DK146630B - PROCEDURE FOR GELATINE PREPARATION BY PROCESSING COLLAGENIC MATERIAL WITH PROTEOLYTIC ENZYMES - Google Patents

PROCEDURE FOR GELATINE PREPARATION BY PROCESSING COLLAGENIC MATERIAL WITH PROTEOLYTIC ENZYMES Download PDF

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DK146630B
DK146630B DK536376AA DK536376A DK146630B DK 146630 B DK146630 B DK 146630B DK 536376A A DK536376A A DK 536376AA DK 536376 A DK536376 A DK 536376A DK 146630 B DK146630 B DK 146630B
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gelatin
preparation
procedure
enzymatic
processing
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DK536376A (en
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Michel Hooreman
Marcel Forgeot
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Michel Hooreman
Marcel Forgeot
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09HPREPARATION OF GLUE OR GELATINE
    • C09H3/00Isolation of glue or gelatine from raw materials, e.g. by extracting, by heating
    • 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
    • A23J1/00Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A23J1/02Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from meat
    • 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
    • A23J1/00Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A23J1/10Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from hair, feathers, horn, skins, leather, bones, or the like
    • 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
    • A23J3/32Working-up of proteins for foodstuffs by hydrolysis using chemical agents
    • A23J3/34Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes
    • A23J3/341Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes of animal 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
    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32Working-up of proteins for foodstuffs by hydrolysis using chemical agents
    • A23J3/34Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes
    • A23J3/341Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes of animal proteins
    • A23J3/342Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes of animal proteins of collagen; of gelatin
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Biochemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Zoology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Organic Chemistry (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Materials For Medical Uses (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Enzymes And Modification Thereof (AREA)

Description

146630146630

Opfindelsen angår en hidtil ukendt fremgangsmåde til fremstilling af gelatine, hvilken fremgangsmåde er af den i kravets indledning angivne art, og fremgangsmåden er ejendommelig ved det i kravets kendetegnende del angivne.The invention relates to a novel process for the preparation of gelatin which is of the kind specified in the preamble of the claim and is characterized by the characterizing part of the claim.

5 Fra Chemical Abstracts 68—96816 y kendes en to-trins fremgangsmåde til fremstilling af gelatine omfattende en behandling af collagenholdigt materiale, kalveskind, med et proteolytisk enzym, pronase, under tilstedeværelse af CaCl^, og opvarmning til denaturering til β-kædemolekyler.Chemical Abstracts 68-96816 y discloses a two-step process for preparing gelatin comprising treating collagen-containing material, calfskin, with a proteolytic enzyme, pronase, in the presence of CaCl 2, and heating for denaturation to β-chain molecules.

10 Fra Chemical Abstracts 73-78571 p kendes en tre trins fremgangsmåde til fremstilling af gelatine, omfattende en partiel hydrolyse af kalveskind i surt medium, enzymatisk hydrolyse ved pH 2,9 med et enzym frembragt af Aspergillus niger, og neutralisering af mediet og denatu-15 rering af collagenet ved opvarmning i 2,5 timer.Chemical Abstracts 73-78571 p discloses a three step process for the preparation of gelatin, comprising a partial hydrolysis of calfskin in acidic medium, enzymatic hydrolysis at pH 2.9 with an enzyme produced by Aspergillus niger, and neutralization of the medium and denaturing agent. Heating the collagen by heating for 2.5 hours.

I Chemical Abstracts 78-160919 v sammenlignes de forskellige fremgangsmåder til fremstilling af gelatine fra svineskinds-collagen. Ved denne sammenligning giver pronase højere udbytter af gelatine end nogen 20 anden indtil da kendt enzymatisk fremgangsmåde, men denne oplysning refererer til fremstilling af gelatine ud fra collagenholdigt materiale ikke fra brusk eller kødaffald.In Chemical Abstracts 78-160919 v, the various methods for preparing gelatin from pigskin collagen are compared. In this comparison, pronase yields higher yields of gelatin than any other enzymatic method known to date, but this disclosure refers to the preparation of gelatin from collagen-containing material not from cartilage or meat waste.

Fra Chemical Abstracts 79“122997 g kendes en behandling af kalveskind med proteaser fra Actinomyces fradiae 25 119.From Chemical Abstracts 79 “122997 g, a treatment of calfskin with proteases from Actinomyces fradiae 25 119 is known.

Fra Chemical Abstracts 82-107985 v kendes virkningen af proteaser fra Actinomyces fradiae 119, der er blevet fraktionerede på carboxymethylcellulose, hvor de tre første fraktioner viste sig at besidde både elastolytiske, 30 proteolytiske og collagenolytiske egenskaber, hvorimod den fjerde fraktion kun havde proteolytiske og collagenolytiske egenskaber. En yderligere fraktionering af den første fraktion gav meget stærke proteaser, som hydrolyserer collagen og elastin til fire frie aminosyrer og små pepti-35 der. De andre enzymer, der er indeholdte i denne enzymblanding, har en peptidasisk aktivitet (enzymerne i den 2.Chemical Abstracts 82-107985 v discloses the action of proteases from Actinomyces fradiae 119 which have been fractionated on carboxymethyl cellulose, where the first three fractions were found to possess both elastolytic, proteolytic and collagenolytic properties, whereas the fourth fraction had only proteolytic and collagenolytic properties. A further fractionation of the first fraction yielded very strong proteases which hydrolyze collagen and elastin to four free amino acids and small peptides. The other enzymes contained in this enzyme mixture have a peptidic activity (the enzymes in the 2).

146630 2 og 3. fraktion hydrolyserer peptider med en molekylvægt mindre end 25.000). Brusk har imidlertid en molekylvægt på ca 130.000, og det er derfor usandsynligt, at disse enzymer kan have nogen virkning på brusk til fremstilling 5 af gelatine.146630 2 and 3 fraction hydrolyzes peptides having a molecular weight less than 25,000). However, cartilage has a molecular weight of about 130,000, and therefore these enzymes are unlikely to have any effect on cartilage for the preparation of gelatin.

Fra tysk fremlæggelsesskrift nr. 1.1^5.904 kendes en fremgangsmåde til forbedring af udbyttet af collagen, hvilken fremgangsmåde sammenlignes med fremgangsmåden, der er kendt fra fransk patentskrift nr. 1.1^9.555, hvor 10 kohud behandles med et proteolytisk enzym, såsom takadiasta-se eller pankreatin, efterfulgt af en opvarmning i surt medium. Det højere udbytte, der opnås ifølge det tyske fremlæggelsesskrift 1.1U5-90U opnås kun, når den proteo-lytiske behandling suppleres med en syrehydrolyse.German Patent Specification No. 1.1 ^ 5,904 discloses a method of improving the yield of collagen, which is compared to the method known from French Patent No. 1.1 ^ 9,555 wherein 10 cowhides are treated with a proteolytic enzyme such as takadiastase or pancreatin, followed by heating in acidic medium. The higher yield obtained according to German presentation specification 1.1U5-90U is obtained only when the proteolytic treatment is supplemented with an acid hydrolysis.

15 Fra tysk fremlæggelsesskrift nr. 1.298.211 kendes en fremgangsmåde til fremstilling af opløseligt collagen udfældet i form af fibre, og ved denne fremgangsmåde behandles ben med en enzymatisk opløsning, der er frembragt ved kultivering af stammen Aspergillus niger, og den resul-20 terende viskose opløsning gøres neutral, hvorefter det opløselige collagen udfældes. Denne fremgangsmåde omhandler altså ikke fremstilling af gelatine, men derimod opløselig collagen.15 German Patent Specification No. 1,298,211 discloses a process for producing soluble collagen precipitated in the form of fibers, and in this process, bones are treated with an enzymatic solution produced by cultivation of the strain Aspergillus niger and the resultant viscous solution is neutralized and the soluble collagen precipitates. Thus, this process does not deal with the preparation of gelatin, but rather soluble collagen.

Ingen af disse kendte fremgangsmåder til fremstil-25 ling af gelatine anvender brusk, kødstykker og/eller kødaffald som udgangsmateriale, og ingen af disse kendte fremgangsmåder anvender en enzymatisk blanding, der er fremstillet ud fra næringsmedier af Streptomyces fradiae nr.None of these known methods for the preparation of gelatin use cartilage, cuts of meat and / or meat waste as a starting material, and none of these known methods use an enzymatic mixture prepared from nutrient media of Streptomyces fradiae no.

2019 eller Streptomyces fradiae nr. 1998 fra Museum d'Hi-30 stoire Uaturelle de Paris, og ingen af disse kendte fremgangsmåder gennemfører fremgangsmåden i et trin, men der kræves altid en yderligere behandling ud over den enzymatiske .2019 or Streptomyces fradiae No. 1998 from the Museum d'Histoire Uaturelle de Paris, and none of these known methods perform the procedure in one step, but additional treatment is always required in addition to the enzymatic.

Enzymerne fra Streptomyces fradiae 1998 eller fra 35 Streptomyces fradiae nr. 2019 er kendte, men er hidtil kun blevet anvendt til terapeutiske formål, og det er der- 146630 3 for ikke nærliggende at anvende disse enzymprodukter til fremstilling af gelatine.The enzymes from Streptomyces fradiae 1998 or from Streptomyces fradiae No. 2019 are known, but have so far only been used for therapeutic purposes, and it is therefore not obvious to use these enzyme products for the preparation of gelatin.

Fremgangsmåden ifølge opfindelsen omfatter således en hidtil ukendt et-trins-fremgangsmåde til fremstilling 5 af gelatine, ved hvilken fremgangsmåde der anvendes en til fremstilling af gelatine hidtil ukendt og ikke nærliggende enzymblanding.Thus, the process of the invention comprises a novel one-step process for the preparation of gelatin, using a process for the preparation of novel gelatin and an unrelated enzyme mixture.

Fremgangsmåden ifølge opfindelsen medfører desuden den fordel, at man opnår gelatinen i et meget stort udbyt-10 te på ea 70 % i modsætning til de hidtil kendte fremgangsmåder, hvor man opnår gelatinen i et udbytte på ca 15 ? eller mindre, afhængigt af det udgangsmateriale der anvendes .The process of the invention furthermore has the advantage of obtaining the gelatin in a very large yield of about 70%, in contrast to the known methods, where the gelatin is obtained in a yield of about 15%. or less, depending on the starting material used.

Uden at være bundet til nogle teoretiske betragtninger 15 må det antages, at de enzymatiske blandinger indeholdende Streptomyees fradiaenr. 1998 eller Streptomyces fradiaenr.Without being bound by some theoretical considerations 15, it must be assumed that the enzymatic mixtures containing Streptomployes no. 1998 or Streptomyces fradiaenr.

2019 angriber de glycoproteiner og de mucopolysaccharider, der er bundet til collagenet, og derved opnår man gelatinen i den mængde, der er langt større end den mængde, der 20 opnås ved de kendte fremgangsmåder.In 2019, the glycoproteins and the mucopolysaccharides bound to the collagen attack attack, thereby obtaining the gelatin in the amount far greater than the amount obtained by the known methods.

Endvidere er den efter fremgangsmåden ifølge opfindelsen fremstillede gelatine af en meget fin kvalitet med et meget lavt indhold af mineralske stoffer på mindre end 1 %. Fremgangsmåden ifølge opfindelsen beskrives nærmere i 25 det efterfølgende, hvor: den enzymatiske behandling udføres ved en temperatur mellem + 10°C og 50°C, fortrinsvis mellem 15 og 25°C, den enzymatiske behandling foretages i en tidsperiode på fra 30 min. til 25 timer afhængigt af det anvendte rå-30 materiale, fortrinsvis i fra 17 til 20 timer,Furthermore, the gelatin prepared according to the invention is of a very fine quality with a very low mineral content of less than 1%. The process of the invention is described in more detail below, wherein: the enzymatic treatment is carried out at a temperature between + 10 ° C and 50 ° C, preferably between 15 and 25 ° C, the enzymatic treatment is carried out for a period of time of 30 minutes. to 25 hours depending on the raw material used, preferably from 17 to 20 hours,

den enzymatiske behandling udføres ved en pH-værdi på fra 3 til 9, fortrinsvis fra ^ til 5Sthe enzymatic treatment is carried out at a pH of from 3 to 9, preferably from 5 to 5 S

isoleringen af gelatinen udføres ved filtrering eller centrifugering af reaktioneblandingen og ekstraktion af ge-35 latinen fra den uopløste rest med varmt vand. Temperaturen af det varme vand kan variere fra JO til 9°°c» it U6630 ekstraktionen af gelatinen fra den uopløste rest gennemføres ved kontakt mellem den uopløste rest og varmt vand i en tidsperiode på fra 30 min. til 90 min., isoleringen af gelatinen udføres ved inddampning af 5 den vandige ekstrakt til tørhed enten under reduceret tryk eller ved lyophilisering eller ved forstøvning, den enzymatiske blanding er fortrinsvis den, der opnås ved koncentrering af et næringsmedium indeholdende Streptomyces fradiae, stamme 2019.the isolation of the gelatin is carried out by filtration or centrifugation of the reaction mixture and extraction of the gelatin from the undissolved hot water residue. The temperature of the hot water can vary from JO to 9 ° C. The extraction of the gelatin from the undissolved residue is effected by contact between the undissolved residue and hot water for a period of time of from 30 minutes. to 90 minutes, the isolation of the gelatin is carried out by evaporation of the aqueous extract to dryness either under reduced pressure or by lyophilization or by atomization, the enzymatic mixture being preferably that obtained by concentration of a nutrient medium containing Streptomyces fradiae, strain 2019.

10 Den således fremstillede gelatine kan anvendes i næ ringsmiddelindustrien som gelerende middel, f.eks. i dåsemad, desserter, konfekt, marmelade eller syltetøj. Den kan også anvendes i den pharmaceutiske industri til fremstilling af pharmaceutiske præparater indeholdende gela-15 tine, f.eks. injicerbare opløsninger af gelatine, og den kan endvidere anvendes som bindemateriale ved fremstillingen af tabletter eller mikrobedlets.The gelatin thus prepared can be used in the food industry as a gelling agent, e.g. in canned food, desserts, confectionery, jam or jam. It can also be used in the pharmaceutical industry for the preparation of pharmaceutical compositions containing gelatin, e.g. injectable solutions of gelatin, and it can also be used as binding material in the preparation of tablets or microbedlets.

Endvidere indeholder den opløselige fraktion fra reaktionsblandingen sædvanligvis fra 10 til 20 % opløse-20 ligt materiale, som kan udvindes ved inddampning, forstøvningstørring eller lyophilisering af de vandige opløsninger til tørhed. Den således fremstillede tørre rest kan anvendes som dyrefoder, da den har et stort indhold af proteiner.Furthermore, the soluble fraction of the reaction mixture usually contains from 10 to 20% soluble material which can be recovered by evaporation, spray drying or lyophilization of the aqueous solutions to dryness. The dry residue thus prepared can be used as animal feed as it has a high content of proteins.

Den kan f.eks. blandes i foderblandinger.It can e.g. mixed in compound feed.

25 Det følgende eksempel belyser fremgangsmåden ifølge opfindelsen nærmere.The following example illustrates the process of the invention in more detail.

Eksempel.Example.

Trin AStep A

Udgangsmaterialet kan være brusk, kødstumper eller 30 kødaffald. Dette råmateriale vaskes forud, men det er ikke obligatorisk. Råmaterialet moses ud og suspenderes derefter under omrøring i den vandige opløsning eller suspension af den enzymatiske blanding af Streptomyces fradiae nr. 2019.The starting material may be cartilage, meat slices or 30 meat waste. This raw material is pre-washed, but it is not mandatory. The raw material is mashed out and then suspended with stirring in the aqueous solution or suspension of the 2019 enzymatic mixture of Streptomyces fradiae.

35 Arten af det anvendte vand er uden betydning, der kan anvendes destilleret vand, afioniseret vand eller ledningsvand, uden at det har nogen indflydelse på gennemførel- 146630 5 sen af den enzymatiske reaktion.The nature of the water used is immaterial, which can be used distilled water, deionized water or tap water, without affecting the performance of the enzymatic reaction.

Reaktionsblandingen holdes under omrøring, og pH-værdi-en indstilles på en værdi mellem k og 5, hvilken værdi synes at være optimal. Fra tid til anden kontrolleres pH-værdien 5 således, at den holdes inden for disse grænser.The reaction mixture is kept under stirring and the pH is adjusted to a value between k and 5 which appears to be optimal. From time to time, pH 5 is checked to keep it within these limits.

Reaktionsblandingen holdes på en temperatur på 20°C - 5°C i 17 timer under fortsat omrøring. Herefter filtreres det uopløste materiale fra ved sugning og vaskes tre gange med koldt vand. Filtratet inddampes til tørhed og anvendes 10 som næringsmiddel eller som dyrefoder.The reaction mixture is kept at a temperature of 20 ° C - 5 ° C for 17 hours with continued stirring. Afterwards, the undissolved material is filtered off by suction and washed three times with cold water. The filtrate is evaporated to dryness and used as food or as animal feed.

Den uopløste rest suspenderes under forsigtig omrøring i varmt vand, der forud er opvarmet til 80~90°C, til nedbrydning af den enzymatiske blanding og til opløsning af så meget gelatine som muligt hver gang. Efter en times kontakt 15 filtreres suspensionen ved sugning, det uopløste materiale tørres, og den vandige fase forenes med opløsningerne fra de forudgående gelatineudvindinger.The undissolved residue is suspended with gentle stirring in hot water, preheated to 80 ~ 90 ° C, to decompose the enzymatic mixture and dissolve as much gelatin as possible each time. After one hour of contact, the suspension is filtered by suction, the undissolved material is dried and the aqueous phase is combined with the solutions of the previous gelatin recoveries.

Disse vandige opløsninger klares og affarves ved tilsætning af små mængder trækul, filtreres og inddampes i va-20 kuum. Den tørre rest giver en meget ren gelatine.These aqueous solutions are clarified and decolorized by the addition of small amounts of charcoal, filtered and evaporated in vacuo. The dry residue gives a very pure gelatin.

Den uopløste rest fra filtreringen suspenderes derefter i varmt vand under de samme betingelser. Efter en times forløb skilles opløsningen fra, den uopløste rest vaskes igen med varmt vand og vaskevandet samles med filtratet. Den van-25 dige opløsning destilleres under reduceret tryk, og man får et andet udbytte af gelatine. Udbytte i alt JO %.The undissolved residue from the filtration is then suspended in hot water under the same conditions. After an hour, the solution is separated, the undissolved residue is washed again with warm water and the wash water is collected with the filtrate. The aqueous solution is distilled under reduced pressure to give a different yield of gelatin. Yield in total JO%.

Trin B.Step B.

Til den fra trin A tilbageblivende uopløste rest sættes en ny vægtmængde brusk eller kødaffald. Hele blandingen 30 blandes med vand ved 20°C - 5°C og en yderligere mængde enzymatisk blanding tilsættes. Blandingen holdes under omrøring, og pH-værdien indstilles på mellem ^ og 5. Reaktionen udføres i 17 timer, som angivet i trin A, og den uopløste rest ekstraheres, som beskrevet i trin A.To the residue left in step A, a new amount of cartilage or meat waste is added. The entire mixture 30 is mixed with water at 20 ° C - 5 ° C and an additional amount of enzymatic mixture is added. The mixture is kept under stirring and the pH is adjusted to between 5 and 5. The reaction is carried out for 17 hours as indicated in step A and the undissolved residue is extracted as described in step A.

35 På denne måde vil alt brusk blive omdannet til gela tine .35 In this way, all cartilage will be transformed into gela tine.

6 1466306 146630

Antallet af behandlinger kan gentages så mange gange som nødvendigt, indtil der ikke længere udvindes gelatine.The number of treatments can be repeated as many times as necessary until no gelatin is recovered.

Den enzymatiske blanding fra Streptomyces fradiae har følgende analytiske specificationer: 5 Total proteolytisk aktivitet 7000 Ansonenheder/mg proteolystisk aktivitet, der ikke er inhiberet med aprotinin 5160 Ansonenheder/mg proteolytisk aktivitet, der ikke er inhiberet med trypsin- 1ø inhibitor fra sojabønner 5570 Ansonenheder/mg proteinindhold (Lowry's metode) ^5,7 % beregnet på det tørre materiale.The enzymatic mixture of Streptomyces fradiae has the following analytical specifications: 5 Total proteolytic activity 7000 Anson units / mg proteolytic activity not inhibited with aprotinin 5160 Anson units / mg proteolytic activity not inhibited by trypsin-1o inhibitor from soybeans 5570 Anson units / mg protein content (Lowry's method) ^ 5.7% based on the dry material.

Elektroforese: hovedbestanddel komponent 2, som defi-neret af Morihara og coll. (Bio. Chim. Biophys. Acta 139 (1967) 382).Electrophoresis: major component component 2, as defined by Morihara and Coll. (Bio. Chem. Biophys. Acta 139 (1967) 382).

DK536376AA 1975-12-01 1976-11-29 PROCEDURE FOR GELATINE PREPARATION BY PROCESSING COLLAGENIC MATERIAL WITH PROTEOLYTIC ENZYMES DK146630B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR7536723 1975-12-01
FR7536723A FR2333447A2 (en) 1975-12-01 1975-12-01 ENZYMATIC PRODUCTS OPTIMIZING MUCUS VISCOSITY AND THEIR APPLICATIONS

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Publication Number Publication Date
DK536376A DK536376A (en) 1977-06-02
DK146630B true DK146630B (en) 1983-11-21

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BE (1) BE848937R (en)
CH (1) CH610346A5 (en)
DE (1) DE2654093A1 (en)
DK (1) DK146630B (en)
FR (1) FR2333447A2 (en)
GB (1) GB1540607A (en)
IT (1) IT1076850B (en)
NL (1) NL7613302A (en)
NO (1) NO146607C (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2813075A1 (en) * 1978-03-25 1979-10-11 Roehm Gmbh PROCESSING PROCESS OF RAW MATERIAL CONTAINING COLLAGEN
HU194933B (en) * 1984-09-10 1988-03-28 Valeria Duschanek Process for digesting raw materials containing collagen for producing gelatine
FR2737644B1 (en) * 1995-08-09 1997-10-17 Salaisons D Orly PROTEIN EXTRACTION PROCESS BY ENZYMATIC HYDROLYSIS
US6100381A (en) * 1998-11-03 2000-08-08 Eastman Kodak Company Enzyme method of manufacturing gelatin
US5919906A (en) * 1998-11-05 1999-07-06 Eastman Kodak Company Protease produced gelatin

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GB1540607A (en) 1979-02-14
DK536376A (en) 1977-06-02
NO146607C (en) 1982-11-03
FR2333447A2 (en) 1977-07-01
NL7613302A (en) 1977-06-03
NO146607B (en) 1982-07-26
BE848937R (en) 1977-05-31
NO764082L (en) 1977-06-02
CH610346A5 (en) 1979-04-12
FR2333447B2 (en) 1979-06-15
DE2654093A1 (en) 1977-06-02

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