentation tank 40 was fermented by adding a deodorant composed of 0.1 to 1 part by weight of stevia, 1 to 10 parts by weight of wood vinegar solution, and 0.1 to 1 part by weight of charcoal powder, respectively, to 100 parts by weight of blood. Eliminating the odor of blood improves the usability of the operator.

Preferably, each tank (10, 20, 30, 40) by installing an air shower ball therein is a step-by-step reaction and after the blood is discharged to the outside, it is possible to clean the remaining blood accumulated.

By providing a plurality of tanks (10, 20, 30, 40) partitioned in each step of the manufacturing process, it is possible to significantly reduce the tact time of the manufacturing process, due to such a quick tack time It is possible to prevent the blood from being finely changed in the manufacturing process.

In addition, by having a plurality of tanks (10, 20, 30, 40) partitioned with each other in the course of the manufacturing process step by step also serves to enable the manufacturing process of the present invention step by step.

Hereinafter, a description will be given of an example of a method for producing animal amino acid organic material through slaughter blood recycling according to the present invention and the physical properties of the animal amino acid organic material prepared through the manufacturing method.

<Examples>

The blood of the livestock generated in the slaughterhouse is collected in a certain container, the particle size of the collected blood is finely pulverized in the range of 0.4 to 0.9 mesh, and the blood is maintained at a temperature range of 60 ° C. 0.5 parts by weight of alcalase (alcalase) is composed of 100 parts by weight of the alkalase, the alkalase is 52.5 parts by weight of water, 2.5 parts by weight of propylene glycol, 1 part by weight of protease And fermented by mixing a decomposition enzyme that decomposes blood particles comprising 2.5 parts by weight of sodium formate, 2 parts by weight of sorbbitol (solbitol), the fermented blood is cooled to room temperature, the blood 100 weight 25 parts by weight of molasses to the part is an antiseptic, which is composed of 0.5 parts by weight of stevia, 5 parts by weight of wood vinegar, and 0.5 parts by weight of charcoal powder, respectively, in 100 parts by weight of blood. Chwije was prepared by mixing an organic material with an amino acid animal slaughter blood recycle.

The results of the component analysis of the 18 amino acids of the animal amino acid organic material prepared as described above are shown in the following [Table 1] (Comparative example is the analysis of the components of the organic material manufactured using commercially available livestock blood powder) Result).

However, the embodiment described in [Table 1] represents an embodiment of the present invention, but there may be other components in addition to the components described in Examples and Comparative Examples shown in Table 1, but 18 kinds of amino acids essential for plant growth Only ingredients excerpts are prepared.

As can be seen in Table 1 above, the amino acid organic material prepared according to the present invention showed a remarkably superior result compared to the conventional organic material in the content of 18 kinds of amino acids essential for plant growth.

In the process of the present invention during the transfer of blood through each tank, some blood attached to the inner circumferential wall of each tank is buried, some blood on the inner circumferential wall of each tank is washed after one cycle of the process Through the outside.

In this way, the total amount of 18 amino acids (21.46% by weight) contained in a certain volume of blood with some blood on the inner circumferential wall of each tank may cause an error of ± 3.

Although the present invention has been described through the preferred embodiments as described above, the present invention is not limited to the above-described embodiments, and those of ordinary skill in the art to which the present invention pertains describe the technical idea of the present invention and the following. Of course, various modifications and variations are possible within the scope of the claims.

10: primary tank 20: secondary tank
30: tertiary tank 40: fermentation tank
50: storage tank

Claims (9)

(a) collecting the livestock blood generated in the slaughterhouse in a predetermined container;
(b) pulverizing the particle size of the collected blood in the range of 0.4 to 0.9 mesh;
(c) fermenting a mixture of a degrading enzyme that decomposes the blood particles in the blood while maintaining the blood in a temperature range of 36 to 75 ° C;
(d) cooling the blood to room temperature; And
(e) mixing a preservative to prevent corruption and deodorant to remove odors in the blood;
In the step (e), the preservative is a method for producing animal amino acid organic material through slaughter blood recycling, characterized in that 3 to 10 parts by weight molasses is mixed with 100 parts by weight of the blood.
The method according to claim 1,
In the step (c), the degrading enzyme is composed of 0.2 to 1 part by weight of alkalase (alcalase) is added to 100 parts by weight of the blood, the alkalase is 50 to 55 parts by weight of water, 0.5 to 5 parts by weight of propylene glycol, 0.5 to 2 parts by weight of protease, 1 to 5 parts by weight of sodium formate, and 1 to 3 parts by weight of sorbitol, Method of producing animal amino acid organic materials through slaughter blood recycling.
The method according to claim 1,
In step (e), the deodorant is slaughtered, characterized in that composed of 0.1 to 1 parts by weight of stevia, 1 to 10 parts by weight of wood vinegar, 0.1 to 1 parts by weight of charcoal powder, respectively, in 100 parts by weight of the blood. Method for producing animal amino acid organic materials through blood recycling.
The method according to claim 1,
The step (b)
(b-1) a primary grinding step of pulverizing the rotary blades by inputting the collected blood in the primary tank equipped with a rotary blade therein; And
(b-2) a secondary pipe connected to the pipe from the primary tank and pumped into a secondary tank equipped with a cutter and a grinder therein, and then finely pulverizing the particle size of the blood in the range of 0.4 to 0.9 mesh; Method of producing an animal amino acid organic material through slaughter blood recycling, characterized in that consisting of; crushing step.
The method according to claim 1,
The step (c)
(c-1) pumping the blood that has passed through the secondary grinding step from the secondary tank to a tertiary tank connected to a pipe and temporarily waiting the blood;
(c-2) pumping the blood held in the tertiary tank into a fermentation tank connected to the tertiary tank by piping; And
(c-3) a step of injecting the degrading enzyme into the blood introduced into the fermentation tank.
The method according to claim 1,
The step (d) is a method for producing animal amino acid organic materials through slaughter blood recycling, characterized in that the fermentation tank itself is cooled to room temperature while the blood is put into the fermentation tank.
The method according to claim 1,
In the step (e), the animal amino acid organic material manufacturing method through slaughter blood recycling, characterized in that the preservative and the deodorant is added to the fermentation tank in the state that the blood is put into the fermentation tank.
The method according to claim 1,
(F) pumping and storing the blood passed through the mixing of the step (e) from the fermentation tank to the storage tank connected to the production of animal amino acids through slaughter blood recycling characterized in that it further comprises Way.
Animal amino acid organic material through slaughter blood recycling prepared by the method of any one of claims 1 to 8.

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