KR20130085803A - A meat protein made by the method of increasing hydrolysis - Google Patents

A meat protein made by the method of increasing hydrolysis Download PDF

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KR20130085803A
KR20130085803A KR1020120006882A KR20120006882A KR20130085803A KR 20130085803 A KR20130085803 A KR 20130085803A KR 1020120006882 A KR1020120006882 A KR 1020120006882A KR 20120006882 A KR20120006882 A KR 20120006882A KR 20130085803 A KR20130085803 A KR 20130085803A
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protein
chicken breast
beef
high pressure
hydrolysis
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KR101367592B1 (en
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김종태
김철진
김남수
조용진
맹진수
안병학
김양하
김인환
이호영
훈희 선우
오현정
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한국식품연구원
주식회사 이노웨이
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23JPROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00Working-up of proteins for foodstuffs
    • A23J3/04Animal proteins
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23JPROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00Working-up of proteins for foodstuffs
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23JPROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00Working-up of proteins for foodstuffs
    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L13/00Meat products; Meat meal; Preparation or treatment thereof
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L13/00Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/40Meat products; Meat meal; Preparation or treatment thereof containing additives
    • A23L13/42Additives other than enzymes or microorganisms in meat products or meat meals
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L13/00Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/40Meat products; Meat meal; Preparation or treatment thereof containing additives
    • A23L13/42Additives other than enzymes or microorganisms in meat products or meat meals
    • A23L13/422Addition of natural plant hydrocolloids, e.g. gums of cellulose derivatives or of microbial fermentation gums
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L13/00Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/40Meat products; Meat meal; Preparation or treatment thereof containing additives
    • A23L13/48Addition of, or treatment with, enzymes
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L13/00Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/50Poultry products, e.g. poultry sausages
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L13/00Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/50Poultry products, e.g. poultry sausages
    • A23L13/52Comminuted, emulsified or processed products; Pastes; Reformed or compressed products from poultry meat
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L13/00Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/50Poultry products, e.g. poultry sausages
    • A23L13/55Treatment of original pieces or parts

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Nutrition Science (AREA)
  • Health & Medical Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Biochemistry (AREA)
  • Microbiology (AREA)
  • Zoology (AREA)
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Abstract

PURPOSE: Meat protein is provided to maximize the digestion-absorption rate of the meat protein having a low molecular weight using high pressure enzyme proteolysis technology. CONSTITUTION: 10-40 wt% of chicken breast for the total weight of water, 0.05-4.0 wt% of proteinase for the total weight of chicken breast, and the balance of water is processed with a high-pressure device to increase the degree of hydrolysis of chicken breast protein. The molecular weight of the chicken breast produced by the previous method is 1,700-2,400 Da. The high-pressure processing is conducted for 4-48 hours at 25-60°C and in the pressure of 25-400 MPa. The hydrolyzed chicken breast protein is mixed with one bio-polymer selected from pectin, alginic acid, xanthan gum, carrageenan, agar, soy protein, cellulose, or guar gum for stabilizing. [Reference numerals] (AA) Meat material; (BB) Grinding; (CC) Hydrating and dispersing; (DD) Adding enzyme; (EE) High pressure enzyme decomposition; (FF) Centrifuging; (GG) Filtration; (HH) Enzyme deactivation; (II) Container packaging; (JJ) Heating; (KK) Protein beverage

Description

육류 단백질의 가수분해도를 높이는 방법에 의해 제조되는 육류 단백질{A MEAT PROTEIN MADE BY THE METHOD OF INCREASING HYDROLYSIS}Meat protein produced by a method of increasing the degree of hydrolysis of meat protein {A MEAT PROTEIN MADE BY THE METHOD OF INCREASING HYDROLYSIS}

본 발명은 육류로부터 얻어지는 단백질을 가수분해함에 있어서,The present invention in hydrolyzing the protein obtained from meat,

물에 대한 기질의 비율 10-40중량%, 기질 대비 파인애플 추출액, 파파야 추출액, 키위 추출액, Alkalase, 및 Flavourzyme으로 이루어지는 군으로부터 선택되는 어느 하나 이상의 단백질 분해효소 0.05-4.0중량%, 잔여량의 물을 고압처리 시간 4-48, 고압처리 압력 25-400MPa, 고압처리 온도 25℃-60℃의 범위에서 고압기를 이용하여 육류 단백질의 가수분해도를 높이는 방법에 의하여 제조되는 분자량이 낮은 육류 단백질에 관한 것이다.10-40% by weight of the substrate to water, 0.05-4.0% by weight of any one or more proteolytic enzymes selected from the group consisting of pineapple extract, papaya extract, kiwi extract, Alkalase, and Flavorzyme to the substrate, the remaining amount of water The present invention relates to a low-molecular weight meat protein produced by a method of increasing the degree of hydrolysis of meat protein using a high pressure machine in a processing time of 4-48, high pressure 25-400 MPa, and high pressure 25 ° -60 ° C.

음식물을 통하여 얻는 단백질은 체내 단백질 합성에 필요한 아미노산을 제공하며, 단백질은 표준 또는 조정 체중당 0.8-1.2 g이 권장섭취량이며 한국인을 위한 권장섭취량에서는 표준 체중당 1.0g의 단백질 섭취를 권장한다. 인체에 단백질 공급은 생체이용률이 높은 양질의 단백질 위주로 공급하는 것을 중요한 목적으로 하고, 열량 제한의 정도가 클수록 단백질 섭취 상태가 중요하다. 체중 조절과 관련하여 체지방이 소모될 때 근육 단백질의 손실도 발생하지만, 단백질을 적절히 섭취하면 손실량을 최소로 줄일 수 있다. Proteins from foods provide amino acids for protein synthesis in the body. Proteins are recommended at 0.8-1.2 g per standard or adjusted weight, and recommended intakes of 1.0 g per standard weight are recommended for Koreans. The supply of protein to the human body is an important purpose to supply mainly high quality protein with high bioavailability, and the greater the degree of caloric restriction, the more important the state of protein intake. Loss of muscle protein occurs when body fat is consumed in relation to weight control, but proper protein intake can minimize the loss.

환자 및 노약자의 경우 면역력 증가를 위하여 신체에 필요한 필수아미노산을 모두 함유하고 있는 양질의 육류 단백질 섭취가 권장된다. 그러나 암이나 당뇨 등과 같은 질병과 투병하는 환자 및 노약자의 경우 약화된 신체적 상태 때문에 소화능력이 정상인에 비하여 현저하게 낮아 소화 및 흡수율이 매우 낮은 것으로 보고되고 있다. 한편, 육류를 고온에서 구운 형태로 섭취할 경우는 구울 때 발생하는 heterocyclic amine류나 연기에서 발생하는 polycyclic aromatic hydrocarbon류, 고기에 함유된 돌연변이 유발 물질인 N-nitro 화합물(NOC)이 알려져 있으며, 하루 100-200g 이상의 적색 고기류 섭취는 대장암 발생율을 12-24% 증가시키는 것으로 보고되었다(Sandhu et al 2001; Norta et al 2002). 또한, 최근 연구결과에 의하면 고기 속에 함유된 헴철이 건강한 사람에게도 NOC 형성을 증가시키는 것으로 밝혀졌다.Patients and seniors are encouraged to eat high-quality meat protein that contains all the essential amino acids necessary for the body to increase immunity. However, patients and seniors who suffer from diseases such as cancer or diabetes have been reported to have very low digestion and absorption rates due to their weakened physical condition compared to normal people. On the other hand, when meat is ingested at high temperatures, heterocyclic amines generated during roasting, polycyclic aromatic hydrocarbons generated from smoke, and N-nitro compound (NOC), which is a mutagen in meat, are known. Red meat intake above -200 g has been reported to increase colorectal cancer incidence 12-24% (Sandhu et al 2001; Norta et al 2002). In addition, recent studies have shown that heme iron in meat increases NOC formation in healthy people.

단백질을 추가로 섭취할 경우 운동능력과 근력 증진효과가 있는 것으로 알려져 최근 다양한 육류 단백질 제품이 출시되어 시장규모가 점진적으로 증가되고 있다. 그러나 단백질 보충용 시판 제품은 대부분 육류 상태가 그대로 보존된 형태로 판매되고 있어, 섭취시 거북하고 부드러운 식감을 주지 못하는 단점이 있다. 따라서 단백질을 가수분해한 액상 형태의 제품이 존재한다면 기호도와 체내 흡수도를 높일 수 있어 기존의 단백질 식품과 차별화된 제품이 될 수 있을 것으로 판단된다. 또한, 단백질 함량이 단위 포장당 정량 함유된 단백질 제품을 섭취할 경우 과다 섭취에서 오는 탄수화물 이용감소 및 운동능력 감소 등과 같은 문제를 방지할 수 있다.Ingestion of additional protein is known to have the effect of improving athletic performance and muscle strength. Recently, various meat protein products have been released and the market size is gradually increasing. However, most commercial products for protein supplementation are sold in a form in which meat is preserved as it is, and has a disadvantage in that it does not give a hard and soft texture when ingested. Therefore, if there is a liquid form of the product hydrolyzed protein can increase the preference and absorption in the body can be a product that is differentiated from the existing protein foods. In addition, ingestion of protein products containing a protein content per unit package can prevent problems such as decreased carbohydrate utilization and reduced exercise ability resulting from excessive intake.

단백질 가수분해물의 소화 및 흡수에 관한 연구에서 10명의 남자노인을 대상으로 가수분해 단백질 (hydrolysate protein)과 원래의 원형 단백질(intact protein)을 비교한 결과, 가수분해 단백질은 원래의 원형 단백질과 비교하여 장에서의 소화 흡수력이 촉진되고 식후의 아미노산의 이용도와 골격근내의 식이 아미노산의 유입이 증가되는 것으로 나타났다(RenKoopman et al 2009). 저분자량 펩타이드가 함유된 가수분해물은 주로 di- 또는 tri-peptide가 주류를 이루고 일부 아미노산으로 구성되어 고영양 및 치료용 소재로 이용되는데(Bhaskar eta al 2007), 이에 따라서 가수분해 단백질은 면역활성을 감소시키는 기능이 있어 중증 알러지 소아용 식이조성물 제조에 사용이 되기도 한다(Mahmoud 1994). 또한, 펩타이드는 체내에 쉽게 흡수되기 때문에 스포츠영양에 있어 최적 질소공급원이 되며, 고도의 생물학적 가치가 있는 펩타이드는 다양한 식이제품의 일반적인 단백질 보조제로서 이용성이 높다(Sliet al 2005). In the study of digestion and absorption of protein hydrolysates, hydrolysate protein and intact protein were compared with 10 male elderly. Digestive absorption in the intestine is promoted and the availability of amino acids after meals and the influx of dietary amino acids in skeletal muscle are increased (RenKoopman et al 2009). Hydrolysates containing low molecular weight peptides are mainly composed of di- or tri-peptides and composed of some amino acids, which are used for high nutrition and therapeutics (Bhaskar eta al 2007). It also has a reducing function, which can be used to make dietary compositions for children with severe allergies (Mahmoud 1994). In addition, since the peptide is easily absorbed into the body, it is an optimal source of nitrogen for sports nutrition, and peptides of high biological value are highly available as general protein supplements in various dietary products (Sliet al 2005).

단백질 가수분해물은 효소, 산 및 알칼리 가수분해 방법으로 획득할 수 있는데, 이중 효소적 가수분해 방법이 산업적 활용성이 가장 크다. 효소적 분해방법은 단백질분해효소를 육류 단백질에 작용시켜 단백질을 용해 및 분열시켜 펩타이드 형태의 용해성 물질을 얻을 수 있다. 이 과정에서 육류의 향미를 증진시키는 아미노산이 방출되기 때문에, 식품산업에서 육류 단백질 가수분해물은 향미증진제 같은 기능성 소재로 이용되고 있다. 또한, 산 및 알칼리 가수분해 방법은 가열처리 과정을 거치게 되는데, 이때 열에 의하여 단백질이 응고(coagulation)되어 단백질 변성에 따른 이화학적 품질특성이 변함과 동시에 생산 수율도 낮아지는 단점이 있다.   Protein hydrolysates can be obtained by enzyme, acid and alkaline hydrolysis methods, of which enzymatic hydrolysis is the most industrially feasible. In the enzymatic digestion method, proteolytic enzymes are applied to meat proteins to dissolve and divide proteins to obtain soluble substances in the form of peptides. In this process, meat protein hydrolyzate is used as a functional material such as flavor enhancer in the food industry because amino acids are released to enhance meat flavor. In addition, the acid and alkali hydrolysis method is subjected to a heat treatment process, in which the coagulation of the protein by heat, the physicochemical quality characteristics due to protein denaturation, and the production yield is also lowered.

최근 식품분야에서 고압기술은 식품 생산공정에 있어 살균 또는 멸균 목적의 범주를 벗어나 비가열 처리방법의 하나로 50℃ 이하의 온도에서 식품 영양소 및 고유성분의 파괴나 손실없이 기능성 식품원료를 저분자화 용해하거나 추출하는 목적으로 활용할 수 있는 기술이 시도되고 있다. 특히 고압처리에 의하여 수용화 및 추출율 증대 효과로 저분자화한 생리활성 물질은 인체의 소화흡수율을 극대화함은 물론 유용 성분의 색상, 향미, 영양성분 등을 유지할 수 있는 장점이 부각되면서 기존 가열처리 공정에 의한 제품과 비교시 기능 특성이 차별화된 제품을 생산할 수 있다. 따라서, 50-500 MPa의 고압 및 50℃의 온도에서 처리대상 원료의 분해에 적절한 효소를 작용시켜 분해할 경우 종래 가열처리 공정에 비하여 고품질의 추출 및 분해물을 생산하는데 있어 생산성 및 효율성을 증진시킬 수 있다. In the food field, high pressure technology is one of the non-heating treatment methods in the food production process, which is a method of non-heating treatment. Techniques that can be utilized for the purpose of extraction have been tried. In particular, biomolecules that have been made low-molecularly by increasing the solubility and extraction rate by high pressure treatment can maximize the digestive absorption rate of the human body and maintain the color, flavor, and nutritional value of useful ingredients. Compared with the product, it is possible to produce a product with different functional characteristics. Therefore, when decomposing by applying an enzyme suitable for the decomposition of the raw material at a high pressure of 50-500 MPa and a temperature of 50 ℃ can improve the productivity and efficiency in producing high quality extraction and decomposition products compared to the conventional heat treatment process. have.

고압조건 300 MPa에서 단백질 분해효소 trypsin은 상압조건보다 활성이 40% 증가하였으나, thermolysin의 경우는 잔존활성이 5% 이하를 보이는 것과 같이 효소의 내압특성은 효소의 작용기작과 밀접한 관계가 있다. 즉, trypsin과 thermolysin효소의 활성부위 구조를 비교해 보면 serine계 단백질 분해효소인 trypsin의 활성부위에는 공유결합만 존재하므로 고압조건에서 파괴되지 않는 반면, metalloprotease의 한 종류인 thermolysin은 아연(Zn)이온이 배위결합에 의하여 활성부위의 아미노산인 histidine과 glutamic acid와 결합을 할 뿐만 아니라 효소의 촉매작용에 있어서 중요한 역할을 한다. 따라서 고압처리는 아연에 의한 배위결합을 파괴하고 그 결과로서 thermolysin은 효소활성을 잃게 되는 것으로 보고되었다(김남수 외, 2010, 한국식품연구원 보고서).     At 300 MPa under high pressure, protease trypsin showed 40% more activity than normal pressure, but thermolysin showed less than 5% residual activity, so the pressure resistance of enzyme was closely related to the mechanism of action. In other words, when comparing the structure of the active site of trypsin and thermolysin enzyme, covalent bonds exist in the active site of trypsin, a serine protease, and it is not destroyed under high pressure conditions, whereas thermolysin, a kind of metalloprotease, is a zinc (Zn) ion. Coordination bonds not only bind the active sites amino acids histidine and glutamic acid, but also play an important role in catalysis of enzymes. Therefore, high-pressure treatment destroys the coordination bonds by zinc, and as a result, thermolysin has been reported to lose enzymatic activity (Kim Nam-su et al., 2010, Korea Food Research Institute).

따라서 본 발명의 목적은 육류로부터 얻어지는 가수분해도가 높은 단백질을 제공함에 있다. It is therefore an object of the present invention to provide a protein with high degree of hydrolysis obtained from meat.

본 발명은 육류로부터 얻어지는 단백질을 가수분해함에 있어서, 물과 기질의 비율 10-40중량%, 기질 대비 단백질 분해효소 0.05-4.0중량%, 잔여량의 물, 고압처리 시간 4-48, 고압처리 압력 25-400MPa, 고압처리 온도 25℃-60℃의 범위에서 고압기를 이용하여 육류 단백질의 가수분해도를 높이는 방법 및 그에 의해 제조되는 가수분해도가 높은 육류 단백질을 제공한다. 이상의 수치한정은 하기의 실시예에 의해 뒷받침된다.In the present invention, in hydrolyzing a protein obtained from meat, the ratio of water and substrate is 10-40% by weight, 0.05-4.0% by weight of protease to substrate, residual amount of water, high-pressure treatment time 4-48, high-pressure treatment pressure 25 Provided are a method of increasing the hydrolyzability of meat protein using a high pressure machine in the range of -400 MPa and a high pressure treatment temperature of 25 ° C.-60 ° C., and a high hydrolyzable meat protein produced thereby. The above numerical limitation is supported by the following examples.

본 발명에서 제안하는 고압효소분해 기술은 저에너지를 사용하여 육류 단백질을 가장 높은 분해율로 추출분리할 수 있어, 이를 이용하여 단백질 음료를 제공할 수 있는 잇점이 있다. 또한 본 발명에 따른 고압효소 단백질 분해기술은 기존의 단백질 추출공정과 비교할 때, 저렴한 비용으로 제조할 수 있어 경제적인 효과가 뛰어난 것으로 판단된다. 또한 가수분해도가 높은 단백질을 제공함으로써 소화흡수율을 극대화할 수 있다.The high-pressure enzymatic decomposition technology proposed in the present invention can extract and isolate meat protein at the highest decomposition rate using low energy, thereby providing a protein drink. In addition, the high-pressure enzyme protein degradation technology according to the present invention can be produced at a low cost compared to the existing protein extraction process, it is determined that the economic effect is excellent. In addition, by providing a high degree of hydrolysis protein digestion absorption can be maximized.

도 1은 본 발명의 방법에 의해 수득되는 단백질 가수분해물의 제조 공정도를 나타낸 것이다.1 shows a manufacturing process diagram of the protein hydrolyzate obtained by the method of the present invention.

이하, 본 발명을 본 발명이 속하는 기술분야에서 통상의 지식을 가지는 자각 용이하게 실시할 수 있도록 상세히 설명한다. 단, 하기 실시예는 본 발명을 예시하는 것일 뿐, 본 발명의 내용이 하기 실시예에 한정되는 것은 아니다.Hereinafter, the present invention will be described in detail so that the present invention can be easily realized with ordinary knowledge in the art. However, the following examples are illustrative of the present invention, and the present invention is not limited to the following examples.

이하의 실시예에서 사용한 육류는 육류 단백질로서 대표적으로 섭취되는 것으로 여겨지는 닭가슴살 및 쇠고기로서 시중에서 구입한 원료의 단백질 함량 분석결과는 [표 1]과 같았다. 이하의 실시예에서는 닭가슴살과 쇠고기를 사용하여 실험한 결과를 나타냈지만, 당업자는 본 발명을 다른 육류에도 적용할 수 있음을 용이하게 이해할 수 있을 것이다.The meat used in the following examples is a chicken breast and beef, which is considered to be typically ingested as a meat protein, the protein content analysis results of commercially purchased raw materials were shown in [Table 1]. In the following examples, the results of experiments using chicken breast and beef are shown, but those skilled in the art will readily understand that the present invention can be applied to other meats.

닭가슴살 및 쇠고기의 단백질 함량Protein Content in Chicken Breast and Beef 닭가슴살chicken breast 쇠고기beef 조단백질 (%)Crude protein (%) 22.022.0 23.623.6

각 과실에 존재하는 단백질 분해효소의 활성도 반응조건은 [표 2]와 같으며, 파인애플의 경우 pH 7.0, 60℃, 키위는 pH 5.0-8.0, 40℃, 파파야는 pH 7.0, 60℃에서 최대 활성을 나타내었다. The reaction conditions of the protease activity present in each fruit are shown in [Table 2], and the maximum activity at pH 7.0 and 60 ℃ for pineapple, pH 5.0-8.0 and 40 ℃ for kiwi and pH 7.0 and 60 ℃ for papaya. Indicated.

과실 추출액중 단백질 분해효소 활성도 반응조건Reaction Conditions of Protease Activity in Fruit Extracts 과실명Error name 반응 온도(℃)Reaction temperature (캜) pH pH 제조사manufacturer 파인애플 추출액Pineapple Extract 40-7040-70 5.0-8.05.0-8.0 Dole, PhilippineDole, Philippine 키위 추출액Kiwi Extract 40-7040-70 5.0-8.05.0-8.0 Zespri, New Zealand Zespri, New Zealand 파파야 추출액Papaya Extract 40-8040-80 5.0-8.05.0-8.0 Dole, PhilippineDole, Philippine

이하의 실시예에서 수득된 단백질 가수분해물은 80-100℃에서 열처리하여 효소를 불활성화 시킨다. 80℃로 효소를 불활성화시킬 경우 30분, 100℃로 불활성화시킬 경우 10분 처리한다. 80℃ 이하로 처리하면 시간을 늘려도 효소가 불활성화되지 아니하며, 100℃에서는 상기 10분에서 충분히 불활성화됨을 확인하였다.The protein hydrolyzate obtained in the following examples is heat treated at 80-100 ° C. to inactivate the enzyme. If the enzyme is inactivated at 80 ° C, it is treated for 30 minutes, and if it is inactivated at 100 ° C, it is treated for 10 minutes. When the treatment was carried out at 80 ° C. or less, the enzyme was not inactivated even with increasing time, and it was confirmed that at 100 ° C., the enzyme was sufficiently inactivated in the 10 minutes.

효소를 불활성화시킨 후 단백질 가수분해물을 0.1-100㎛ 크기의 여과재로 여과하여 단백질 가수분해물을 포함하는 음료를 수득한다.After inactivation of the enzyme, the protein hydrolyzate is filtered through a filter medium of 0.1-100 μm in size to obtain a beverage comprising the protein hydrolyzate.

상기 여과된 단백질 가수분해물은 음료의 식감 및 단백질의 변성을 방지하기 위하여 펙틴, 알긴산, 잔탄검, 카라기난, 한천, 대두단백질, 셀룰로오스 및 구아검으로 이루어지는 군으로부터 선택되는 어느 하나 의 생고분자를 첨가시켜 안정화 시킨다The filtered protein hydrolyzate is added to any one of the raw polymers selected from the group consisting of pectin, alginic acid, xanthan gum, carrageenan, agar, soy protein, cellulose and guar gum in order to prevent the texture of the beverage and the denaturation of protein. Stabilize

상기 액체상태의 단백질 음료는 121℃로 살균시킨다.The liquid protein drink is sterilized at 121 ° C.

과실 추출액 및 상업용 효소의 단백질 함량, Brix 및 역가 측정Determination of Protein Content, Brix and Potency of Fruit Extracts and Commercial Enzymes

과실 추출액 효소에서 얻을 수 있는 단백질 함량, Brix(%) 및 0.6% casein에 대한 역가의 비교는 표 3과 같다. 과실 추출액에 함유되어 있는 단백질의 함량은 파인애플, 키위 및 파파야가 각각 0.46%, 0.53% 및 0.59%로 파파야의 단백질 함량이 가장 높게 나타났다. 그리고 당도를 나타내는 Brix(%)를 보면 파인애플, 키위 및 파파야가 각각 14.6%, 13.5% 및 13.7%로 파인애플이 약간 높은 당도를 나타내었다. 과실 추출액의 역가를 상대 비교해 볼 때 파인애플>키위>파파야의 순으로 파인애플이 130.6(Unit), 키위가 73.8(Unit)를 나타낸 반면, 파파야가 상대적으로 매우 적은 6.1(Unit) 역가를 보였다. 과실 추출액중 역가가 가장 높은 파인애플 추출액과 Aalcalase 2.4L 및 Flavourzyme 500 MG을 상대 비교해 보면 파인애플 추출액보다 각각 14.7 및 14,3배 높은 역가를 나타내었다. Table 3 shows a comparison of the protein content, Brix (%), and 0.6% casein obtained from the fruit extract enzymes. The protein content of the fruit extracts was 0.46%, 0.53% and 0.59% for pineapple, kiwi and papaya, respectively. In Brix (%), which represents sugar content, pineapple, kiwi, and papaya were 14.6%, 13.5%, and 13.7%, respectively. When comparing the titers of the fruit extracts, pineapples were 130.6 (Unit) and kiwis were 73.8 (Unit), while pineapple, kiwi, and papaya were relatively low, while papaya showed relatively low titer of 6.1 (Unit). Comparing pineapple extract with the highest titer among fruit extracts with Aalcalase 2.4L and Flavourzyme 500 MG, the titer was 14.7 and 14,3 times higher than pineapple extract, respectively.

과실 및 상업용 효소의 단백질 함량, Brix 및 역가Protein Content, Brix and Potency of Fruits and Commercial Enzymes 효소명Enzyme name 총단백질 (%)Total protein (%) Brix(%)Brix (%) 활성도
(Unit)2)
Activity
(Unit) 2)
파인애플pineapple 0.46±0.31) 0.46 ± 0.3 1) 14.6±0.314.6 ± 0.3 130.6±3130.6 ± 3 키위Kiwi 0.53±0.40.53 ± 0.4 13.5±0.313.5 ± 0.3 73.8±473.8 ± 4 파파야papaya 0.59±0.30.59 ± 0.3 13.7±0.213.7 ± 0.2 6.1±26.1 ± 2 Alcalase 2.4LAlcalase 2.4L -- -- 1912.7±81912.7 ± 8 Flavourzyme 500 MGFlavorzyme 500 MG -- -- 1859.3±61859.3 ± 6 1) Values are the meansㅁSD of three determinations.
2) Unit : produce to 1μg of tyrosine per 1 minute
1) Values are the means
2) Unit: produce to 1μg of tyrosine per 1 minute

이와 같은 결과로 인하여, 이하의 실시예에서는 파인애플 추출액인 Bromelain만을 사용하여 가수분해도를 측정하였으나 정도의 차이는 있지만 파파야 추출액, 키위 추출액, Aalcalase 2.4L 및 Flavourzyme 500 MG도 육류 단백질의 가수분해도가 Bromelain과 유사하거나 우수할 것으로 예상할 수 있다. 이하의 실시예 5는 그러한 사실을 나타내고 있다.As a result, in the following examples, the degree of hydrolysis was measured using only pineapple extract, Bromelain, but there was a difference in the degree of papaya extract, kiwi extract, Aalcalase 2.4L and Flavourzyme 500 MG. It can be expected to be similar or superior. Example 5 below illustrates this fact.

단백질 가수분해도 측정Protein hydrolysis measurement

본 발명에서 고압조건에서 효소분해에 의한 단백질 가수분해물을 제조함에 있어 가수분해도는 수용성 질소정량법과 아미노산태 질소정량법을 사용하였다. 즉, 수용성 질소정량법은 Kjeldahl 질소정량법을 이용하여 고압처리 후 분해된 수용성 총 질소량을 측정하였다. 시료 3 mL에 진한 황산 12 mL과 분해촉매제를 넣어 420℃에서 1시간 동안 단백질을 분해하였다. 분해액에 과잉의 40% NaOH를 가해 중화·증류하여 유출된 암모니아를 4% 붕산용액에 포집하여 잔존하는 과잉의 NaOH를 0.1N-HCl 표준용액으로 적정하여 분해액에 존재하는 총 질소량을 측정하였다. 아미노산태 질소정량법은 즉, 중성 수용액에서 아미노산에 formaldehyde를 작용시키면 amino기와 formaldehyde가 반응하여 amino기의 염기성이 없어지고 아미노산은 carboxyl기만 남아 산성을 나타내므로 알칼리 표준용액으로 적정하여 아미노산태 질소량을 구할 수 있다. 비이커에 시료용액 10 mL와 증류수 100 mL를 넣어 혼합한 후 pH8.4로 조정하였다. 여기에 pH 8.4로 중화한 formalin 용액 20 mL를 가하여 혼합한 후 0.1N-NaOH 표준용액으로 적정하여 pH 8.4로 조정하였다. In the present invention, in the preparation of protein hydrolyzate by enzymatic digestion under high pressure conditions, the degree of hydrolysis was determined by using water soluble nitrogen determination and amino acid nitrogen determination. That is, the water-soluble nitrogen determination method measured the total amount of dissolved water-soluble nitrogen after high pressure treatment using Kjeldahl nitrogen determination method. 12 mL of concentrated sulfuric acid and a decomposition catalyst were added to 3 mL of the sample to decompose the protein at 420 ° C. for 1 hour. Excess 40% NaOH was added to the digestion solution to neutralize and distill. The ammonia spilled was collected in 4% boric acid solution, and the remaining excess NaOH was titrated with 0.1 N-HCl standard solution to measure the total amount of nitrogen present in the digestion solution. . In the amino acid nitrogen determination method, if formaldehyde is reacted to an amino acid in a neutral aqueous solution, the amino group and formaldehyde react to lose basicity of amino group, and amino acid remains carboxyl group, indicating acidity. have. 10 mL of the sample solution and 100 mL of distilled water were added to the beaker, mixed, and adjusted to pH 8.4. 20 mL of the formalin solution neutralized to pH 8.4 was added thereto, mixed, and titrated with 0.1 N-NaOH standard solution to adjust the pH to 8.4.

아미노산태 질소(%) =

Figure pat00001
Amino acid nitrogen (%) =
Figure pat00001

V1 : 본시험 적정소비량(mL)V 1 : Proper consumption of this test (mL)

V0 : 공시험 적정소비량(mL)V 0 : Empty test titration consumption (mL)

F : 0.1N-NaOH 표준용액의 역가           F: Titer of 0.1N-NaOH Standard Solution

D : 희석배수           D: Dilution factor

S : 시료 채취량(mL)           S: sampling amount (mL)

0.0007 : 0.1N-NaOH 용액 1 mL에 상당하는 질소량(g)
0.0007: Nitrogen content (g) corresponding to 1 mL of 0.1N-NaOH solution

고압 및 효소분해 조건에서 닭가슴살 및 쇠고기 단백질 가수분해도 측정Determination of Chicken Breast and Beef Protein Hydrolysis under High Pressure and Enzymatic Conditions

파인애플에서 추출한 Bromelain(Great Food Co., LTD) 상업용 효소를 사용하여 고압 및 효소분해 조건에서 닭가슴살 및 쇠고기 단백질 가수분해를 실시하였다. 즉, 닭가슴살 및 쇠고기를 습식분쇄기로 30-50 mesh 크기로 마쇄하여 물에 대한 닭가슴살 및 쇠고기의 비율을 10-30중량%, 기질 대비 Bromelain 효소의 농도를 0.01-4.0중량%, 잔여량의 물, 압력 25-200 MPa, 고압처리시간 4-48 시간, 고압분해온도 40-60℃ 조건에서 고압기(TFS-10L, DIMA Puretech Co. Korea)를 이용하여 고압분해를 실시하였다. 고압분해 후 단백질 분해물은 원심분리(5,000g, 30분)하여 회수하고 95℃에서 20분간 효소불활성화 후 50um 크기의 여과재로 여과하고, 121℃에서 가열살균 처리하여 최종 단백질 가수분해물을 획득하였다. 원심분리는 1000-10000×g 범위에서 할 수 있다. 자세한 제조공정도는 도 1과 같다.Chicken breast and beef protein hydrolysis was performed under high pressure and enzymatic conditions using Bromelain (Great Food Co., LTD) commercial enzyme extracted from pineapple. In other words, the chicken breast and beef were crushed to a size of 30-50 mesh using a wet mill, and the ratio of chicken breast and beef to water was 10-30% by weight, the concentration of Bromelain enzyme to substrate was 0.01-4.0% by weight, and the residual amount of water was High pressure decomposition was carried out using a high pressure machine (TFS-10L, DIMA Puretech Co. Korea) at 25-200 MPa pressure, 4-48 hours high pressure treatment time, 40-60 ℃ high pressure decomposition temperature. After digestion, the protein digest was recovered by centrifugation (5,000 g, 30 minutes), the enzyme was inactivated at 95 ° C. for 20 minutes, filtered through a 50 um filter medium, and sterilized at 121 ° C. to obtain a final protein hydrolyzate. Centrifugation can be performed in the range of 1000-10000 × g. Detailed manufacturing process diagram is shown in FIG.

파인애플에서 추출한 Bromelain(Great Food Co., LTD,) 상업용 효소를 기질의 중량에 대하여 0.05중량% 사용하여 고압 및 효소분해 조건에서 닭가슴살 및 쇠고기 단백질 가수분해를 실시하였다. Chicken breast and beef protein hydrolysis was performed under high pressure and enzymatic digestion using 0.05% by weight of Bromelain (Great Food Co., LTD,) commercial enzyme extracted from pineapple based on the weight of the substrate.

닭가슴살 및 쇠고기의 물 비율에 따른 단백질 가수분해도Protein Hydrolysis Degree According to Water Ratio of Chicken Breast and Beef 물에 대한 기질비율 (%)
Substrate Ratio to Water (%)
단백질 가수분해도(%)Protein hydrolysis degree (%)
닭가슴살chicken breast 쇠고기beef 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 아미노태질소Amino nitrogen 아미노태질소Amino nitrogen 1010 40.640.6 98.298.2 23.223.2 90.790.7 1515 42.742.7 95.995.9 25.025.0 92.692.6 2020 43.943.9 99.799.7 26.926.9 98.798.7 2525 43.443.4 91.391.3 25.125.1 89.489.4 3030 39.739.7 92.292.2 22.322.3 87.687.6 4040 39.539.5 90.490.4 22.222.2 86.586.5

*압력:100MPa, 압력처리시간:16시간, 온도:50℃* Pressure: 100 MPa, Pressure treatment time: 16 hours, Temperature: 50 ° C

이상의 표 4를 살펴보면 닭가슴살과 쇠고기의 물에 대한 기질 비율은 10-30%가 적당함을 알 수 있었다. 최대 효과를 가지는 비율은 20%로써 그 이하 또는 그 이상 기질을 첨가하여도 단백질 가수분해도(%)는 증가하지 않음을 알 수 있었다.Looking at the above Table 4, it was found that the ratio of substrate to water of chicken breast and beef is 10-30%. The maximum effect was found to be 20%, and even if less or more substrates were added, the degree of protein hydrolysis (%) did not increase.

물과 기질 전체 중량에 대하여 물과 기질비율 20%, 파인애플 과즙 효소를 이하의 표 7에 나타난 비율로 첨가하여 닭가슴살과 쇠고기 단백질의 가수분해도를 측정하여 그 결과를 표 5에 나타내었다.Water and substrate ratio 20%, pineapple juice enzyme with respect to the total weight of water and substrate was added to the ratio shown in Table 7 below to measure the degree of hydrolysis of chicken breast and beef protein and the results are shown in Table 5.

Bromelain 효소농도에 따른 단백질 가수분해도Protein Hydrolysis Degree According to Bromelain Enzyme Concentration 효소 농도 (%)Enzyme Concentration (%) 단백질 가수분해도(%)Protein hydrolysis degree (%) 닭가슴살chicken breast 쇠고기beef 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 0.010.01 30.530.5 74.274.2 15.415.4 73.673.6 0.030.03 33.433.4 86.586.5 22.622.6 84.784.7 0.050.05 40.140.1 98.798.7 25.225.2 98.898.8 0.070.07 40.640.6 98.598.5 25.325.3 98.898.8 0.10.1 41.741.7 98.198.1 25.425.4 98.498.4 0.20.2 41.541.5 98.498.4 25.525.5 98.398.3 0.50.5 40.740.7 98.298.2 24.824.8 98.498.4 1.01.0 40.840.8 98.398.3 25.225.2 98.598.5 2.02.0 41.141.1 98.498.4 24.824.8 98.298.2 4.04.0 40.340.3 98.398.3 24.124.1 98.298.2

* 압력: 100 MPa, 압력처리시간: 16 시간, 온도: 50℃, 닭가슴살 및 쇠고기의 물에 대한 비율: 20% * Pressure: 100 MPa, Pressure treatment time: 16 hours, Temperature: 50 ° C, Chicken breast and beef water ratio: 20%

표 5에 의하면 효소 첨가량 0.05중량%부터 단백질 가수분해도가 유의성 있게 증가함을 알 수 있으나 효소 첨가량을 그 이상 증가시켜도 단백질 가수분해도는 크게 증가하지 않음을 알 수 있었다. 따라서 경제성까지 고려할 때, 효소 첨가량 0.05%가 가장 적당함을 알 수 있다.According to Table 5, it can be seen that the protein hydrolysis degree increased significantly from 0.05 wt% of the enzyme addition amount, but the protein hydrolysis degree did not increase significantly even if the enzyme addition amount was increased more than that. Therefore, in consideration of economics, it can be seen that the most suitable amount of enzyme addition is 0.05%.

상기 표 5의 실험예와 같은 조건에서 효소 첨가량을 0.05%로 한 것을 달리하고 압력을 25MPa에서 400MPa로 아래와 같이 변경하면서 실험한 결과를 표 6에 나타내었다. Table 6 shows the results of the experiment while changing the amount of the enzyme added to 0.05% under the same conditions as in the experimental example of Table 5 and changing the pressure from 25MPa to 400MPa as follows.

압력변화에 따른 단백질 가수분해도 Protein hydrolysis according to pressure change 압력 (MPa)Pressure (MPa) 단백질 가수분해도(%)Protein hydrolysis degree (%) 닭가슴살chicken breast 쇠고기beef 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 2525 14.714.7 67.467.4 10.310.3 64.664.6 5050 22.622.6 70.270.2 22.422.4 68.468.4 7575 37.737.7 75.875.8 23.823.8 74.274.2 100100 41.841.8 98.798.7 25.725.7 98.398.3 125125 42.942.9 98.898.8 25.925.9 98.498.4 150150 42.442.4 98.898.8 26.326.3 98.398.3 175175 42.642.6 98.898.8 25.625.6 98.398.3 200200 42.542.5 98.898.8 25.725.7 98.498.4 300300 42.642.6 98.898.8 25.825.8 98.598.5 400400 42.642.6 98.898.8 25.725.7 98.598.5

* 닭가슴살 및 쇠고기의 물에 대한 비율: 20%, 압력처리시간: 16 시간, 온도: 50℃, 효소농도 0.05%* Chicken breast and beef to water ratio: 20%, pressure treatment time: 16 hours, temperature: 50 ℃, enzyme concentration 0.05%

이상의 표 6에 의하면 고압의 압력은 100MPa에서 400MPa의 압력에서 가장 우수한 단백질 가수분해도를 나타내었다. 따라서 경제성까지 고려할 때, 100MPa의 압력이 가장 적당함을 알 수 있다. According to the above Table 6, the high pressure showed the best degree of protein hydrolysis at the pressure of 100MPa to 400MPa. Therefore, considering the economics, it can be seen that the pressure of 100MPa is most suitable.

압력의 변화에 따른 단백질 가수분해도는 낮은 압력에서도 효소 첨가량을 높이면 증가됨을 확인할 수 있는 바, 이를 이하의 표 7에서 확인할 수 있다.  The degree of protein hydrolysis according to the change in pressure can be confirmed to increase by increasing the amount of enzyme addition even at low pressure, which can be confirmed in Table 7 below.

효소의 첨가량 변화에 따른 압력변화에 따른 단백질 가수분해도Protein hydrolysis according to pressure change according to the amount of enzyme addition 고압분해 조건Autoclave Condition 단백질 가수분해도(%)Protein hydrolysis degree (%) 닭가슴살chicken breast 쇠고기beef 압력(MPa)Pressure (MPa) 효소농도(%)Enzyme concentration (%) 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 2525 4,04.0 41.641.6 87.587.5 24.924.9 89.189.1 5050 3.53.5 41.741.7 88.288.2 25.425.4 88.488.4 7575 3.03.0 42.442.4 85.585.5 25.825.8 86.286.2

* 닭가슴살 및 쇠고기의 물에 대한 비율: 20%, 압력처리시간: 16 시간, 온도: 50℃* Chicken breast and beef to water ratio: 20%, pressure treatment time: 16 hours, temperature: 50 ℃

상기 표 6의 실험예와 같은 조건에서 압력을 100MPa로 한 것을 달리하고 압력처리 시간을 아래와 같이 변경하면서 실험한 결과를 표 8에 나타내었다. Table 8 shows the results of the experiment while changing the pressure to 100 MPa under the same conditions as in the experimental example of Table 6 and changing the pressure treatment time as follows.

압력처리 시간에 따른 단백질 가수분해도Protein hydrolysis according to pressure treatment time 압력처리(시간)Pressure treatment (time) 단백질 가수분해도(%)Protein hydrolysis degree (%) 닭가슴살chicken breast 쇠고기beef 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 44 13.713.7 36.536.5 10.410.4 33.833.8 88 18.418.4 48.148.1 18.318.3 46.746.7 1616 41.641.6 97.597.5 24.624.6 97.697.6 2424 42.242.2 98.198.1 24.824.8 97.497.4 3232 41.841.8 98.298.2 25.125.1 97.797.7 4848 42.842.8 97.697.6 24.824.8 97.597.5

* 닭가슴살 및 쇠고기의 물에 대한 비율: 20%, 압력: 100 MPa, 온도: 50℃, 효소농도 0.05%* Ratio of chicken breast and beef to water: 20%, pressure: 100 MPa, temperature: 50 ℃, enzyme concentration 0.05%

표 8의 결과에 의하면 16시간부터 단백질 가수분해도가 유의성 있게 증가하였으나 시간을 그 이상 증가하여도 단백질 가수분해도는 크게 향상되지 아니함을 알 수 있었다. 따라서 경제성까지 고려할 때, 16시간의 고압처리가 가장 적당함을 알 수 있다.According to the results of Table 8, although the degree of protein hydrolysis was significantly increased from 16 hours, the protein hydrolysis degree was not significantly improved even after increasing the time. Therefore, considering the economics, it can be seen that the high pressure treatment of 16 hours is most suitable.

압력처리 시간의 변화에 따른 단백질 가수분해도는 적은 처리 시간에서도 효소 첨가량 및 압력을 높이면 증가됨을 확인할 수 있는 바, 이를 이하의 표 9에서 확인할 수 있다.The degree of protein hydrolysis according to the change in pressure treatment time can be confirmed to increase by increasing the amount of enzyme addition and pressure even in a small treatment time, which can be confirmed in Table 9 below.

효소 첨가량의 변화 및 압력의 변화에 따른 압력처리 시간별 단백질 가수분해도.Protein hydrolysis degree according to pressure treatment time according to the change of enzyme addition amount and pressure change. 고압분해조건Autoclave Condition 단백질 가수분해도(%)Protein hydrolysis degree (%) 닭가슴살chicken breast 쇠고기beef 압력(MPa)Pressure (MPa) 효소농도(%)Enzyme concentration (%) 압력처리(시간)Pressure treatment (time) 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 200200 1.51.5 44 42.142.1 88.588.5 25.225.2 87.787.7 300300 1.01.0 88 43.843.8 86.886.8 25.225.2 86.486.4 400400 0.50.5 1616 43.243.2 86.386.3 25.725.7 87.587.5

* 닭가슴살 및 쇠고기의 물에 대한 비율: 20%, 온도: 50℃* The ratio of chicken breast and beef to water: 20%, temperature: 50 ℃

표 6의 실험예에서 압력처리 시간을 16시간으로 하고 압력처리 온도를 아래의 표 10과 같이 변경하면서 단백질 가수분해도를 측정하여 그 결과를 이하의 표 12에 나타내었다..In the experimental example of Table 6, the pressure treatment time was 16 hours, and the degree of protein hydrolysis was measured while changing the pressure treatment temperature as shown in Table 10 below, and the results are shown in Table 12 below.

압력처리 온도에 따른 단백질 가수분해도Protein hydrolysis according to pressure treatment temperature 압력처리온도(℃)Pressure Treatment Temperature (℃) 단백질 가수분해도(%)Protein hydrolysis degree (%) 닭가슴살chicken breast 쇠고기beef 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 2525 22.722.7 62.662.6 10.210.2 58.758.7 3030 24.324.3 68.368.3 10.810.8 64.564.5 4040 27.527.5 72.472.4 11.511.5 71.371.3 4545 35.335.3 76.876.8 22.622.6 75.775.7 5050 41.841.8 98.598.5 24.424.4 97.397.3 5555 41.541.5 98.498.4 24.824.8 97.497.4 6060 42.342.3 98.298.2 25.025.0 97.797.7

* 닭가슴살 및 쇠고기의 물에 대한 비율: 20%, 압력: 100 MPa, 압력처리시간: 16 시간, 효소농도 0.05% * Chicken breast and beef to water ratio: 20%, pressure: 100 MPa, pressure treatment time: 16 hours, enzyme concentration 0.05%

표 10의 결과에 의하면 압력처리 온도 50℃에서부터 단백질 가수분해도가 유의성 있게 증가하였으나 압력처리 온도를 그 이상 상승시켜도 단백질 가수분해도는 크게 증가하지 않음을 알 수 있었다. 따라서 경제성까지 고려할 때, 50℃의 온도가 가장 적당함을 알 수 있다.According to the results of Table 10, the degree of protein hydrolysis was significantly increased from the pressure treatment temperature of 50 ° C., but the degree of protein hydrolysis was not significantly increased even if the pressure treatment temperature was increased above. Therefore, considering the economics, it can be seen that the temperature of 50 ℃ is most suitable.

온도의 변화에 따른 단백질 가수분해도는 높은 압력에서 낮은 온도에서 고압처리할 경우 증가됨을 확인할 수 있는 바, 이를 이하의 표 11에서 확인할 수 있다.The degree of protein hydrolysis according to the change in temperature can be confirmed that it is increased when the high pressure treatment at a low temperature at a high pressure, it can be confirmed in Table 11 below.

압력의 증가에 따른 온도별 단백질 가수분해도Protein hydrolysis degree by temperature with increasing pressure 고압분해조건Autoclave Condition 단백질 가수분해도(%)Protein hydrolysis degree (%) 닭가슴살chicken breast 쇠고기beef 압력처리온도(℃)Pressure Treatment Temperature (℃) 압력(MPa)Pressure (MPa) 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 아미노태질소Amino nitrogen 수용성질소Water soluble nitrogen 2525 400400 42.142.1 85.485.4 24.824.8 86.586.5 3030 300300 43.843.8 87.687.6 25.325.3 87.287.2 4040 200200 41.941.9 86.786.7 25.825.8 87.487.4

* 닭가슴살 및 쇠고기의 물에 대한 비율: 20%, 압력처리시간: 16 시간, 효소농도 0.05%* Chicken breast and beef to water ratio: 20%, pressure treatment time: 16 hours, enzyme concentration 0.05%

기타 효소에 의한 단백질 가수분해도 측정Measurement of protein hydrolysis by other enzymes

파인애플에서 추출한 Bromelain(Great Food Co., LTD), 파파야 추출물인 Collupulin MG, Alkalase 및 Flavourzyme 500MG 등과 같은 상업용 효소를 사용하여 닭가슴살과 쇠고기 단백질 가수분해를 실시하였다. 닭고기 및 쇠고기 각각 20g에 효소 종류, 효소 농도 및 고압처리 시간에 따른 조건으로 가수분해를 실시하였다. 원료 육류에 물을 가하여 최종 용량을 150 mL로 맞추어 100 MPa로 50℃에서 5, 16, 64 시간동안 고압처리 하여 가수분해를 실시하였다. 그 결과 Bromelain과 Collupulin의 경우 파인애플 과즙으로 분해했을 때와 마찬가지로 효소 종류에 대한 가수분해도의 차이가 있음을 알 수 있었다. 또한 고압처리시간에 대해서도 비슷한 경향을 보였는데 고압처리 5시간에서 닭가슴살의 경우 약 15.8-17.3%의 가수분해도를 보인 반면 고압처리 16시간일 경우 40% 이상으로 가수분해도가 증가하였다. 고압처리 64시간의 경우 40% 이상의 가수분해도를 나타내었으나 고압처리시간에 비하여 가수분해도의 증가정도는 만족하지 못하다고 판단된다. 따라서 고압처리시간을 16시간 정도로 하고 각각의 상업용 효소를 혼합한 복합효소 시스템을 사용하는 방법을 고려할 수 있다. 쇠고기의 경우 Collupulin 효소를 사용한 고압 가수분해 처리 64시간 후에도 가수분해도가 각각 24.8% 및 17.1% 정도를 보여 닭고기에 비해 가수분해도가 낮았다. 또한, Alcalase와 Flavourzyme 효소를 사용하였을 때 닭가슴살의 경우 16시간 고압효소 분해시 45.8 및 46.2%의 가수분해도를 보였으며, 쇠고기의 경우는 22.1 및 33%의 가수분해도를 보였다. 한편, Alcalase와 Flavourzyme을 동량비로 혼합한 효소를 사용하여 16시간 가수분해의 경우 닭가슴살 및 쇠고기의 가수분해도는 47.9 및 34.6%로 각각 약간씩 증가하였다. 따라서 고압효소분해 시간을 16시간 이상 유지하는 것은 품질과 생산공정 관리면에서 유리하지 않을 것으로 판단된다. Chicken breast and beef protein hydrolysis was performed using commercial enzymes such as Bromelain (Great Food Co., LTD) extracted from pineapple, Collupulin MG, Alkalase and Flavourzyme 500MG. 20 g of chicken and beef were hydrolyzed under the conditions of enzyme type, enzyme concentration and autoclave time. Water was added to the raw meat, and the final volume was adjusted to 150 mL, and hydrolysis was performed by autoclaving at 100 MPa for 5, 16, and 64 hours at 50 ° C. As a result, it was found that Bromelain and Collupulin had different hydrolytic degrees for the enzyme types as they were digested with pineapple juice. In addition, there was a similar tendency with respect to the high pressure treatment time. In 5 hours of high pressure treatment, the degree of hydrolysis was about 15.8-17.3% for the chicken breast, while the degree of hydrolysis increased to 40% or more for 16 hours of the high pressure treatment. In case of 64 hours of high pressure treatment, the degree of hydrolysis was over 40%, but the degree of increase in hydrolysis degree was not satisfactory compared to the high pressure treatment time. Therefore, a high pressure treatment time of about 16 hours and a method using a complex enzyme system in which each commercial enzyme is mixed may be considered. In the case of beef, the degree of hydrolysis was about 24.8% and 17.1% after 64 hours of high pressure hydrolysis with Collupulin enzyme, respectively. In addition, when Alcalase and Flavorzyme enzyme were used, chicken breast showed 45.8 and 46.2% of hydrolysis at 16 hours of hyperbaric enzyme digestion and 22.1 and 33% of beef. On the other hand, the hydrolysis of chicken breast and beef was slightly increased to 47.9 and 34.6%, respectively, for 16 hours of hydrolysis using enzymes containing Alcalase and Flavorzyme in the same ratio. Therefore, maintaining the high-pressure enzymatic decomposition time for more than 16 hours is not advantageous in terms of quality and production process management.

효소 종류, 농도 및 고압처리 시간에 따른 단백질 가수분해 (unit: %) Protein hydrolysis according to enzyme type, concentration and autoclave time (unit:%) 효소종류 및 첨가량Enzyme Type and Amount 닭가슴살chicken breast 쇠고기beef 고압분해(시간)Autoclave (hours) 고압분해(시간)Autoclave (hours) 55 1616 6464 55 1616 6464 아미노태질소Amino nitrogen 아미노태질소Amino nitrogen Bromelain-0.04%Bromelain-0.04% 15.815.8 40.340.3 42.642.6 11.611.6 24.624.6 24.824.8 0.07%          0.07% 17.317.3 40.640.6 13.613.6 23.723.7 Collupulin-0.04%Collupulin-0.04% 14.814.8 40.440.4 53.053.0 8.48.4 10.210.2 17.117.1 0.07%           0.07% 16.816.8 43.843.8 9.59.5 14.514.5 Alcalase-100㎕Alcalase-100µl 24.524.5 45.845.8 51.151.1 12.212.2 22.122.1 32.532.5 Flavourzyme-100mgFlavorzyme-100mg 19.419.4 46.246.2 55.655.6 17.217.2 33.033.0 36.836.8 Alka.50㎕+Flav.50mgAlka.50 μl + Flav.50 mg 28.728.7 47.947.9 17.217.2 34.634.6

실험결과로 나타내지는 않았지만, α-chymotrypsin, papain, trypsin acetylated, ficin, thermolysin, pancreatin, protease, pepsin, trypsin 등과 같은 단백질 분해효소도 유사한 결과를 나타내었다. Although not shown in the experimental results, proteolytic enzymes such as α-chymotrypsin, papain, trypsin acetylated, ficin, thermolysin, pancreatin, protease, pepsin and trypsin showed similar results.

Bromelain과 Collupulin 효소의 혼합비에 따른 닭가슴살과 쇠고기 단백질 가수분해Hydrolysis of Chicken Breast and Beef Protein by Mixing Ratio of Bromelain and Collupulin Enzymes

표 13에 Bromelain과 Collupulin 효소의 혼합비를 달리하여 첨가하고 기질 20g, 물 80g, 100MPa의 압력, 및 50℃의 온도하에서 16시간 동안 고압처리 하였다. 그 결과 닭가슴살의 경우 모든 혼합효소 조건에서 42~45% 수준의 가수분해도를 나타냈고, 쇠고기의 경우 혼합효소 조건에서 20~26% 범위의 가수분해도를 보였으나, Bromelain 20mg과 Flavourzyme 50 μL의 혼합효소 조건에서는 30%로 높은 가수분해도를 나타내었다.The mixing ratio of Bromelain and Collupulin enzyme was added to Table 13, and the mixture was autoclaved under a temperature of 20 g, 80 g of water, 100 MPa, and 50 ° C. for 16 hours. As a result, in case of chicken breast, the degree of hydrolysis was 42 ~ 45% under all mixed enzyme conditions, and in case of beef, the degree of hydrolysis was in the range of 20 ~ 26% under mixed enzyme conditions. In the enzymatic condition, the degree of hydrolysis was high as 30%.

Bromelain과 Collupulin의 혼합효소에 따른 가수분해도 (unit: %)Hydrolysis Degree According to Mixed Enzyme of Bromelain and Collupulin (unit:%) 혼합효소 종류 및 첨가량Mixed Enzyme Type and Amount 닭가슴살chicken breast 쇠고기beef 아미노태질소Amino nitrogen 아미노태질소Amino nitrogen Bromelain+Collupulin=20mg+20mgBromelain + Collupulin = 20mg + 20mg 43.843.8 20.720.7 Bromelain+Alcalase=20mg+20㎕Bromelain + Alcalase = 20mg + 20μl 44.944.9 24.524.5 Bromelain+Alcalase=20mg+50㎕Bromelain + Alcalase = 20mg + 50μl 42.742.7 22.622.6 Bromelain+Flavourzyme=20mg+20㎕Bromelain + Flavourzyme = 20mg + 20μl 41.641.6 26.426.4 Bromelain+Flavourzyme=20mg+50㎕Bromelain + Flavourzyme = 20mg + 50μl 44.444.4 30.830.8

닭가슴살 및 쇠고기 가수분해물의 분자량 측정Molecular weight measurement of chicken breast and beef hydrolyzate

·GPC를 이용한 단백질 분해액의 분자량 측정Molecular weight measurement of proteolytic solution using GPC

- 고압/효소 처리에 의한 닭고기와 소고기 단백질 분해액의 분자량 측정을 위해 GPC를 이용하였으며 조건은 표 13에 나타내었다. 단백질 분해 후 효소 불활성화 한 여과액을 0.2 μm syringe filter로 여과하여 분석 시료로 사용하였다. 표준물질은 conalbumin(75kDa), ovalbumin(44kDa), carbonic anhydrase(29kDa), ribonuclease A(13.7kDa) 그리고 aprotinin(6.5kDa)을 GE Healthcare(UK)사에서 구입하여 사용하였으며, column의 void volume을 측정하기위해 blue dextran을 사용하였다. -GPC was used to measure the molecular weight of chicken and beef protein digested by high pressure / enzyme treatment and the conditions are shown in Table 13. After proteolysis, the enzyme-inactivated filtrate was filtered through a 0.2 μm syringe filter and used as analytical sample. Conalbumin (75kDa), ovalbumin (44kDa), carbonic anhydrase (29kDa), ribonuclease A (13.7kDa) and aprotinin (6.5kDa) were purchased from GE Healthcare (UK), and the volume of the column was measured. Blue dextran was used to do this.

GPC 분석 조건GPC Analysis Conditions HPLCHPLC Agilent 1260 Infinity Quarternary LCAgilent 1260 Infinity Quarternary LC DetectorDetector VWD 1260 : 214 nm
RID 1260
VWD 1260: 214 nm
RID 1260
ColumnColumn SuperdexTM 75 10/300 GL (GE Healthcare, UK)Superdex TM 75 10/300 GL (GE Healthcare, UK) Column ovenColumn oven 25℃25 ℃ Mobile phaseMobile phase 50 mM phosphate buffer, pH7.0 (0.15% NaCl)
(HPLC grade)
50 mM phosphate buffer, pH7.0 (0.15% NaCl)
(HPLC grade)
Flow rateFlow rate 0.3 mL/min0.3 mL / min Injection volumeInjection volume 20 μL20 μL

닭가슴살 및 쇠고기 가수분해물의 분자량 측정결과Molecular weight measurement results of chicken breast and beef hydrolyzate 가수분해물 분획Hydrolysate fraction 분자량 (Da)Molecular Weight (Da) 조성비(%)Composition ratio (%) 닭가슴살
단백질 가수분해 분획-1
단백질 가수분해 분획-2
단백질 가수분해 분획-3
chicken breast
Proteolytic Fraction-1
Proteolytic Fraction-2
Proteolytic Fraction-3

1700-2400
1000-1700
50-1000

1700-2400
1000-1700
50-1000

13.5
12.1
74.4

13.5
12.1
74.4
쇠고기
단백질 가수분해 분획-1
단백질 가수분해 분획-2
단백질 가수분해 분획-3
beef
Proteolytic Fraction-1
Proteolytic Fraction-2
Proteolytic Fraction-3

2300-3000
1100-2300
50-1100

2300-3000
1100-2300
50-1100

13.3
11.2
75.5

13.3
11.2
75.5

닭가슴살 및 쇠고기 가수분해물의 분자량을 측정한 결과를 [표 15]에 나타내었다. 현재 가열처리를 통하여 제조되는 닭고기 가수분해물 분획의 분자량이 4500-10000 Da (57%), 3500-4500 Da (36%), 2640-3500 Da (3%) 및 2640 이하(4%), 쇠고기 가수분해물 분획의 분자량은 107000-195000 Da (36%), 56000-71000 Da (34%), 42000-43000 Da (30%)인 사실에 비추어볼 때 본 발명의 결과로 얻어지는 닭고기 가수해물은 분자량이 1700-2400 Da인 분획이 13.57%, 1000-1700 Da인 분획이 12.1.3%, 50-1000 Da인 분획이 74.4%인 결과를 보였으며, 쇠고기 가수분해물의 경우 분자량 2300-3000 Da인 분획은 13.3%, 1100-2300 Da인 분획은 11.24%, 50-1100 Da인 분획이 75.7%로 체내흡수율이 우수한 단백질 가수분해물로 조성되었음을 알 수 있다.Table 15 shows the results of measuring the molecular weight of the chicken breast and beef hydrolyzate. The molecular weight of chicken hydrolyzate fraction produced by heat treatment is 4500-10000 Da (57%), 3500-4500 Da (36%), 2640-3500 Da (3%) and below 2640 (4%) In view of the fact that the molecular weight of the digested fraction is 107000-195000 Da (36%), 56000-71000 Da (34%), 42000-43000 Da (30%), the resulting hydrolyzate of chicken meat has a molecular weight of 1700. The fraction with -2400 Da was 13.57%, the fraction with 1000-1700 Da was 12.1.3%, and the fraction with 50-1000 Da was 74.4%. For the hydrolyzate of beef, the fraction with molecular weight of 2300-3000 Da was 13.3. %, 1100-2300 Da fraction is 11.24%, 50-1100 Da fraction is 75.7% it can be seen that the composition was composed of protein hydrolyzate with excellent body absorption.

Claims (7)

닭가슴살로부터 얻어지는 단백질을 가수분해함에 있어서,
물에 대한 닭가슴살의 비율 10-40중량%, 닭가슴살 대비 파인애플 추출액, 파파야 추출액, 키위 추출액, Alkalase, 및 Flavourzyme으로 이루어지는 군으로부터 선택되는 어느 하나 이상의 단백질 분해효소 0.05-4.0중량%, 잔여량의 물을 고압처리 시간 4-48, 고압처리 압력 25-400MPa, 고압처리 온도 25℃-60℃의 범위에서 고압기를 이용하여 닭가슴살 단백질의 가수분해도를 높이는 방법에 의하여 제조되는 분자량이 1700-2400Da임을 특징으로 하는 닭가슴살.
In hydrolyzing the protein obtained from chicken breast,
10-40% by weight of chicken breast to water, 0.05-4.0% by weight of any one or more proteolytic enzymes selected from the group consisting of pineapple extract, papaya extract, papaya extract, kiwi extract, Alkalase, and Flavorzyme The molecular weight produced by the method of increasing the degree of hydrolysis of chicken breast protein using a high pressure in the high pressure treatment time 4-48, the high pressure treatment pressure 25-400MPa, the high pressure treatment temperature 25 ℃ -60 ℃ characterized in that 1700-2400Da Chicken breast.
제1항에 있어서,
분자량이 1000-1700Da임을 특징으로 하는 닭가슴살.
The method of claim 1,
Chicken breasts, characterized in that the molecular weight is 1000-1700 Da.
제1항에 있어서,
분자량이 50-1000Da임을 특징으로 하는 닭가슴살.
The method of claim 1,
Chicken breast, characterized in that the molecular weight is 50-1000 Da.
쇠고기로부터 얻어지는 단백질을 가수분해함에 있어서,
물에 대한 쇠고기의 비율 10-40중량%, 쇠고기 대비 파인애플 추출액, 파파야 추출액, 키위 추출액, Alkalase, 및 Flavourzyme으로 이루어지는 군으로부터 선택되는 어느 하나 이상의 단백질 분해효소 0.05-4.0중량%, 잔여량의 물을 고압처리 시간 4-48, 고압처리 압력 25-400MPa, 고압처리 온도 25℃-60℃의 범위에서 고압기를 이용하여 쇠고기 단백질의 가수분해도를 높이는 방법에 의하여 제조되는 분자량이 2300-3000Da임을 특징으로 하는 쇠고기.
In hydrolyzing the protein from beef,
10-40% by weight of beef to water, 0.05-4.0% by weight of any one or more proteolytic enzymes selected from the group consisting of pineapple extract, papaya extract, kiwi extract, Alkalase, and Flavorzyme to beef, the remaining amount of water Beef, characterized in that the molecular weight produced by the method of increasing the degree of hydrolysis of beef protein using a high pressure in the range of processing time 4-48, high pressure 25-400MPa, high pressure 25 ℃ -60 ℃ the molecular weight is 2300-3000 Da .
제4항에 있어서.
분자량이 1100-2300Da임을 특징으로 하는 쇠고기.
The method of claim 4,
Beef, characterized in that the molecular weight is 1100-2300Da.
제4항에 있어서.
분자량이 50-1100Da임을 특징으로 하는 쇠고기.
The method of claim 4,
Beef, characterized in that the molecular weight is 50-1100 Da.
제1항 내지 제3항의 어느 한 항에 의하여 제조되는 닭가슴살 단백질 가수분해 물에 펙틴, 알긴산, 잔탄검, 카라기난, 한천, 대두단백질, 셀룰로오스, 구아검으로 이루어지는 군으로부터 선택되는 어느 하나의 생고분자를 첨가하여 안정화함을 특징으로 하는 닭가슴살. The raw polymer selected from the group consisting of pectin, alginic acid, xanthan gum, carrageenan, agar, soy protein, cellulose and guar gum in the chicken breast protein hydrolyzate prepared according to any one of claims 1 to 3. Chicken breasts characterized in that by stabilizing the addition.
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JP2016531951A (en) * 2013-10-04 2016-10-13 イノウェイ・カンパニー・リミテッド Animal protein hydrolyzate, production method thereof and use thereof
CN103734652A (en) * 2013-10-29 2014-04-23 华南农业大学 Preparation method of salt roasted chicken flavor nutritional seasoning powder
KR20180076612A (en) * 2016-12-28 2018-07-06 주식회사 한성바이오파마 Hydrolysis method of pig liver and liver hydrolysis composition produced by this method
KR102654392B1 (en) * 2023-03-17 2024-04-03 농업회사법인 주식회사 에프앤비바이오 Manufacturing method of Feed additive for companion animal comprising hydrolysate of lactic acid bacteria

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