KR20230174774A - Manufacturing Method of Petides and Amino acids Derived from Cocoon or Insect - Google Patents

Abstract

The method for producing peptides and amino acids using silkworms or insects of the present invention is a technology for producing low-molecular-weight peptides, liquid amino acids, or amino acid powders by hydrolyzing high-molecular-weight proteins present in silkworms or insects, and includes the production time of low-molecular-weight peptides and amino acids, This relates to a high-efficiency, high-purity peptide and amino acid production method that can dramatically increase the production rate.
According to the present invention, the production time of peptides and amino acids is significantly shortened compared to the previous one, and the production rate of high-purity amino acids is improved, as well as the production cost and production rate of high-purity amino acids, so that high-purity amino acids can be used in various fields such as food, cosmetics, and pharmaceuticals. It can be applied.

Description

{Manufacturing Method of Petides and Amino acids Derived from Cocoon or Insect}

The present invention is a technology for producing low-molecular peptides, liquid amino acids, or amino acid powder by hydrolyzing high-molecular-weight proteins present in silkworms or insects. High-efficiency/high-purity peptides and amino acids can dramatically increase the production time and production rate of low-molecular peptides and amino acids. It is about manufacturing method.

Recently, silkworms and insects have emerged as protein sources that replace livestock/livestock protein, and are being commercialized and released on the market as protein foods, and the related industry is rapidly growing.

In particular, silkworm cocoons are made of sericin and fibroin proteins, and development of these proteins to use them as materials for functional food and beverages or as medical materials has recently been actively underway.

However, the technologies so far have either used the silk protein collected from silkworm cocoons in its original form without undergoing any special processing, or used a method of purifying the dissolved fibroin aqueous solution mostly through dialysis, so the production yield during mass production has been reduced. This was uneconomical, and due to the fibrous structural characteristics of silk protein and the arrangement of amino acids, decomposition in the human body was delayed or difficult to decompose, resulting in a decrease in absorption rate and lower value as a functional/medical material. There was this.

According to the prior art, techniques for producing cocoon/insect peptides or amino acids include chemical decomposition methods such as acid hydrolysis and neutral salt decomposition and biological enzymatic decomposition methods.

Although the chemical decomposition method is easily decomposed and has a high yield, it causes water pollution during the manufacturing process and has the problem of not being able to produce functional peptides because even amino acids other than peptides are decomposed during the hydrolysis step. In addition, the enzymatic decomposition method had a problem in that although the process was simple, the decomposition rate was low, resulting in low yield.

As a result, the quality level of related products using silkworms/insects is low, as silkworms or insects are sold in powder form by simply drying and pulverizing them, or the adult insects are sold in dried form, which not only causes discomfort as edible but does not improve the taste or texture. , low-molecular-weight peptide or amino acid production technology using silkworms or insects also had the disadvantage of being uneconomical as the enzyme reaction time was very long, up to 24 to 72 hours, and the amino acid production rate was low at 40-50%, as well as being expensive and having limited uses.

Meanwhile, in the case of silkworms, depending on the part, the cocoon part has a molecular weight of up to 300,000 Da, and the other parts have a molecular weight of around 100,000 Da. In order to decompose proteins with different molecular weights, different enzymes, input ratios, reaction times, temperature, and pH are required. etc. must be applied differently, but in reality, it is bound to be unproductive and uneconomical, and the existing technology does not disclose detailed technologies but only suggests comprehensive manufacturing methods, and the amino acid production rate is very low and the production time is also considerable through specific enzymatic decomposition alone. It was almost impossible to produce high-efficiency, high-purity amino acids using the previous method.

Therefore, by setting temperature management, PH management, type of enzyme, enzyme input ratio, reaction time, etc. to create the best environment for ultra-fine protein particles and enzymatic decomposition for high-efficiency amino acid production, highly efficient peptides and There is a need for a manufacturing method that can produce amino acids.

The matters described as background technology above are only for the purpose of improving understanding of the background of the present invention, and should not be taken as recognition that they correspond to prior art already known to those skilled in the art.

The present invention was devised to solve the problems of the prior art described above, including ultrafine atomization of silkworm or insect protein particles, temperature management to create the best environment for enzymatic decomposition, PH management, type of enzyme, and enzyme injection. The purpose is to provide a manufacturing method that can produce low-molecular-weight peptides or amino acids at a high production rate from high-molecular-weight proteins of silkworms or insects within a short period of time by setting ratios, reaction times, etc.

The technical problems to be achieved by the present invention are not limited to the technical problems mentioned above, and other technical problems not mentioned can be clearly understood by those skilled in the art from the description of the present invention. .

The present invention to solve the problems of the prior art described above includes the steps of pulverizing silkworm or insect protein powder and producing a protein solution: heating the protein solution; A first enzyme reaction step of adding endo type enzyme and exo type enzyme to the protein solution; And a second enzyme reaction step of reintroducing endo type enzyme and exo type enzyme into the protein solution, wherein the endo type enzyme in the second enzyme reaction step And the Exo type enzyme is a silkworm or insect characterized in that the weight percentage relative to the weight of the protein solution is lower than the Endo type enzyme and Exo type enzyme in the first enzyme reaction step, respectively. Provides methods for producing peptides and amino acids.

In the present invention, the protein grinding and protein solution generation steps include dry grinding silkworm or insect protein powder; Mixing the dry-ground protein powder and water into a protein solution at a ratio of 2:8 and then wet-grinding; and pulverizing the wet-ground protein solution with ultrasonic waves.

In the present invention, in the ultrasonic pulverization step, it is preferable to irradiate the protein solution with ultrasonic waves having a frequency in the range of 20 KH to 40 KH for 20 to 60 minutes.

In the present invention, in the heating step of the protein solution, the protein solution is introduced into a reaction tank, and the reaction tank is equipped with an instantaneous heater, and through this, the protein solution is preferably raised and maintained at 55°C to 60°C in a circulatory manner. do.

In the present invention, in the first enzyme reaction step, 2 to 3% by weight of Endo type enzyme and 0.2 to 0.5% by weight of Exo type enzyme relative to the weight of the pulverized protein solution are added to the reaction tank and pH It is desirable to react the enzyme with the protein solution within 3 hours while adjusting between 6-8.

In the present invention, the first enzyme reaction step is preferably maintained at pH 8 for up to 1 hour after enzyme addition, pH 6.0 to 6.5 for 1 to 2 hours, and pH 7 for 2 to 3 hours. .

In the present invention, in the second enzyme reaction step, 1 to 2% by weight of Endo type enzyme and 0.1 to 0.2% by weight of Exo type enzyme based on the weight of the pulverized protein solution are added to the reaction tank, It is desirable to react the enzyme with the protein solution within 1 hour and maintain the pH at 7.

In the present invention, the endo type enzyme is preferably Alcarase, and the exo type enzyme is preferably a flavourzyme.

In the present invention, the temperature in the reaction tank is maintained at 55°C to 60°C, the stirring speed of the stirring propeller mounted inside the side of the reaction tank is 60 to 100 rpm, and the stirring propeller is preferably stirred to rotate in the vertical direction. do.

In the present invention, the second enzyme reaction step is to produce an amino acid peptide mixed solution after irradiating ultrasound with a frequency of 20 to 40 kHz for 15 to 25 minutes to stop the activity of the introduced enzyme 1 hour after the enzyme is added. desirable.

In the present invention, a 1-2% solution of chitosan and an 8-10% solution of citric acid are added to the amino acid peptide mixed solution to coagulate and filter the undegraded proteins and impurities, and the amino acid peptide mixed solution in which the undegraded proteins and impurities are filtered. It is desirable to purify through a filter press to obtain an amino acid solution and an organic cake.

In the present invention, it is preferable to dry the organic cake using a microwave method to obtain a peptide amino acid mixed powder.

The method for producing peptides and amino acids using silkworms or insects of the present invention has the effect of significantly shortening the production time of peptides and amino acids compared to the existing method and greatly improving the production rate of high-purity amino acids.

In addition, according to the present invention, there is a chain effect that can be easily applied to various fields such as food, cosmetics, and pharmaceuticals using high-purity amino acids by improving the production cost and production rate of high-purity amino acids.

The effects of the present invention are not limited to those mentioned above, and other problems not mentioned will be clearly understood by those skilled in the art from the description below.

Figure 1 is a flowchart of a method for producing peptides and amino acids using silkworms or insects according to an embodiment of the present invention.
Figure 2 is a step-by-step flow chart of a method for producing peptides and amino acids using silkworms or insects according to an embodiment of the present invention.
Figure 3 is an external configuration diagram of a reaction tank according to an embodiment of the present invention.
Figure 4 is an internal configuration diagram of a reaction tank according to an embodiment of the present invention.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the attached drawings. Prior to this, the terms or words used in this specification and claims should not be construed as limited to their usual or dictionary meanings, and the inventor should appropriately use the concept of terms to explain his or her invention in the best way. It must be interpreted as meaning and concept consistent with the technical idea of the present invention based on the principle of definability. Therefore, the embodiments described in this specification and the configurations shown in the drawings are only one of the most preferred embodiments of the present invention and do not represent the entire technical idea of the present invention, so at the time of filing the present application, various alternatives are available. It should be understood that equivalents and variations may exist.

Introduction to prior art

According to the enzymatic decomposition method of the prior art, the technology for finely pulverizing polymer protein particles derived from silkworms or insects has not been disclosed.

In addition, according to the conventional enzyme decomposition method, due to the lack of experiments on numerous enzymes that decompose proteins, there is no distinction in the use of endo-type enzymes and exo-type enzymes in most cases, and only one enzyme is used. It was often used. In addition, even if the protein is decomposed by this method, there is a disadvantage that a significant amount of the polymer protein is not converted to amino acids.

Conventionally, it takes more than 2 hours just to heat the temperature of the silkworm powder soluble solution to approximately 60℃, and it must be continuously maintained at 60℃ for a long time, but there is a temperature difference between the center and the surrounding area inside the reaction tank containing the soluble solution. As a result, it used to be a factor in inhibiting enzyme reactions and reducing productivity.

Furthermore, the prior art is not specific about the temperature, pH, and reaction time required for the enzyme reaction depending on the type of enzyme, and does not disclose management or response to temperature and pH changes.

Manufacturing method of the present invention

The method for producing peptides and amino acids using silkworms or insects of the present invention includes the following steps: i) pulverizing protein powder mixed with silkworms or insects and producing a protein solution, ii) heating the protein solution, iii) the protein solution A first enzyme reaction step of adding Endo type enzyme and Exo type enzyme to the protein solution, and iv) Adding Endo type enzyme and Exo type enzyme again to the protein solution. It can be formed including a second enzyme reaction step.

In the present invention, any one or more of the silkworms, silkworm cocoons or their powders, dried silkworms or their powders, and red silkworms or their powders may be applied.

In addition, the above insects may be double-star crickets, grasshoppers, silkworm pupae, white snails, mealworms, white-spotted radish caterpillars (slugs), brown mealworm larvae, rhinoceros beetle larvae, drone pupae, grasshoppers, or powders thereof. It is not necessarily limited to this, and any insect species that contains protein components may be included.

First, in the grinding of silkworm/insect protein powder, the present invention applies a three-stage grinding technology of 'dry grinding, wet grinding, and ultrasonic grinding' to ultrafine the polymer protein particles and greatly expand the specific surface area of the protein particles to enable enzyme It allows to dramatically increase decomposition time and efficiency.

However, just because the protein is decomposed by the grinding process does not mean that all of it is amino acidized, and both endo-type enzymes, which decompose proteins well in a short time, and exo-type enzymes, which increase the amino acid production rate, are appropriately added. This causes an enzyme reaction to occur.

The present invention identifies and optimizes the most efficient Alcarase enzyme and Flavozyme enzyme among Endo Type enzymes and Exo Type enzymes based on the results obtained through experiments. It is applied at an input rate of .

In the present invention, the protein solution (soluble solution) of silkworms/insects is introduced into the reaction tank 100, and while heating the reaction tank 100, the protein solution is continuously passed through the instantaneous heater 70 to produce protein. By raising the temperature of the solution to 55℃~60℃ within 5~10 minutes, the time required to heat the existing soluble solution can be drastically reduced to within a few minutes, thereby dramatically improving productivity.

In this way, in the present invention, the temperature of the protein solution (soluble solution) is managed without deviation by simultaneously using the heating system of the instantaneous heater (70) and the reaction tank (100), so that a highly efficient enzyme reaction is possible without factors that inhibit the enzyme reaction due to temperature. You can hope.

In addition, in the present invention, the first enzyme reaction is divided into the first enzyme reaction and the second enzyme reaction, and the first enzyme, Endo Type enzyme, and the second enzyme, Exo Type enzyme, are used separately or simultaneously at the optimal mixing ratio. A method of inputting the solution is presented, and a method of managing the reaction solution without temperature deviation is presented, as well as a management method according to the appropriate pH of the reaction solution and changes in pH, to enable the production of peptides and amino acids with high purity and high productivity.

Figure 1 is a flowchart of a method for producing peptides and amino acids using silkworms or insects according to an embodiment of the present invention, and Figure 2 is a step-by-step flowchart of a method for producing peptides and amino acids using silkworms or insects according to an embodiment of the present invention. Below, each step will be explained in detail with reference to Figures 1 and 2.

Grinding stage: dry grinding, wet grinding and ultrasonic grinding process

The protein grinding and protein solution generation steps of the present invention include i) dry grinding protein powder mixed with silkworms or insects, ii) mixing the dry grinded protein powder and water into a protein solution at a ratio of 2:8. After wet grinding, and iii) ultrasonically grinding the wet grinded protein solution.

In the present invention, dried silkworm or insect powder, that is, silkworm or insect protein powder from which salt and fat have been removed, is prepared, and this is used as a raw material and pulverized in three steps.

First, the protein powder mixed with silkworms or insects is dry-ground (S10). The dry grinding may use a known dry grinding method.

Next, the dry-ground protein powder and water are mixed into a protein solution at a ratio of 2:8, and then wet-ground (S20). Compared to dry grinding, wet grinding can grind protein particles more finely, and a known wet grinding method can also be used.

However, depending on the needs of the invention, a protein solution may be formed by adjusting the ratio of 15 to 20% by weight of the dry ground protein powder and 80 to 85% by weight of water.

Next, the wet-ground protein solution is ultrasonically ground (S30).

At this time, ultrasonic pulverization can be done using a circular ultrasonic irradiation method (see Figure 4). When the protein solution is irradiated with ultrasonic waves with a frequency ranging from 20 KH to 40 KH for 20 to 60 minutes, the polymer protein particles are ultrafine to the peptide level. It will happen.

In other words, when a 300,000 Da high molecular protein or a 100,000 Da medium/low molecular protein of a silkworm or insect undergoes an ultrasonic pulverization process, they can all be miniaturized into peptide-level ultrafine protein particles, and the high molecular protein and low molecular protein are broken down separately. You can break away from unproductive ways of doing things.

Meanwhile, in the ultrasonic pulverization process, no significant pulverization occurs after 60 minutes even if the ultrasonic time is continuously increased. This is because when the ultrasonic irradiation time passes from about 20 minutes to 60 minutes, the average particle size of the protein becomes uniform and significant pulverization action no longer occurs.

In this way, the ultrasonic pulverized protein solution of the present invention can dramatically increase the enzyme reaction speed and peptide/amino acid production efficiency because the protein particles are ultrafine and the specific surface area is greatly increased. In other words, it can be said that as protein particles become ultrafine, the rate and speed of protein decomposition during enzymatic reactions increases dramatically.

Meanwhile, in the process of irradiating ultrasound, ultrasound destroys pathogens contained in the protein solution in a sterile state, preventing degradation of the enzyme reaction due to pathogens during the enzyme reaction, thereby acting as another major factor in increasing the efficiency of the enzyme reaction. .

The previous sterilization method involved putting a protein solution into a reaction tank, heating it to 100°C, performing a sterilization process for more than an hour, and then lowering the temperature again. This was a wasteful method that required a lot of energy, process steps, and process time. However, in the sterilization process, irradiating the protein solution with ultrasound can prevent waste in the above process and greatly increase productivity.

In the present invention, the ultrasonic pulverization can be performed using a separate ultrasonic generator and irradiation system located outside the reaction tank, but the method is not limited thereto, and the protein solution is placed in the reaction tank 100 according to the needs of the invention. After input, an ultrasonic irradiation process may be performed on the protein solution that is continuously circulated through the ultrasonic generator 30 attached to the reaction tank 100 (see FIG. 4).

The circulating ultrasonic method of Figure 4 is installed outside the reaction tank and irradiates ultrasonic waves while circulating the solution in the tank. Unlike the bath-type ultrasonic method installed inside the reaction tank, temperature control is easy and the solution is The grinding efficiency is high by irradiating ultrasonic waves in a 360-degree direction, and the strong cavitation effect has the advantage of fine grinding, so the grinding efficiency can be increased using the circular ultrasonic method.

Protein solution heating and circulation process

Figure 3 is an external configuration diagram of a reaction tank according to an embodiment of the present invention, and Figure 4 is an internal configuration diagram of a reaction tank according to an embodiment of the present invention.

First, Figure 3 is an external configuration diagram of the reaction tank. By adjusting the controller 19 attached to the outside of the tank, the water level, temperature, pH, and ultrasonic irradiation of the protein solution can be adjusted, and further, the protein concentration of the soluble solution, Amino acid concentration can also be measured.

In addition, the user can check the water level, temperature, pH, ultrasonic irradiation, protein concentration, and amino acid concentration of the protein solution through each indicator outside the reaction tank.

Meanwhile, referring to FIG. 4, a protein solution (soluble solution) in which protein particles have been pulverized is introduced into the reaction tank 100.

The reaction tank 100 is equipped with an instantaneous heater 70 on the side, and through this, the protein solution is controlled to rise and maintain the temperature at 55°C to 60°C in a circulatory manner (S40). Of course, according to the needs of the invention, the reaction tank 100 can operate the hot water boiler system at the same time to more quickly raise the temperature of the protein solution to 55°C to 60°C.

The conventional method is to heat the reaction tank 100 using only a hot water boiler system. It takes several hours or more depending on the capacity of the reaction tank just to heat it to 60°C, and the heated solution is also heated to the core of the reaction tank. The temperature difference between the edges occurred, which was a factor in inhibiting the productivity of the enzyme reaction.

In the present invention, an instantaneous heating method is adopted to raise the protein solution to 60°C within 5 to 10 minutes, greatly contributing to improved productivity by significantly shortening the solution heating time, and the protein solution with the increased temperature is fed back into the reaction tank. By circulating this and preventing temperature differences between the protein solutions in the reaction tank, factors that inhibit the enzyme reaction due to temperature changes are eliminated, thereby improving the enzyme reaction.

As will be described later, during the first and second enzyme reaction processes, the temperature in the reaction tank is maintained at 55°C to 60°C, and the stirring speed of the stirring propeller 51 mounted on the inside of the side of the reaction tank 100 is 60°C to 60°C. Set to 100 rpm, the stirring propeller 51 is stirred to rotate in the vertical direction. Due to this action, the temperature difference of the soluble solution in the reaction tank 100 will be further reduced.

First enzyme reaction process

In the present invention, in the first enzyme reaction step, 2 to 3% by weight of Endo type enzyme and 0.2 to 0.5% by weight of Exo type enzyme based on the weight of the pulverized protein solution are added to the reaction tank and the pH is adjusted. The enzyme is reacted with the protein solution within 3 hours while adjusting between 6-8 (S50).

In order to optimize the enzyme reaction of the heated protein solution, it is necessary to first measure the amount of protein contained in the protein solution. Measure the weight of the protein using a protein mass meter provided in the reaction tank to calculate the optimal amount of enzyme accordingly. will be invested.

In the present invention, Alcarase can be used as the endo type enzyme used in the first enzymatic reaction, and Flavozyme can be used as the exo type enzyme.

Meanwhile, in order to perform an enzyme reaction in a heated protein solution, the temperature of the protein solution is continuously maintained at 55°C-60°C, the stirring speed of the stirring propeller is set to 60rpm-100rpm, and the stirring propeller is stirred in the up and down direction.

This is because the amount of enzyme added is very small compared to the protein solution, and when the enzyme is added, the enzyme remains on the upper surface of the solution and takes a considerable amount of time to spread evenly across the bottom and the entire solution, which is a factor in hindering productivity.

As mentioned above, in the first enzyme reaction step, 2%-3% of the endo type enzyme Alcarase and 0.2%-0.5% of the Exo type enzyme Flavozyme were added. Add in the enzyme and perform the enzyme reaction within 3 hours while adjusting the pH between 6 and 8.

Table 1 below shows the pH adjustment and maintenance time during the first and second enzyme reactions.

Reaction time after enzyme addition appropriate pH note

Primary enzyme reaction

0 to 1 hour

8.0
Accelerated protein breakdown
1~2 hours

6.0~6.5
Accelerating amino acid production
2~3 hours

7.0
telogen
Secondary enzyme reaction
3-4 hours
7.0
Final decomposition of remaining undecomposed amount

In the conventional method, the enzyme reaction was usually carried out at pH 7. Since the pH at which protein decomposition is good and the pH at which amino acid production is good are different, the pH concentration is adjusted according to the time by considering the protein decomposition rate and amino acid production rate during the enzyme reaction. It must be adjusted accordingly to achieve the best productivity and efficiency. Therefore, in the first enzyme reaction step of the present invention, pH is maintained at 8 for 1 hour after enzyme addition to accelerate protein decomposition and amino acid production, and pH is maintained at 6.0 to 6.5 for 1 to 2 hours, and the peptide solution is commercialized. PH is maintained at 7 for 2 to 3 hours as a rest period.

And, as will be described later, in the case of the second enzyme reaction, the pH is maintained at 7 until 1 hour after the enzyme is added for final decomposition of the remaining undigested protein.

Once the first enzyme reaction process is completed, a low-purity peptide solution can be extracted, and it is also possible to commercialize it separately.

Second enzyme reaction process

division
Endo Type Enzyme Exo Type Enzyme Usage
protein breakdown
Amino acid production Enzyme name
Alcarase

Flavorzyme
Optimal response pH
8.0
6.0~6.5
Protein degradation (%)

After 1 hour → 85%
2 hours later → 96%
1 hour later → 56%
2 hours later → 75% Amino acid production (g/L)

After 1 hour →7,7 (g/L)
After 2 hours → 9.5 (g/L)
After 1 hour → 33.9 (g/L)
After 2 hours → 38.8 (g/L) characteristic
Excellent protein decomposition power
Low amino acid vitality
Low protein decomposition ability
Excellent amino acid production ability

As shown in Table 2 above, in the present invention, the Endo type enzyme is for decomposing proteins and the optimal reaction pH is 8.0, and the Exo type enzyme is for producing amino acids and has an optimal reaction. The PH that shows is 6.0~6.5. However, as shown in Table 2 above, if more than 2 hours have passed since the enzyme reaction, the vitality of each enzyme decreases and the enzyme reaction decreases accordingly. After a rest period of about 1 hour, a new endo type The vitality of the enzyme is added by adding 1%-2% of the enzyme Alcarase and 0.1%-0.2% of the Exo type enzyme Flavorzyme (S60).

At this time, if the temperature in the reaction tank is maintained at 55℃~60℃ and the stirring speed of the stirring propeller is set at 60rpm-100rpm and the secondary enzyme reaction is carried out within 1 hour, the amino acid production rate can eventually reach 90%. there is.

In the second enzyme reaction, the pH is maintained at 7 for up to 1 hour after enzyme addition. In the present invention, the second enzyme reaction is not for accelerating protein decomposition or amino acid production, but for final decomposition of the remaining amount of undigested protein. For this purpose, the pH is set to 7 and the enzyme reaction is carried out.

Meanwhile, in the second enzyme reaction step, 1 hour after the enzyme is added, ultrasonic waves with a frequency of 20 to 40 kHz are irradiated through the ultrasonic generator 30 for 15 to 25 minutes to stop the activity of the added enzyme. .

This is because the enzyme activity must be stopped once the secondary enzyme reaction process is completed, and if the enzyme activity is not stopped, it may remain in the product and affect it.

Conventionally, in order to stop enzyme activity, a method was adopted to stop enzyme activity by heating the temperature of the protein solution to 100°C and maintaining it for more than 1 hour, which was a factor in increasing manufacturing costs due to high energy costs and decreased productivity.

Accordingly, by using the ultrasound waves of the present invention to stop enzyme activity, energy costs and time can be significantly reduced, thereby improving productivity and reducing costs.

Once the second enzyme reaction step as described above is completed, a mixture of low-molecular-weight peptides and amino acids is obtained, which can be packaged and commercialized.

Comparative example
Example protein particles
Ultra-fine atomization process
X
Goes through 1st dry grinding, 2nd wet grinding, and 3rd ultrasonic grinding. Enzyme used
Input 1 type of enzyme
Simultaneous injection of Endo Type enzyme and Exo Type enzyme PH management
Fixed at PH 7
Adjustable within PH 6~8 range Enzyme vitality management
X
Addition of second enzyme after 2 hours of enzyme reaction Enzyme reaction time
24 to 72 hours
4 to 5 hours Amino acid production rate
40~50%
over 90 Amino acid purity (content)
32~37%
More than 63% product
Peptide/amino acid mixture
1. Peptide/amino acid mixture
2. Amino acids

Table 3 above contains a comparison between the enzyme reaction experiment according to the conventional method and the enzyme reaction experiment according to the present invention. The silkworm/insect mixed powder used in the above comparative examples and examples was a mixed powder of the same weight within the range of 5 to 10 kg, and the amino acid production rate of the comparative example was 40 to 50%, whereas the amino acid production rate of the present invention was 40 to 50%. More than 90% was measured, and while the amino acid purity of the comparative example was 32-37%, the amino acid purity of the present invention was measured to be more than 63%.

Furthermore, it was confirmed that the product of the comparative example produced only a peptide/amino acid mixture, whereas the product of the example produced not only peptide/amino acid but also amino acid.

Filtration/purification process

Next, a 1-2% solution of chitosan and an 8-10% solution of citric acid were added to the amino acid peptide mixed solution produced through the second enzyme reaction process to coagulate and filter the undegraded proteins and impurities. This filtered amino acid peptide mixed solution is purified through a filter press to obtain a high purity amino acid solution (S70).

In other words, undegraded proteins and impurities may remain in the amino acid peptide mixed solution produced through the secondary enzyme reaction process. Some of the undecomposed proteins and impurities are first coagulated and filtered before passing through the filter press. Chitosan or activated carbon is used as a coagulant.

More specifically, in the present invention, a 1%-2% solution of chitosan is dissolved in an 8%-10% solution of citric acid and used for aggregation of undecomposed proteins and impurities. Since chitosan has an antibacterial effect due to its amino group, the antibacterial effect of amino acid solution can be obtained by using chitosan.

The peptide/amino acid solution in which undecomposed proteins and impurities are aggregated is filtered, and a known filtration method may be adopted.

Then, when the peptide/amino acid solution from which undigested proteins and impurities have been removed is passed through a filter press, a high-purity amino acid solution and an organic cake are formed. In the final amino acid solution, more than 90% of the protein contained in the initially added mixed powder is made up of amino acids. It is a high purity amino acid solution and this amino acid solution is transferred to the packaging process to be commercialized.

In addition, the organic cake is transferred to a drying process to be described later and dried.

Microwave drying process

Next, the organic cake is dried using a microwave method to obtain a peptide amino acid mixed powder (S80).

In the present invention, the organic material drying method is preferably dried using a microwave drying method, which is excellent in terms of drying speed and drying efficiency. However, it is not necessarily limited to this, and hot air drying or spray drying methods may be adopted depending on the needs of the invention. The dried powder can be commercialized by dry grinding it and then transferring it to a packaging process.

As such, the present invention is an innovative manufacturing method that implements production technology of more than 90% production rate of low-molecular peptides or amino acids from high-molecular-weight proteins of silkworms or insects within 4 to 5 hours. It provides a more efficient production method than existing production methods and provides high-purity amino acids. It not only contributes to health by producing , but can also be applied to various fields.

In order to produce highly efficient amino acids, temperature management, PH management, type of enzyme, enzyme input ratio, reaction time, etc. must be specified to create the best environment for ultra-fine atomization of protein particles and enzymatic decomposition, through which highly efficient amino acids can be produced. Implement manufacturing.

In addition, the present invention uses fine grinding of protein particles, endo type enzymes and exo type enzymes in an appropriate ratio, and discloses the optimal temperature, optimal pH, and reaction time sensitive to enzyme reaction to produce high protein from silkworms/insects. We present a method for converting amino acids to high purity with high efficiency.

Although the present invention has been described above in relation to specific embodiments of the present invention, this is only an example and the present invention is not limited thereto. A person of ordinary skill in the technical field to which the present invention pertains may change or modify the described embodiments without departing from the scope of the present invention, and within the scope of equivalency of the technical idea of the present invention and the scope of the patent claims described below. Various modifications and variations are possible.

11: water level indicator 12: temperature indicator
14: PH indicator 15: Protein concentration indicator
16: Ultrasonic indicator 17: Amino acid concentration indicator
18: ON/OFF switch 19: Controller
20: Enzyme injection device 30: Ultrasonic generator
40: Cooling device 50: Stirring rotation shaft
51: stirring propeller 60: circulation motor
70: instantaneous heater 80: hot water
90: cover 100: reaction tank

Claims (13)

Steps of grinding protein powder mixed with silkworms or insects and producing protein solution:
heating the protein solution;
A first enzyme reaction step of adding endo type enzyme and exo type enzyme to the protein solution; and
Including a second enzyme reaction step of re-injecting endo type enzyme and exo type enzyme into the protein solution,
The Endo type enzyme and Exo type enzyme in the second enzyme reaction step are more protein than the Endo type enzyme and Exo type enzyme in the first enzyme reaction step, respectively. A method for producing peptides and amino acids using silkworms or insects, characterized in that the weight percentage relative to the weight of the solution is small.
The method of claim 1, wherein the protein pulverization and protein solution generation steps include:
Dry grinding protein powder mixed with silkworms or insects;
Mixing the dry-ground protein powder and water into a protein solution at a ratio of 2:8 and then wet-grinding; and
ultrasonically pulverizing the wet pulverized protein solution;
A method for producing peptides and amino acids using silkworms or insects, comprising:
The method of claim 2, wherein the ultrasonic pulverization step,
A method for producing peptides and amino acids using silkworms or insects, characterized in that the protein solution is irradiated with ultrasonic waves having a frequency in the range of 20 KH to 40 KH for 20 to 60 minutes.
The method of claim 1, wherein the step of heating the protein solution comprises:
The protein solution is put into a reaction tank, wherein the reaction tank is equipped with an instantaneous heater, and through this, the protein solution is raised and maintained at 55°C to 60°C in a circulatory manner. Peptide and amino acid production using silkworms or insects. method.
The method of claim 1, wherein the first enzyme reaction step is,
Add 2-3% by weight of Endo type enzyme and 0.2-0.5% by weight of Exo type enzyme into the reaction tank and adjust the pH between 6-8 to dissolve the protein within 3 hours. A method for producing peptides and amino acids using silkworms or insects, characterized by reacting enzymes in a solution.
According to clause 5,
A method for producing peptides and amino acids using silkworms or insects, characterized in that pH is maintained at 8 for up to 1 hour after enzyme injection, pH is maintained at 6.0 to 6.5 for 1 to 2 hours, and pH is maintained at 7 for 2 to 3 hours.
The method of claim 1, wherein the second enzyme reaction step is,
1~2% by weight of Endo type enzyme and 0.1~0.2% by weight of Exo type enzyme are added to the reaction tank based on the weight of the pulverized protein solution, and the enzyme is reacted with the protein solution within 1 hour. Method for producing peptides and amino acids using silkworms or insects.
In clause 7,
A method for producing peptides and amino acids using silkworms or insects, characterized in that pH is maintained at 7 for up to 1 hour after enzyme addition.
According to clause 5 or 7,
A method for producing peptides and amino acids using silkworms or insects, characterized in that the endo type enzyme is Alcarase, and the Exo type enzyme is a Flavorzyme.
According to clause 5 or 7,
The temperature in the reaction tank is continuously maintained at 55°C to 60°C, the stirring speed of the stirring propeller mounted inside the side of the reaction tank is 60 to 100 rpm, and the stirring propeller is stirred to rotate in the vertical direction. Method for producing peptides and amino acids using insects.
The method of claim 1, wherein the second enzyme reaction step is,
Peptides and amino acids using silkworms or insects, characterized in that 1 hour after the injection of the enzyme, irradiation of ultrasound with a frequency of 20 to 40 kHz for 15 to 25 minutes is performed to stop the activity of the introduced enzyme, and then an amino acid peptide mixed solution is derived. Manufacturing method.
According to clause 11,
To the amino acid peptide mixed solution, a 1-2% solution of chitosan and an 8-10% solution of citric acid were added to coagulate undiluted proteins and impurities and filter them.
A method for producing peptides and amino acids using silkworms or insects, characterized in that the amino acid peptide mixed solution from which the undecomposed protein and impurities have been filtered is purified through a filter press to produce an amino acid solution and an organic cake.
According to clause 12,
A method for producing peptides and amino acids using silkworms or insects, characterized in that the organic cake is dried using a microwave method to obtain a peptide amino acid mixed powder.