FR2884256A1 - Enzymatic process for obtaining degraded vegetable gum, comprises producing a vegetable solution in water with an enzyme, leaving the solution to degrade the gum and separating the degraded vegetable gum by centrifugation and/or filtration - Google Patents
Enzymatic process for obtaining degraded vegetable gum, comprises producing a vegetable solution in water with an enzyme, leaving the solution to degrade the gum and separating the degraded vegetable gum by centrifugation and/or filtration Download PDFInfo
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- FR2884256A1 FR2884256A1 FR0650929A FR0650929A FR2884256A1 FR 2884256 A1 FR2884256 A1 FR 2884256A1 FR 0650929 A FR0650929 A FR 0650929A FR 0650929 A FR0650929 A FR 0650929A FR 2884256 A1 FR2884256 A1 FR 2884256A1
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/04—Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
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- Life Sciences & Earth Sciences (AREA)
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- Chemical Kinetics & Catalysis (AREA)
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- General Chemical & Material Sciences (AREA)
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- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
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- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Description
2884256 12884256 1
DESCRIPTIONDESCRIPTION
La présente invention concerne un procédé enzymatique permettant d'obtenir une gomme végétale dégradée. The present invention relates to an enzymatic process for obtaining a degraded vegetable gum.
Dans la présente description, le terme gomme végétale désigne un polysaccharide végétal à poids moléculaire élevé choisi de préférence parmi les polygalactomannanes et, à titre d'exemple non limitatif, parmi le groupe constitué de la gomme de caroube, la gomme de guar et la gomme Tara. In the present description, the term "vegetable gum" denotes a high molecular weight plant polysaccharide preferably chosen from polygalactomannans and, by way of non-limiting example, from the group consisting of locust bean gum, guar gum and gum Tara.
L'objectif de la présente invention est de créer un procédé permettant d'obtenir une gomme végétale dégradée, simple à mettre en oeuvre et présentant des rendements élevés. The object of the present invention is to create a process for obtaining a degraded vegetable gum, simple to implement and having high yields.
Selon la présente invention cet objectif est atteint grâce à un procédé qui comprend les phases suivantes: - réaliser une solution de gomme végétale dans de l'eau à une température comprise entre 0 et 80 C, ladite solution contenant en outre une enzyme choisie parmi un groupe important constitué par la galactomannase, la pectinase, la cellulase, l'hémicellulase et des mélanges de celles-ci, laisser la solution dans lesdites conditions pendant un laps de temps compris entre 8 et 18 heures, de façon à dégrader la gomme végétale, et séparer la gomme végétale dégradée de la suspension. According to the present invention, this objective is achieved by means of a process which comprises the following steps: producing a solution of vegetable gum in water at a temperature of between 0 and 80 ° C., said solution also containing an enzyme chosen from a important group consisting of galactomannase, pectinase, cellulase, hemicellulase and mixtures thereof, leave the solution in said conditions for a period of time between 8 and 18 hours, so as to degrade the vegetable gum, and separate the degraded vegetable gum from the suspension.
La phase de dégradation proprement dite du procédé de la présente invention est effectuée dans un réacteur agité qui permet d'obtenir une bonne solubilisation de la gomme végétale. Ladite phase de dégradation peut être suivie de phases de neutralisation de la solution grâce à l'ajout d'un sel et/ou à la désactivation de l'enzyme. The actual degradation phase of the process of the present invention is carried out in a stirred reactor which makes it possible to obtain good solubilization of the vegetable gum. Said degradation phase may be followed by neutralization phases of the solution through the addition of a salt and / or the deactivation of the enzyme.
De manière avantageuse, le rapport en poids entre la gomme végétale et l'eau dans la solution initiale est compris entre 0,2 et 0,5 et est de préférence égal à 0,4, tandis que la concentration en poids d'enzyme dans la solution initiale est comprise entre 0,01 et 0,3%. La gomme végétale peut être ajoutée à la solution en une seule charge ou en plusieurs charges décalées dans le temps. Advantageously, the weight ratio between the vegetable gum and the water in the initial solution is between 0.2 and 0.5 and is preferably equal to 0.4, whereas the concentration by weight of enzyme in the initial solution is between 0.01 and 0.3%. The vegetable gum can be added to the solution in a single charge or in several charges shifted in time.
Toujours de manière avantageuse, le rapport en poids entre la gomme végétale et l'eau dans la solution diluée est compris entre 0,1 et 0,25 et est de préférence égal à 0,2. Still advantageously, the ratio by weight between the vegetable gum and the water in the diluted solution is between 0.1 and 0.25 and is preferably equal to 0.2.
A titre d'exemple, le sel de neutralisation peut être du citrate de sodium. By way of example, the neutralization salt may be sodium citrate.
La désactivation de l'enzyme peut être effectuée grâce à la pasteurisation à une température comprise entre 80 et 95 C et de préférence à 85 C. The deactivation of the enzyme can be carried out by pasteurization at a temperature of between 80 and 95 ° C. and preferably at 85 ° C.
La séparation de la solution de gomme végétale dégradée peut être réalisée grâce à une centrifugation et/ou une filtration, et la gomme végétale dégradée séparée de la solution peut être soumise à un séchage. Separation of the degraded vegetable gum solution can be achieved by centrifugation and / or filtration, and the degraded vegetable gum separated from the solution can be subjected to drying.
D'autres avantages et caractéristiques de la présente invention apparaîtront dans les exemples de réalisation qui suivent, fournis à titre indicatif et non limitatif. Other advantages and features of the present invention will become apparent in the following exemplary embodiments, provided for information and not limitation.
Exemple 1:Example 1
sont introduits, dans un Becher, 800 ml d'eau déionisée auxquels sont ajoutés 90 mg d'une solution enzymatique telle quelle la température est portée à 40 C 2 C et on ajuste le pH 4 avec de l'acide formique; É 160 grammes de gomme Tara sont ajoutés en maintenant une forte agitation et en tamisant la poudre introduite grâce à une petite passoire; É la température et le mouvement d'agitation doivent être maintenus pendant environ 10 heures; É la solution doit être refroidie et filtrée, afin d'obtenir environ 740 g d'une solution claire contenant environ 16% de matière sèche; et É la solution doit être séchée afin d'obtenir de la gomme Tara dégradée. 800 ml of deionized water are introduced into a beaker, to which are added 90 mg of an enzymatic solution such that the temperature is brought to 40 ° C. and the pH 4 is adjusted with formic acid; É 160 grams of Tara gum are added maintaining a strong agitation and sieving the powder introduced through a small colander; The temperature and stirring motion must be maintained for approximately 10 hours; The solution must be cooled and filtered to obtain about 740 g of a clear solution containing about 16% dry matter; and the solution must be dried in order to obtain degraded Tara gum.
Exemple 2:Example 2
É sont introduits, dans un Becher, 800 ml d'eau déionisée auxquels sont ajoutés 90 mg d'une solution enzymatique telle quelle; É la température est portée à 40 C 2 C et on ajuste le pH 4 avec de l'acide formique; É 16 grammes de gomme Tara sont ajoutés toutes les heures, 10 fois de suite, en maintenant une forte agitation et en tamisant la poudre introduite grâce à une petite passoire; É la solution doit être refroidie et filtrée afin d'obtenir environ 740 g d'une solution claire contenant environ 16% de matière sèche; et É la solution doit être séchée afin d'obtenir de la gomme Tara dégradée. 20 800 ml of deionized water are added to a beaker to which are added 90 mg of an enzymatic solution as it is; The temperature is brought to 40 ° C. and the pH 4 is adjusted with formic acid; E 16 grams Tara gum are added every hour, 10 times in a row, maintaining strong agitation and sieving the powder introduced through a small colander; The solution should be cooled and filtered to obtain about 740 g of a clear solution containing about 16% dry matter; and the solution must be dried in order to obtain degraded Tara gum. 20
Exemple 3:Example 3
É sont introduits, dans un Becher, 800 ml d'eau déionisée auxquels sont ajoutés 90 mg d'une solution enzymatique telle quelle; É la température est portée à 40 C 2 C et on ajuste le pH 4 avec de l'acide formique; e 16 grammes de gomme Tara sont ajoutés toutes les heures, 10 fois de suite, en maintenant une forte agitation et en tamisant la poudre introduite grâce à une petite passoire; 2884256 4 É la solution doit être refroidie et pasteurisée afin d'éliminer l'activité résiduelle de l'enzyme; É la solution doit être filtrée afin d'obtenir environ 740 g d'une solution claire contenant environ 16% de matière sèche; et É la solution doit être séchée afin d'obtenir de la gomme Tara dégradée. Bien entendu, tout en restant dans le cadre de l'invention, les détails de réalisation et les modes de réalisation pourront varier considérablement par rapport à ce qui est décrit seulement à titre d'exemple, sans pour cela sortir du cadre de la présente invention. 1. 2. 3. 4. 5. 800 ml of deionized water are added to a beaker to which are added 90 mg of an enzymatic solution as it is; The temperature is brought to 40 ° C. and the pH 4 is adjusted with formic acid; e 16 grams of Tara gum are added every hour, 10 times in succession, maintaining a strong agitation and sieving the powder introduced through a small colander; The solution must be cooled and pasteurized to eliminate the residual activity of the enzyme; The solution should be filtered to obtain about 740 g of a clear solution containing about 16% dry matter; and the solution must be dried in order to obtain degraded Tara gum. Of course, while remaining within the scope of the invention, the details of implementation and the embodiments may vary considerably compared to what is described only by way of example, without departing from the scope of the present invention. . 1. 2. 3. 4. 5.
2884256 52884256 5
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT000180A ITTO20050180A1 (en) | 2005-03-18 | 2005-03-18 | ENZYMATIC PROCEDURE FOR OBTAINING DEGRADED VEGETABLE RUBBER |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2884256A1 true FR2884256A1 (en) | 2006-10-13 |
FR2884256B1 FR2884256B1 (en) | 2011-03-04 |
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ID=37054990
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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FR0650929A Expired - Fee Related FR2884256B1 (en) | 2005-03-18 | 2006-03-17 | ENZYMATIC PROCESS FOR OBTAINING A DEGRADED PLANT GUM |
Country Status (3)
Country | Link |
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DE (2) | DE102006012415B4 (en) |
FR (1) | FR2884256B1 (en) |
IT (1) | ITTO20050180A1 (en) |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2506328A1 (en) * | 1981-05-22 | 1982-11-26 | Inst Francais Du Petrole | ENZYMATIC PROCESS FOR TREATING XANTHAN GUMS WITH A VIEW TO IMPROVING THE FILTRATION OF THEIR AQUEOUS SOLUTIONS |
DE3785449T2 (en) * | 1987-04-14 | 1993-07-29 | Inst Francais Du Petrol | ENZYMATIC METHOD FOR TREATING XANTHAN GUM TO IMPROVE THE FILTERABILITY OF YOUR AQUEOUS SOLUTIONS. |
DE3830469A1 (en) * | 1988-09-08 | 1990-03-15 | Gruenau Gmbh Chem Fab | METHOD FOR PRODUCING POWDER-SHAPED, WATER-WASHABLE, ENZYMATICALLY DEGRADED HETEROPOLYSACCHARIDES |
DE4411681A1 (en) * | 1994-04-05 | 1995-10-12 | Hoechst Ag | Process for the preparation of low molecular weight polysaccharide ethers |
-
2005
- 2005-03-18 IT IT000180A patent/ITTO20050180A1/en unknown
-
2006
- 2006-03-17 FR FR0650929A patent/FR2884256B1/en not_active Expired - Fee Related
- 2006-03-17 DE DE102006012415.4A patent/DE102006012415B4/en not_active Expired - Fee Related
- 2006-03-17 DE DE102006012414.6A patent/DE102006012414B4/en not_active Expired - Fee Related
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Publication number | Publication date |
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DE102006012415B4 (en) | 2020-09-03 |
FR2884256B1 (en) | 2011-03-04 |
DE102006012414A1 (en) | 2006-11-02 |
ITTO20050180A1 (en) | 2006-09-19 |
DE102006012414B4 (en) | 2017-06-29 |
DE102006012415A1 (en) | 2006-12-14 |
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