KR100420824B1 - Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials - Google Patents

Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials Download PDF

Info

Publication number
KR100420824B1
KR100420824B1 KR10-2001-0035437A KR20010035437A KR100420824B1 KR 100420824 B1 KR100420824 B1 KR 100420824B1 KR 20010035437 A KR20010035437 A KR 20010035437A KR 100420824 B1 KR100420824 B1 KR 100420824B1
Authority
KR
South Korea
Prior art keywords
silk
molecular weight
alkali
filtrate
dried
Prior art date
Application number
KR10-2001-0035437A
Other languages
Korean (ko)
Other versions
KR20020096638A (en
Inventor
배도규
Original Assignee
배도규
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 배도규 filed Critical 배도규
Priority to KR10-2001-0035437A priority Critical patent/KR100420824B1/en
Publication of KR20020096638A publication Critical patent/KR20020096638A/en
Application granted granted Critical
Publication of KR100420824B1 publication Critical patent/KR100420824B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/12General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length by hydrolysis, i.e. solvolysis in general
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14Extraction; Separation; Purification
    • C07K1/16Extraction; Separation; Purification by chromatography
    • C07K1/18Ion-exchange chromatography
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14Extraction; Separation; Purification
    • C07K1/34Extraction; Separation; Purification by filtration, ultrafiltration or reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K14/00Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/435Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • C07K14/43504Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans from invertebrates
    • C07K14/43563Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans from invertebrates from insects
    • C07K14/43586Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans from invertebrates from insects from silkworms
    • 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
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/17Amino acids, peptides or proteins
    • A23L33/18Peptides; Protein hydrolysates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Biophysics (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Biochemistry (AREA)
  • Analytical Chemistry (AREA)
  • Zoology (AREA)
  • Water Supply & Treatment (AREA)
  • Insects & Arthropods (AREA)
  • Engineering & Computer Science (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Toxicology (AREA)
  • Gastroenterology & Hepatology (AREA)
  • Cosmetics (AREA)
  • Peptides Or Proteins (AREA)

Abstract

본 발명은 부잠사 및 폐견을 이용하여 정선 및 세척과정을 거쳐 세리신을 제거하는 정련을 실시해서 얻어진 피브로인을 주원료로 하여 저분자량의 실크 펩타이드와 고분자량의 수(水) 불용성 피브로인 분말을 제조하는 방법에 관한 것으로, 정련된 실크를 수산화칼슘 또는 수산화바륨으로 알칼리 가수분해한 후 여과한 다음, 여과물은 수세하여 건조시키고, 여과액은 용액 중의 알칼리를 침전시켜 여과하여 제거하고, 여과액을 농축, 건조하는 것을 특징으로 한다.The present invention is a method for producing a low molecular weight silk peptide and a high molecular weight water insoluble fibroin powder using fibroin obtained by refining to remove sericin through a selection process and washing process using sub-nausea and lung dog. Alkyl hydrolysis of the refined silk with calcium hydroxide or barium hydroxide, followed by filtration, the filtrate is washed with water and dried, the filtrate is precipitated by filtration of the alkali in the solution, the filtrate is concentrated, dried Characterized in that.

본 발명의 제조방법에 의해 제조된 실크 펩타이드는 식품용으로 사용가능하며, 고분자량의 수(水) 불용성 피브로인 분말은 산업용으로 사용될 수 있다.Silk peptides prepared by the production method of the present invention can be used for food, high molecular weight water insoluble fibroin powder can be used for industrial purposes.

Description

실크를 이용하여 제조한 실크 펩타이드와 피브로인 분말 물질 및 그 제조방법{Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials}Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials

본 발명은 누에고치 및 그 외 부잠사를 이용하여 수세-정련하고, 정련된 피브로인을 알칼리 용액으로 가수분해하여 아미노산 및 저분자량 피브로인 펩타이드계 물질과 미세한 수(水) 불용성 고분자량 피브로인 분말 물질을 제조하는 방법 및 이 방법에 의해 제조된 저분자량 실크 펩타이드와 고분자량 피브로인 분말에 관한 것이다.The present invention is to wash-refined by using a cocoon and other sub-nax, hydrolyzed refined fibroin to an alkaline solution to prepare amino acids and low molecular weight fibroin peptide-based material and fine water insoluble high molecular weight fibroin powder material And a low molecular weight silk peptide and a high molecular weight fibroin powder produced by the method.

실크는 오래 전부터 그 심미성의 탁월성으로 인해 의류소재로써의 널리 사용되어왔다. 최근에는, 실크가 거의 100%의 단백질로 구성되어 있다는 점에 착안하여, 기능성 소재 특히 식품소재로 활용하려는 개발이 활발해지고 있다.Silk has long been widely used as a garment because of its aesthetic excellence. In recent years, focusing on the fact that silk is composed of almost 100% protein, developments to utilize it as a functional material, especially a food material, have been actively developed.

현재까지 공지된 특허 및 학술문헌을 통한 예를 보면 다음과 같다. 실크 소재를 이용하여 식품소재로 활용하려는 개발은 크게 두 분류로 나누어 진다. 즉, 실크 피브로인을 이용하는 것과 실크 세리신을 이용하는 것이다. 그 중 실 피브로인을 활용할려는 개발 내용을 살펴보면, 식품(일본특허공개 평 1-256350호), 영양보조식품(일본특허공개 평7-31417호), 숙취방지제(일본특허공개 평1-256352호), 콜레스테롤 상승억제식품(일본특허공개 평4-210577호), 혈당상승억제식품(일본특허공개 평4-210576호), 기능성식품(한국특허공고 96-582) 등의 제조방법 및 그 기능성이 개시되어 있다.Examples of patents and scholarly literature known to date are as follows. The development of using silk as a food material is divided into two categories. In other words, silk fibroin is used and silk sericin is used. Among them, the development contents to utilize actual fibroin include food (Japanese Patent Laid-Open Publication No. 1-256350), nutritional supplement (Japanese Patent Laid-Open Publication No. 7-31417), and hangover inhibitors (Japanese Patent Laid-Open Publication No. 1-256352). , Manufacturing method of the cholesterol rising inhibitory food (Japanese Patent Laid-Open Publication No. 4-210577), blood sugar rising inhibitory food (Japanese Patent Laid-Open Publication No. 4-210576), functional food (Korean Patent Publication No. 96-582), and its functionality are disclosed. It is.

상기에 소개되고 있는 바와 같이, 실크 피브로인을 식품소재로써 활용하기 위한 제조방법의 개발 및 상업화를 위해서 많은 연구와 개발이 이루어 졌으나, 식품제조상에 여러 가지 문제점과 제한성을 나타내고 있었다. 그 예를 들면 다음과 같다.As introduced above, many researches and developments have been made for the development and commercialization of a manufacturing method for utilizing silk fibroin as a food material, but has shown various problems and limitations in food manufacturing. For example:

고분자인 실크 피브로인(분자량 100,000이상)을 기능성 식품으로 사용하기 위해서는 저분자화가 필요한데, 이의 수단으로 화학약품을 사용한 두 가지 제조방법이 적용되고 있다.In order to use the macromolecule silk fibroin (molecular weight of 100,000 or more) as a functional food, low molecular weight is required. As a means, two manufacturing methods using chemicals have been applied.

그 첫째 제조방법으로는 염산 등과 같은 산(acid)을 이용하여 가수분해한 후 알칼리로 중화하여 탈염 -농축-건조하는 방법이다. 이 제조방법에서는 고농도의 산(acid)으로 장시간 가수분해시켜야 하고, 중화의 결과로 생성된 고농도의 염(salt)을 제거하여야하기 때문에, 막대한 시설과 과다한 약품의 사용을 피할 수가 없다는 점에서 상업화에 제한을 받고 있다. 또한 제조된 저분자량 실크 피브로인의 색상이 짙은 갈색을 띄고 있어 식품으로서의 사용에 제한을 받지 않을 수 없었다. 그래서 색상을 제거하기 위해서 이온교환수지 등을 사용하는 제조방법이 제안되었으나 이의 경우에는 수율이 40% 이하로 감소하게되는 결과를 초래하게 되었다(일본잠사학잡지 61(1), 32-35, 1992).The first manufacturing method is a method of hydrolysis using an acid such as hydrochloric acid, followed by neutralization with alkali, followed by desalination-concentration-drying. In this manufacturing method, it is necessary to hydrolyze with high concentration of acid for a long time, and remove high concentration of salt generated as a result of neutralization, so it is impossible to avoid the use of enormous facilities and excessive chemicals. It is restricted. In addition, the color of the produced low molecular weight silk fibroin was dark brown, it was inevitably restricted to use as a food. Therefore, a manufacturing method using ion exchange resins has been proposed to remove the color, but in this case, the yield is reduced to 40% or less (Japanese Society for Sampling, 61 (1), 32-35, 1992). ).

둘째의 제조방법으로서는 염화칼슘 등과 같은 염(salt)으로 실크 피브로인을 용해시킨 후, 다시 산(acid), 알칼리(alkali), 효소 등으로 가수분해하는 2단계 제조방법이다. 이 방법에서는 고농도의 염(salt) 용액(40% w/v 이상)을 사용하기 때문에 후에 이를 제거하기 위해서 한외여과(ulter-filteration) 혹은 다이아 여과(Dia-filteration) 방법이 도입되고 있다. 이를 위해서는 막대한 시설비를 투입하여야 하기 때문에 제조상 제한을 받지 않을 수 없다.The second manufacturing method is a two-step method of dissolving silk fibroin with a salt such as calcium chloride, and then hydrolyzing it again with an acid, an alkali, an enzyme, or the like. Since this method uses a high concentration of salt solution (40% w / v or more), ultra-filtering or dia-filtering method is introduced to remove it later. To do this, a huge amount of facility costs must be put into place, which is subject to manufacturing restrictions.

또, 미국 특허 제 5,853,764 호에는 알칼리 수용액을 사용하여 실크 피브로인을 분해하고 다시 산으로 중화하는 방법으로 실크 피브로인 분발을 제조하는 방법이 게시되어 있으나, 이 방법은 알칼리 분해 후 다시 황산 등의 산으로 중화를 하므로 식품용으로 사용할 수 없다는 문제점을 지니고 있었다.In addition, U.S. Patent No. 5,853,764 discloses a method for producing silk fibroin powder by decomposing silk fibroin using an aqueous alkali solution and neutralizing it with an acid, but this method is neutralized with an acid such as sulfuric acid after alkali decomposition. Because it had a problem that it can not be used for food.

따라서, 본 발명자는 상기의 여러 가지 문제점을 해결하기 위하여, 정련된 실크 피브로인을 특수한 알칼리를 사용한 화학적 가수분해 방법으로 분해 한 후, 알칼리를 침전시켜 제거하는 방법에 대해 연구한 결과 실크 아미노산 및 저분자량 실크 펩타이드를 제조하여 식품용의 소재로 채택할 수 있게 되었으며, 또한 동일 공정 상에서 제조된 고분자량 수불용성 실크 피브로인 분말을 산업용으로 유용하게 사용할 수 있게 되었다.Therefore, in order to solve the various problems described above, the present inventors have studied the method of decomposing refined silk fibroin by chemical hydrolysis using a special alkali, followed by precipitation of alkali to remove silk amino acids and low molecular weight. Silk peptides can be prepared and used as food materials, and high molecular weight water-insoluble silk fibroin powders prepared in the same process can be usefully used for industrial purposes.

따라서, 본 발명은 식품 소재에 적합한 실크 아미노산과 펩타이드 및 산업용 소재인 고분자량 수(水) 불용성 실크 피브로인 분말을 최소공정과 최소비용으로 제조할 수 있는 제조방법을 제공하는데 목적이 있다.Accordingly, an object of the present invention is to provide a production method capable of producing high-molecular-weight water-insoluble silk fibroin powder, which is a silk amino acid and peptide suitable for food materials, and an industrial material at a minimum process and at a minimum cost.

도 1은 본 발명의 실시예 1에서 얻어진 저분자량 실크 펩타이드의 현미경 사진(40배 배율).1 is a micrograph (40 times magnification) of a low molecular weight silk peptide obtained in Example 1 of the present invention.

도 2는 본 발명의 실시예 2에서 얻어진 색을 제거한 저분자량 실크 펩타이드의 현미경 사진(40배 배율).Figure 2 is a micrograph (40x magnification) of a low molecular weight silk peptide from which color was removed in Example 2 of the present invention.

도 3은 본 발명의 실시예 3에서 얻어진 고분자량 수불용성 피브로인 분말의 현미경 사진(40배 배율).3 is a micrograph (40 times magnification) of a high molecular weight water insoluble fibroin powder obtained in Example 3 of the present invention.

도 4는 본 발명의 실시예 4에서 얻어진 저분자량 실크 펩타이드의 현미경 사진(40배 배율).Figure 4 is a micrograph (40 times magnification) of the low molecular weight silk peptide obtained in Example 4 of the present invention.

도 5는 본 발명의 실시예 5에서 얻어진 고분자량 수불용성 피브로인 분말의 현미경 사진(40배 배율).5 is a micrograph (40-fold magnification) of the high molecular weight water insoluble fibroin powder obtained in Example 5 of the present invention.

도 6은 본 발명의 제조 공정도이다.6 is a manufacturing process chart of the present invention.

상기 본 발명의 목적은 정련된 실크를 수산화칼슘, 수산화바륨으로 알칼리 가수분해한 후 여과하고 용액에 존재하는 알칼리를 침전시켜 여과, 농축, 건조해서 얻어지는 것을 특징으로 하는 실크 펩타이드 및 수(水)불용성 고분자량 피브로인 분말의 제조방법에 의해 달성된다.The above object of the present invention is obtained by alkali hydrolysis of the refined silk with calcium hydroxide and barium hydroxide, followed by filtration and precipitation of alkali present in the solution, followed by filtration, concentration and drying. It is achieved by the process for the preparation of molecular weight fibroin powder.

이하 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail.

제 1 공정1st process

본 발명의 원료로 사용하기 위하여 누에고치 그 외 부잠사를 정선 및 수세를통하여 협잡물과 이물질을 제거하고 잘게 절단한다.In order to use as a raw material of the present invention, silkworm cocoons and other sub-silsa are removed through fine selection and washing to remove contaminants and foreign matter and finely cut.

제 2 공정(고압정련 공정)2nd process (high pressure refining process)

제 1 공정에서 제공된 누에고치 혹은 부잠사에서 세리신(sericin)을 제거하기 위하여 원료대비 5∼20배의 물을 가하고 100∼130℃에서 20∼120분간 가열한 후 세리신을 제거한다.In order to remove sericin from the silkworm cocoon or sub-sasa provided in the first step, 5-20 times of water is added to the raw material and heated at 100-130 ° C. for 20 to 120 minutes to remove sericin.

제 3 공정(피브로인의 가수분해 공정)Third process (hydrolysis of fibroin)

상기 제 2 공정으로부터 얻어진 피브로인을 알칼리 가수분해시킨다. 예로서 피브로인을 기준으로 액비 10∼40으로 물을 채운다. 이때 사용하는 알칼리는 수산화칼슘[Ca(OH)2] 혹은 수산화바륨[Ba(OH)2] 용액으로 농도는 0.4∼2.0w/v%(용액의 pH 기준으로 11.5∼12.4)로 조정된 것을 사용하여, 90∼100℃에서 8∼48시간 가열한 후 냉각시키면 침전물이 생긴다. 이 때 침전물에는 고분자량 수(水) 불용성 피브로인과 알칼리가 포함되어 있으며 이를 여과 분리하면 가수분해된 저분자량의 실크 펩타이드 용액을 얻는다. 이 때의 피브로인 용해도는 표 1과 같다.Alkali hydrolysis of the fibroin obtained from the said 2nd process is carried out. For example, fill water with liquid ratio 10-40 based on fibroin. The alkali used was calcium hydroxide [Ca (OH) 2] or barium hydroxide [Ba (OH) 2] solution, and the concentration was adjusted to 0.4 to 2.0 w / v% (11.5 to 12.4 based on the pH of the solution). , 8 to 48 hours at 90 to 100 ℃ and then cooled to precipitate. At this time, the precipitate contains a high molecular weight water insoluble fibroin and an alkali, which is separated by filtration to obtain a hydrolyzed low molecular weight silk peptide solution. Fibroin solubility at this time is shown in Table 1.

<표1> 가수분해 조건과 용해도 및 평균중합도Table 1 Hydrolysis Conditions, Solubility and Average Polymerization

처리시간Conc (%.)Processing time Conc (%.) 용해도(%)Solubility (%) 평균중합도Average degree of polymerization 1212 1414 1212 1414 0.20.2 37.4037.40 37.6037.60 30.530.5 13.413.4 0.40.4 52.3052.30 53.1053.10 11.111.1 6.606.60 0.60.6 63.5563.55 64.1264.12 2.052.05 1.431.43 0.80.8 63.6963.69 64.1264.12 1.411.41 1.401.40 1.01.0 64.0664.06 64.4064.40 1.651.65 1.181.18 1.21.2 64.2164.21 66.2066.20 1.641.64 1.231.23

제 4 공정(고분자량 수(水) 불용성 피브로인 분말 제조 공정)4th process (high molecular weight water insoluble fibroin powder manufacturing process)

상기 제 3 공정에서 분리된 침전물에 충분한 양의 물을 넣고 알칼리가 더 이상 용출되지 않을 때까지 여과 분리 공정을 반복한다. 이렇게 하여 얻은 고형물을 건조, 분쇄하여 고분자량 수불용성 실크 분말 물질 1 을 얻게된다.A sufficient amount of water is added to the precipitate separated in the third step and the filtration separation process is repeated until alkali is no longer eluted. The solid thus obtained is dried and pulverized to obtain a high molecular weight water insoluble silk powder material 1.

제 5 공정(고분자량 수(水) 불용성 피브로인의 가수분해 공정)5th process (hydrolysis process of high molecular weight water insoluble fibroin)

상기 제 3 공정에서 분리된 침전물에 포함되어 있는 수(水) 불용성 피브로인을 다시 3공정과 같은 조건에서 가수분해하여 저분자량 실크 펩타이드 용액을 얻는다.The water insoluble fibroin contained in the precipitate separated in the third step is hydrolyzed again under the same conditions as in the third step to obtain a low molecular weight silk peptide solution.

제 6 공정(실크 펩타이드 용액에서의 알칼리 제거 공정)6th process (alkali removal process in silk peptide solution)

상기 제 3 공정 및 제 4 공정에서 분리된 실크 펩타이드 용액에, 용해되어 있는 알칼리를 제거하기 위하여, 사용된 알칼리와 난용성 염을 생성할 수 있는 화학약품(예를 들면 황산, 옥살산, 액화 이산화탄소, 드라이 아이스, 중탄산암모늄)을 용해된 알칼리의 당량 만큼 첨가하여 열을 가한 후 방치하면 칼슘염 또는 바륨염으로 침전물이 침전된다. 이때 침전물을 여과 분리하여 알칼리가 제거된 실크 펩타이드 수용액을 얻어낸다. 침전시켜 제거하는 방법 외에 구연산으로 중화하여 구연산 염 형태로 그대로 남겨 두어도 무방하다.In order to remove dissolved alkali in the silk peptide solution separated in the third and fourth processes, chemicals capable of producing alkali and poorly soluble salts used (for example, sulfuric acid, oxalic acid, liquefied carbon dioxide, Dry ice, ammonium bicarbonate) is added as much as the equivalent amount of dissolved alkali and left to heat, and precipitates are precipitated with calcium salt or barium salt. At this time, the precipitate is separated by filtration to obtain an aqueous solution of silk peptide from which alkali is removed. In addition to the method of precipitation and removal, it may be neutralized with citric acid and left in the form of citric acid salt.

제 7 공정(실크 펩타이드 용액의 농축 공정)7th process (concentration process of a silk peptide solution)

제 6 공정에서 회수되는 실크 펩타이드 수용액을 40∼70℃의 온도에서 진공 농축하거나 한외여과막을 이용하여 농도가 10∼40%가 되도록 농축을 시킨다.The silk peptide aqueous solution recovered in the 6th process is concentrated in vacuo at the temperature of 40-70 degreeC, or it is concentrated so that a density | concentration may be 10 to 40% using an ultrafiltration membrane.

제 8 공정(색소물질의 제거 공정)8th process (removal of dyestuff material)

제 7 공정에서 얻어진 농축된 실크 펩타이드 수용액을 이온교환수지를 통과시키거나, 분말 활성탄이나 과산화수소 처리를 통하여 무색의 실크 펩타이드 수용액을 얻는다.The concentrated silk peptide aqueous solution obtained in the seventh step is passed through an ion exchange resin, or a powdery activated carbon or hydrogen peroxide treatment to obtain a colorless silk peptide aqueous solution.

제 9 공정(건조 및 분해 공정)9th process (drying and decomposition process)

상기 공정으로 농축된 무색의 실크 펩타이드 수용액을 건조와 분쇄과정을 거쳐 최종의 미립 상태의 트리펩타이드(tri-peptide) 이하의 물질 2를 얻게 되는 것이다.The colorless silk peptide solution concentrated in the above process is dried and pulverized to obtain substance 2 having a final tripeptide (tri-peptide).

이상과 같은 제조공정을 통해 본 발명에서 목적으로 하는 저분자량 실크 펩타이드 물질 2와 고분자량 수(水) 불용성 피브로인 분말 물질 1을 얻게되는 것이다.Through the manufacturing process as described above to obtain a low molecular weight silk peptide material 2 and a high molecular weight water insoluble fibroin powder material 1 for the purpose of the present invention.

다음은 실시예를 통해 본 발명을 더욱 상세히 설명하기로 한다.Next, the present invention will be described in more detail with reference to Examples.

(실시예 1)(Example 1)

제 1 공정 : 깨끗한 절각견에서 협잡물을 제거하고 잘게 절단하여 500g을 준비하였다.First step: 500g was prepared by removing fines from a clean slice dog and cutting it finely.

제 2 공정 : 순수한 절각견 500g을 고압솥에 물 10L와 함께 넣고 125℃에서 50분간 가열한 후 세리신 및 수용성 불순물을 제거한 후 온수로 1회 수세하여 건조하였다. 이 때의 무게는 350g이였다.Second step: 500 g of pure keratin dogs were put together with 10 L of water in an autoclave, heated at 125 ° C. for 50 minutes, removed sericin and water-soluble impurities, and then washed once with hot water and dried. At this time, the weight was 350g.

제 3 공정 : Ca(OH)2 0.7% 용액 7L에 순수한 피브로인 350g을 넣은 후 95℃에서 12시간 가수분해시켰다.Third step: 350 g of pure fibroin was added to 7 L of a 0.7% solution of Ca (OH) 2 and hydrolyzed at 95 ° C. for 12 hours.

제 4 공정 : 상기공정에서 얻어진 용액을 여과지로 여과하여 불용해물을 제거하였다.4th process: The solution obtained at the said process was filtered by the filter paper, and the insoluble material was removed.

제 5 공정 : 상기 공정에서 얻어진 수용액에 중탄산암모늄 54g을 넣고 잘 교반하여 방치한 후 생성된 탄산칼슘을 침전시켜서 여과지로 침전물을 분리하였다.5th step: 54 g of ammonium bicarbonate was added to the aqueous solution obtained by the said process, it was left to stir well, the calcium carbonate produced was precipitated, and the deposit was isolate | separated with the filter paper.

제 6 공정 : 상기공정에서 얻어진 수용액을 60℃에서 ¼로 진공농축한 후 냉동건조하여 저분자량 실크 펩타이드 물질2를 205g 얻을 수 있었다. 이 때 얻어진 펩타이드의 분자량을 알아보기 위해서 말단기 정량법으로 구한 결과 평균중합도가 2.09로 나타나 물질2는 저분자량의 펩타이드로 구성되어 있음을 알았다. 또한 이 물질의 정색정도를 알아보기 위해서 색채색차계(미놀타)로 측정한 결과는 백도치가 82.20이였다. 얻어진 저분자량 실크 펩타이드의 현미경 사진(40배 배율)을 도 1에 게시하였다.6th step: The aqueous solution obtained by the said process was vacuum-concentrated to ¼ at 60 degreeC, and then lyophilized, and 205g of low molecular weight silk-peptide substance 2 was obtained. In order to determine the molecular weight of the peptide obtained from the end group quantification method, the average degree of polymerization was found to be 2.09, indicating that substance 2 was composed of a low molecular weight peptide. In addition, the color measured by the color difference meter (Minolta) to find the degree of coloration of this material was 82.20. The micrograph (40 times magnification) of the obtained low molecular weight silk peptide was shown in FIG.

(실시예 2)(Example 2)

상기 실시예 1에서 얻어진 저분자량 실크 펩타이드 물질은 약간의 황색을 띄고 있으므로 이의 제거를 목적으로 상기 제 6 공정의 농축된 용액을 양이온교환수지를 통과시킨 후 분말 건조하였다. 이 때 얻어진 분말의 양은 실시예 1에 비해 30%정도를 얻을 수 있었다. 이렇게 하여 얻은 분말의 평균중합도는 2.38로 나타났으며 백도는 83.43이였다. 얻어진 색을 제거한 저분자량 실크 펩타이드의 현미경 사진(40배 배율)을 도 2에 게시하였다.Since the low molecular weight silk peptide material obtained in Example 1 was slightly yellow, the concentrated solution of the sixth process was passed through a cation exchange resin and then powder dried for the purpose of removal thereof. The amount of powder obtained at this time was about 30% as compared with Example 1. The average degree of polymerization of the powders obtained was 2.38 and the whiteness was 83.43. The micrograph (40 times magnification) of the low molecular weight silk peptide from which the obtained color was removed was shown in FIG.

(실시예 3)(Example 3)

실시예 1의 제 4 공정에서의 침전물을 회수하여 5L의 물에 넣고 잘 교반하여 여과하는 공정을 5회 반복하여 알칼리를 완전히 제거한 후 건조하여 고분자량 수불용성 피브로인 물질 1 130g을 얻었고 그 백도치는 75.32였다. 얻어진 고분자량 수불용성 피브로인 분말의 현미경 사진(40배 배율)을 도3에 게시하였다.The precipitate in the fourth process of Example 1 was collected, poured into 5 L of water, stirred well and filtered five times to completely remove the alkali, and then dried to obtain 130 g of a high molecular weight water insoluble fibroin substance 1. It was. A micrograph (40 times magnification) of the obtained high molecular weight water insoluble fibroin powder is shown in FIG. 3.

(실시예 4)(Example 4)

실시예 1의 제 4 공정에서 회수한 침전물을 Ca(OH)2 0.7% 용액 2.5L에 넣은 후 95℃에서 12시간 가수분해시켰다. 계속해서 실시예 1의 제 5, 6공정과 같이하여 84.5g의 물질 2를 얻었다. 이 때 중탄산암모늄의 첨가량은 20g이였고, 그 백도치는 60.99로 약간 황갈색을 띄고 있었다. 색을 제거하기 위해서 분말활성탄을 10% w/w 펩타이드로 첨가하여 색소 물질을 제거한 후의 백도치는 73.4로 나타났고, 이렇게 하여 얻은 저분자량 실크 펩타이드의 평균중합도는 2.96이었다. 얻어진 저분자량 실크 펩타이드의 현미경 사진(40배 배율)을 도 4에 게시하였다.The precipitate recovered in the fourth step of Example 1 was added to 2.5 L of a 0.7% solution of Ca (OH) 2 and then hydrolyzed at 95 ° C. for 12 hours. Subsequently, 84.5 g of substance 2 was obtained in the same manner as in the fifth and sixth steps of Example 1. At this time, the amount of ammonium bicarbonate added was 20 g, and the whiteness was slightly yellowish brown at 60.99. In order to remove the color, powdered carbon was added with 10% w / w peptide to remove the pigment material, and the whiteness was 73.4, and the average degree of polymerization of the low molecular weight silk peptide thus obtained was 2.96. The micrograph (40 times magnification) of the obtained low molecular weight silk peptide was shown in FIG.

(실시예 5)(Example 5)

실시예 4에서 회수한 침전물을 실시예 3과 같은 방법으로하여 고분자량 수(水)불용성 피브로인 분말 34.4g을 얻었고 백도치는 72.11이였다. 얻어진 고분자량 수불용성 피브로인 분말의 현미경 사진(40배 배율)을 도 5에 게시하였다.The precipitate recovered in Example 4 was obtained in the same manner as in Example 3, obtaining 34.4 g of a high molecular weight water insoluble fibroin powder and having a whiteness of 72.11. The micrograph (40 times magnification) of the obtained high molecular weight water insoluble fibroin powder was shown in FIG.

이상의 본 발명의 방법으로 얻은 실크 펩타이드의 아미노산 조성을 표2에 나타냈다.Table 2 shows the amino acid composition of the silk peptide obtained by the method of the present invention.

〈표 2〉 본 발명에서 얻어진 저분자량 실크 펩타이드의 아미노산 조성(%)TABLE 2 Amino Acid Composition (%) of Low Molecular Weight Silk Peptides Obtained in the Present Invention

구 분아미노산Amino acid AA BB CC Asp.Asp. 3.473.47 1.051.05 2.322.32 Ser.Ser. 5.755.75 6.776.77 0.950.95 Glu.Glu. 2.702.70 0.760.76 2.022.02 Pro.Pro. 5.585.58 3.443.44 3.813.81 Gly.Gly. 42.3042.30 46.6346.63 46.1746.17 Ala.Ala. 21.5821.58 24.5824.58 24.7324.73 Val.Val. 2.642.64 1.881.88 3.513.51 Met.Met. 0.390.39 0.300.30 0.590.59 Ile.Ile. 0.700.70 0.390.39 0.730.73 Leu.Leu. 0.760.76 0.580.58 0.900.90 Tyr.Tyr. 7.377.37 1.661.66 3.613.61 Phe.Phe. 0.950.95 0.380.38 0.540.54 His.His. 0.440.44 0.360.36 0.260.26 Lys.Lys. 0.700.70 0.960.96 0.900.90 Amm.Amm. 4.304.30 9.879.87 8.298.29 Arg.Arg. 0.390.39 0.390.39 0.660.66 TotalTotal 100.02100.02 99.6499.64 99.9999.99

A : 본 발명의 실시예 1에서 얻은 펩타이드 물질A: peptide material obtained in Example 1 of the present invention

B : 본 발명의 실시예 2에서 얻은 펩타이드 물질B: peptide material obtained in Example 2 of the present invention

C : 본 발명의 실시예 4에서 얻은 펩타이드 물질C: peptide material obtained in Example 4 of the present invention

이상에서 살펴본 바와 같이, 본 발명에 있어서는 저분자량 실크 펩타이드를 제조함에 있어서 염산가수분해(1N∼3N 농도)와 같은 격렬한 조건이 아닌 온화한 조건에서 알칼리로 가수분해(0.1N 농도)하기 때문에, 약품의 사용량도 줄일 수 있을 뿐만 아니라 가수분해시 산화에 기인한 갈변을 최대한 피할 수 있었고, 사용된 알칼리를 침전시켜 제거함으로써 생산설비를 절감할 수 있는 제조방법으로서, 그 구성 아미노산에는 별 차이가 없으므로, 현재 실크 펩타이드의 효능성이 입증된 숙취방지, 간세포 보호, 콜레스테롤치 상승 억제 등의 기능성 식품으로 응용이 가능할것으로 예상된다.As described above, in the present invention, in the preparation of low molecular weight silk peptides, since the hydrolysis (0.1 N concentration) is performed under alkaline conditions under mild conditions, such as hydrochloric acid hydrolysis (1 N to 3 N concentration), In addition to reducing the amount of use, it was possible to avoid browning due to oxidation during hydrolysis as much as possible, and to reduce production facilities by precipitating and removing used alkalis. It is expected to be applicable to functional foods such as hangover prevention, hepatocyte protection, and cholesterol level suppression, which have demonstrated the efficacy of silk peptides.

또한, 고분자량 수불용성 피브로인 분말은 섬유가공용, 화장품 원료용 등의 전개가 예상된다.In addition, high molecular weight water-insoluble fibroin powder is expected to be developed for textile processing, cosmetic raw materials and the like.

Claims (9)

정련된 실크를 수산화칼슘 또는 수산화바륨으로 알칼리 가수분해한 후 여과한 다음, 여과물은 수세하여 건조시키고, 여과액은 용액 중의 알칼리를 침전시켜 여과하여 제거하고, 여과액을 농축, 건조하는 것을 특징으로 하는 실크 펩타이드 및 수(水)불용성 고분자량 피브로인 분말의 제조방법.Alkyl hydrolysis of the refined silk with calcium hydroxide or barium hydroxide, followed by filtration, the filtrate is washed with water and dried, the filtrate is precipitated by the precipitation of alkali in the solution to remove the filtrate, the filtrate is concentrated and dried Silk peptide and a method of producing a water-insoluble high molecular weight fibroin powder. 제 1 항에 있어서, 상기 알칼리는 황산, 옥살산, 액체 이산화탄소, 드라이 아이스, 및 중탄산암모늄으로 구성된 그룹으로부터 선택된 하나 이상의 화합물을 사용하여 침전시켜 제거하는 것을 특징으로 하는 제조방법.The method of claim 1, wherein the alkali is removed by precipitation using at least one compound selected from the group consisting of sulfuric acid, oxalic acid, liquid carbon dioxide, dry ice, and ammonium bicarbonate. 제 1 항에 있어서, 상기 알칼리를 제거한 실크 펩타이드 용액을 양이온교환수지를 통과시키거나, 분말 활성탄 또는 과산화수소 처리로 색소 물질을 제거하는 단계를 더 포함하는 것을 특징으로 하는 제조방법.The method of claim 1, further comprising passing the alkali-depleted silk peptide solution through a cation exchange resin or removing the pigment material by powdered activated carbon or hydrogen peroxide treatment. 제 1 항에 있어서, 상기 수(水) 불용성 피브로인 분말을 다시 알칼리 가수분해하여 여과하고 알칼리를 침전시켜 제거한 다음, 농축 및 건조과정을 반복하는 것을 특징으로 하는 제조방법.The method according to claim 1, wherein the water-insoluble fibroin powder is again subjected to alkali hydrolysis, filtered, and precipitated and removed, followed by concentration and drying. 제 1 항에 있어서, 상기 수산화칼슘 또는 수산화바륨은 0.2∼2.0%의 수용액으로 피브로인 중량대비 10∼40배로 부가되는 것을 특징으로 하는 제조방법.The method according to claim 1, wherein the calcium hydroxide or barium hydroxide is added at an amount of 10 to 40 times the weight of fibroin in an aqueous solution of 0.2 to 2.0%. 제 1 항에 있어서, 상기 알칼리 가수분해는 90∼100℃에서 8∼48시간동안 행해지는 것을 특징으로 하는 제조방법.The method according to claim 1, wherein the alkali hydrolysis is performed at 90 to 100 ° C for 8 to 48 hours. 정련된 실크를 수산화칼슘 또는 수산화바륨으로 알칼리 가수분해한 후 여과한 다음, 여과물은 수세하여 건조시키고, 여과액은 용액 중의 알칼리를 구연산으로 중화시켜 농축, 건조하는 것을 특징으로 하는 실크 펩타이드 및 수(水)불용성 고분자량 피브로인 분말의 제조방법.Alkali hydrolysis of the refined silk with calcium hydroxide or barium hydroxide, followed by filtration, the filtrate is washed with water and dried, the filtrate is concentrated and dried by neutralizing the alkali in the solution with citric acid and dried ( A method for producing an insoluble high molecular weight fibroin powder. 삭제delete 삭제delete
KR10-2001-0035437A 2001-06-21 2001-06-21 Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials KR100420824B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR10-2001-0035437A KR100420824B1 (en) 2001-06-21 2001-06-21 Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR10-2001-0035437A KR100420824B1 (en) 2001-06-21 2001-06-21 Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials

Publications (2)

Publication Number Publication Date
KR20020096638A KR20020096638A (en) 2002-12-31
KR100420824B1 true KR100420824B1 (en) 2004-03-02

Family

ID=27710371

Family Applications (1)

Application Number Title Priority Date Filing Date
KR10-2001-0035437A KR100420824B1 (en) 2001-06-21 2001-06-21 Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials

Country Status (1)

Country Link
KR (1) KR100420824B1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100694662B1 (en) * 2004-09-21 2007-03-13 주식회사 에이.비.아이 Preparation of amino acids/oligopeptides from animal whole blood or clotted blood
KR100789405B1 (en) * 2007-07-03 2007-12-28 월드웨이(주) Method of producing silk tyrosine
JP6029078B2 (en) 2012-06-26 2016-11-24 アル・プレ・テック エッセ・エルレ・エルレ アラジー・プリヴェンション・テクノロジー・イタリアAl.Pre.Tec. Srl Allergy Prevention Technology Italia Method for producing fibroin powder from silk products or silk filaments

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5640695A (en) * 1979-09-11 1981-04-16 Kanebo Ltd Powdery silk fibroin peptide and its preparation
JPH0767687A (en) * 1993-08-27 1995-03-14 Yamaguchi Kaken Kk Production of water-soluble silk fibroin
JPH08143595A (en) * 1994-11-18 1996-06-04 Kawaken Fine Chem Co Ltd Production of silk protein-hydrolyzed peptide-acylated product or salt thereof
WO1996023020A1 (en) * 1995-01-27 1996-08-01 JAPAN represented by NATIONAL INSTITUTE OF SERICULTURAL AND ENTOMOLOGICAL SCIENCE, MINISTRY OF AGRICULTURE, FORESTRY AND FISHERIES, DIRECTOR GENERAL Process for producing fine silk fibroin powder
WO2001003654A1 (en) * 1999-07-12 2001-01-18 Japan As Represented By Director General Of National Institute Of Sericultural And Entomological Science Ministry Of Agriculture, Forestry And Fisheries Cosmetic containing crystalline silk ultra-fine powder
WO2001042300A1 (en) * 1999-12-09 2001-06-14 National Institute Of Agrobiological Sciences Process for producing functional silk fibroin and utilization of the same
KR20010086537A (en) * 2000-03-02 2001-09-13 김애정 Method of Producing the Powder of Silk Peptide and the Beverage Containing Silk Peptide
KR20020064085A (en) * 2001-01-31 2002-08-07 (주)샘스텍 Blood sugar regulating agent which comprises sericin-peptide from cocoons of Bombyx mori as an effective component and method thereof

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5640695A (en) * 1979-09-11 1981-04-16 Kanebo Ltd Powdery silk fibroin peptide and its preparation
JPH0767687A (en) * 1993-08-27 1995-03-14 Yamaguchi Kaken Kk Production of water-soluble silk fibroin
JPH08143595A (en) * 1994-11-18 1996-06-04 Kawaken Fine Chem Co Ltd Production of silk protein-hydrolyzed peptide-acylated product or salt thereof
WO1996023020A1 (en) * 1995-01-27 1996-08-01 JAPAN represented by NATIONAL INSTITUTE OF SERICULTURAL AND ENTOMOLOGICAL SCIENCE, MINISTRY OF AGRICULTURE, FORESTRY AND FISHERIES, DIRECTOR GENERAL Process for producing fine silk fibroin powder
JPH08198970A (en) * 1995-01-27 1996-08-06 Norin Suisansyo Sanshi Konchu Nogyo Gijutsu Kenkyusho Production of silk fibroin fine powder
KR100217169B1 (en) * 1995-01-27 1999-09-01 노링스이산쇼 산시.곤츄노교기즈츠켄큐쇼쵸가 다이효스루 닛본고쿠 Process for producing fine silk fibroin powder
WO2001003654A1 (en) * 1999-07-12 2001-01-18 Japan As Represented By Director General Of National Institute Of Sericultural And Entomological Science Ministry Of Agriculture, Forestry And Fisheries Cosmetic containing crystalline silk ultra-fine powder
WO2001042300A1 (en) * 1999-12-09 2001-06-14 National Institute Of Agrobiological Sciences Process for producing functional silk fibroin and utilization of the same
KR20010086537A (en) * 2000-03-02 2001-09-13 김애정 Method of Producing the Powder of Silk Peptide and the Beverage Containing Silk Peptide
KR20020064085A (en) * 2001-01-31 2002-08-07 (주)샘스텍 Blood sugar regulating agent which comprises sericin-peptide from cocoons of Bombyx mori as an effective component and method thereof

Also Published As

Publication number Publication date
KR20020096638A (en) 2002-12-31

Similar Documents

Publication Publication Date Title
DE19502168C1 (en) Process for the production of wheat protein hydrolyzates
KR100420824B1 (en) Silk peptide and silk fibroin powder materials made by silk and manufacturing method for those materials
US20060014256A1 (en) Sodium chondroitin sulfate, chondroitin-sulfate-containing material and processes for producing the same
CN113563459A (en) Protein extraction process in production process of collagen peptide
WO2004104036A1 (en) Process for producing soyeban whey protein and digested soybean whey protein
CN1129451C (en) Process for preparing injection liquid of brain protein hydrolyzate
KR100532153B1 (en) producing method of protein hydrolysates from fish scale
JPH05125100A (en) High-purity pepsin soluble scale collagen and its production
KR100647033B1 (en) Process for preparing sterilized pure water-soluble collagen peptide
EP0580694B1 (en) Production of phosphopeptides from casein
CA1340222C (en) Preparations of placenta collagen, their extraction method and their applications
KR100335702B1 (en) Silk peptide and process for the preparation thereof
KR100354960B1 (en) A method for preparation of high purified silk peptide by gel filtration chromatography
JPH06292595A (en) Production of low-molecular weight fibroin
CA2047978C (en) Process for preparing heparin calcium
JPH0767687A (en) Production of water-soluble silk fibroin
CN113754759A (en) Process for extracting multiple nutritional ingredients from fish scales
CN107082796A (en) A kind of method of purifying protein zymolyte small molecular polypeptide
JPH05155900A (en) High-purity acid-insoluble fish scale collagen and its production
KR960000582B1 (en) Making method of functional polypeptide from silkworm cocoon
US2598341A (en) Manufacture of protein hydrolysates
KR100577075B1 (en) Method for purifying hyaluronic acid using calcium salt and phosphate salt, or calcium phosphate salt
KR980008072A (en) Method for manufacturing food and beverage materials through omission of sericin removal step, omission of hydrochloric acid and water volatilization step and improvement of neutralization method
KR101686474B1 (en) Pearl proteins solubilization manufacturing method for using alkali solubilisated and clathrate hydrate
US7048955B2 (en) Soybean phosphopeptide calcium and method for producing thereof

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20130125

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20140127

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20150130

Year of fee payment: 12

LAPS Lapse due to unpaid annual fee