WO1989009793A1 - Amylaceous material and process for producing it - Google Patents

Amylaceous material and process for producing it Download PDF

Info

Publication number
WO1989009793A1
WO1989009793A1 PCT/FR1989/000153 FR8900153W WO8909793A1 WO 1989009793 A1 WO1989009793 A1 WO 1989009793A1 FR 8900153 W FR8900153 W FR 8900153W WO 8909793 A1 WO8909793 A1 WO 8909793A1
Authority
WO
WIPO (PCT)
Prior art keywords
water
approximately
starchy material
starch
rate
Prior art date
Application number
PCT/FR1989/000153
Other languages
French (fr)
Inventor
Paul Colonna
Jean Tayeb
Guy Della Valle
Original Assignee
Institut National De La Recherche Agronomique (Inr
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 Institut National De La Recherche Agronomique (Inr filed Critical Institut National De La Recherche Agronomique (Inr
Publication of WO1989009793A1 publication Critical patent/WO1989009793A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B30/00Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
    • C08B30/12Degraded, destructured or non-chemically modified starch, e.g. mechanically, enzymatically or by irradiation; Bleaching of starch
    • C08B30/14Cold water dispersible or pregelatinised starch
    • 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
    • A23L13/426Addition of proteins, carbohydrates or fibrous material from vegetable origin other than sugars or sugar alcohols
    • 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
    • A23L13/60Comminuted or emulsified meat products, e.g. sausages; Reformed meat from comminuted meat product
    • A23L13/65Sausages
    • 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
    • A23L29/00Foods or foodstuffs containing additives; Preparation or treatment thereof
    • A23L29/20Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents
    • A23L29/206Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of vegetable origin
    • A23L29/212Starch; Modified starch; Starch derivatives, e.g. esters or ethers

Definitions

  • Starchy material and its manufacturing process belongs to the technological field of the physical transformation of starch, and it relates to a starchy material having the following interesting properties, which is found for the first time in combination, to know:
  • the present invention also relates to a process for manufacturing this new starchy material, as well as to its applications.
  • Starch is found in a wide variety of plants, such as cereals, legumes and tubers. It is used for about 50 to 80% by weight (dry matter) in the composition of cereals, for about 25 to 50% by weight (dry matter) in that of legumes, and for about 60 to 95% by weight (dry matter) in that of tubers. It is in the form of dense granular entities (its volumetric mass which is approximately 1.5 g / cm 3 ), which are insoluble in cold water and whose shape and dimensions vary depending on the species and state of maturity.
  • These grains normally consist of a mixture of two polysaccharides, namely amylose and amylopectin, as well as lipid (in an amount of about 0.1 to 1.5% by weight) and protein (in the amount of about 0.1 to 0.6% by weight).
  • Native starch grains have a molecular organization with a tangential axis at the surface of the grain. In addition, areas crystals give the whole a very strong cohesion in the native state.
  • starch grains When subjected to excess water heating, these starch grains absorb water, at a rate of 50 to 59 times their weight of water, and part of their content, essentially consisting of amylose, solubilizes. These two transformations cause an increase in the apparent viscosity of the starch suspension, which constitutes starching. Overall, a job should always be considered as a mixture of swollen, fragmented (ghost) grains and dispersed macromolecules, which have spread out of the granules.
  • the dispersibility of starch in aqueous media at high temperature often remains problematic, due to the difficulty of obtaining homogeneous media. However, the state of dispersion thus obtained is strictly unstable below 60-65 ° C.
  • amylose and amylopectin solution separates into two phases, namely a phase rich in polymers swollen by the solvent and a phase depleted in polymers.
  • a second phenomenon is the subsequent appearance of crystalline zones by the formation of hydrogen bonds between amylose and / or amylopeptin links: the gels thus formed are of the composite type, with particles rich in amylopeptin contained in a network of amyloidosis.
  • the properties (a) and (b) mentioned above are important. From the point of view of the implementation of the methods, property (c) is important for obtaining the desired effect, namely the thickening and starch gelling agent after a dispersion step. From this thickening and gelling nature, the binding properties of starch flow directly.
  • various physical technologies have been proposed so far, which lead to modified starches.
  • the first type of technology that can be mentioned is that of drying the native starch on one or more heating cylinders, this drying possibly being preceded by a treatment by "jet-cooker". This technique leads to gelatinized products, with a high water absorbing power. However, it has the drawback of being difficult to use due to the formation of lumps and of being very costly from an energy point of view. It can be indicated that this technique makes it possible to obtain the property (c) mentioned above, but not the properties (a) and (b).
  • the object of the present invention is to overcome the drawbacks of the state of the art observed in the processes for physical modification of starch, in order to obtain the combination of the three properties (a) to (c) previously indicated, these properties being further improved compared to starches complexed with monoglycerides, as described in the aforementioned US patent.
  • a physically modified starch in the form of macroscopic particles, easily dispersible in water at all temperatures, having a strong thickening power by absorption of water, dissolving slowly at high temperatures and being insoluble at room temperature.
  • the new starchy material which is the subject of the present invention is characterized in that it is in the form of macroscopic particles with a size of between approximately 0.5 and 5 mm, the solubility (S) of which water is between 15 and 65% approximately, and the swelling rate (G) in water is between 15 and 45% approximately, (S) and (G) being calculated according to the formulas below, on samples 0.5 g of dry matter, stirred in 50 ml of water for 1/2 hour in a water bath at 65 ° C, the medium then undergoing centrifugation:
  • the starchy material according to the invention can also be characterized by its consistency with the Brabender viscoamylograph, which is between approximately 30 and 900 cmg at the start of the thermal cycle and between approximately 900 and 1500 cmg at the end of the thermal cycle, the samples being studied. at a concentration of 6-7% and the thermal cycle being defined as follows: - heating with constant progression, at a rate of + 1.5 ° C / minute up to 96oC;
  • starchy material according to the invention its degree of gelatinization, measured by the swelling test in a 0.01 N potassium hydroxide medium, which is between approximately 50 and 100. In this test , increased sediment volume is correlated with grain damage starch.
  • the starchy material according to the invention comes in particular from cassava starch or potato starch, which are common starches of industrial origin.
  • the humidity of the starchy material is in particular less than 10% by weight relative to the total material.
  • the starchy material of the invention may contain at least one amylose complexing agent, at a rate of at most 3% by weight relative to said starchy material.
  • a process for the manufacture of the starchy material of the invention consists in: (1) subjecting to a wave treatment having a frequency between 0.9 and 300 GHz, a medium containing starch, water at a rate from 39 to 50% by weight relative to the mass of the starch, and, optionally, at least one amylose complexing agent at a rate of at most 3% by weight relative to the mass of the starch;
  • step (1) the frequency of 2.45 GHz is used in particular; the treatment is carried out until gelatinization of at least 50% of the starch, and preferably all of the starch, for a period of approximately 0.5 to 15 minutes, in particular from 3 to 4 minutes , and at a temperature of the order of 50 to 98 ° C, in particular from 80 to 98 ° C.
  • the drying of step (3) it can be carried out at a temperature of the order of 80 to 130 ° C., in an apparatus constituted in particular by an oven, continuous or not, with a circulation of hot air, whose humidity can be controlled or not.
  • the starchy material according to the invention is advantageously used as an additive for food products, because of its binding properties, and, in particular, it can constitute an additive for cooked dishes, cold meats, sauces, etc., where it replaces the fat of the formulation, so as to obtain low calorie foods.
  • the preparation of the starchy material according to the invention is illustrated, as it has just been defined above.
  • Country pâté is prepared according to the two formulations below:
  • the preparation is carried out by simple mixing of the ingredients, the mixture then being conventionally subjected to cooking.
  • the product containing the starchy material of the invention the latter is incorporated as late as possible in the mixture.
  • the comparison of the two products shows that the or gano 1 ep tic qualities are preserved and that the caloric value of the product containing the starchy material of the invention is reduced from 20 to 40%.
  • Starchy material of the invention 0 7 qs 100 with spices, lactose, ascorbic acid, polyphosphates
  • Example 1 The preparation is carried out as indicated in Example 1 and the results concerning the organoleptic qualities and the caloric value are similar to those of Example 1.

Abstract

An amylaceous material is readily dispersible in water at all temperatures, dissolves at high temperature, has a marked capacity for thickening by absorption of water, and exists in the form of macroscopic particles between 0.5 and 5 mm in size. The material has a solubility (5) in water of 15 to 65 %, and a swelling ratio (6) in water of 15 to 45 %. S = (initial mass (dry matter) - mass of cull (dry matter))/initial mass (dry matter) x 100, and G = (water added initially - volume of supernatant)/mass of cull (dry matter), S and G being calculated for 0.5 g samples of dry matter stirred in 50 ml of water for 1/2 an hour on a water bath at 65°C and then centrifuged. To prepare the material, a medium containing starch, 30 to 50 % by weight of water, referred to the mass of starch, and if necessary an amylose-complexing agent is subjected to a wave treatment (0.9-300 GHz). The paste so obtained is then fragmented and dried.

Description

"Matière amylacée et son procédé de fabrication" La présente invention appartient au domaine technologique de la transformation physique de l'amidon, et elle porte sur une matière amylacée présentant les propriétés intéressantes suivantes, que l'on trouve pour la première fois en combinaison, à savoir: "Starchy material and its manufacturing process" The present invention belongs to the technological field of the physical transformation of starch, and it relates to a starchy material having the following interesting properties, which is found for the first time in combination, to know:
(a) dispersibilité aisée dans l'eau à toutes temperatures; (b) dissolution à haute température; et(a) easy dispersibility in water at all temperatures; (b) dissolving at high temperature; and
(c) fort pouvoir épaississant par absorption d'eau.(c) strong thickening power by water absorption.
La présente invention porte également sur un procédé de fabrication de cette nouvelle matière amylacée, ainsi que sur ses applications. L'amidon est contenu dans une large variété de végétaux, tels que les céréales, les légumineuses et les tubercules. Il entre pour environ 50 à 80% en poids (matière sèche) dans la composition des céréales, pour environ 25 à 50% en poids (matière sèche) dans celle des légumineuses, et pour environ 60 à 95% en poids (matière sèche) dans celle des tubercules. Il se présente sous la forme d'entités granulaires denses (sa masse volumi que est d'environ 1,5 g/cm3), qui sont insolubles dans l'eau froide et dont la forme et les dimensions varient en fonction de l'espèce et de l'état de maturité. Ces grains sont normalement constitués par un mélange de deux polysaccharides, à savoir l'amylose et l'amylopectine, ainsi que de contaminants lipidiques (à raison de 0,1 à 1,5% en poids environ) et protéiques (à raison d'environ 0,1 à 0,6% en poids). Les grains d'amidon natifs présentent une organisation moléculaire d'axe tangentiel à la surface du grain. En outre, des zones cristallines confèrent à l'ensemble une très forte cohésion h l'état natif.The present invention also relates to a process for manufacturing this new starchy material, as well as to its applications. Starch is found in a wide variety of plants, such as cereals, legumes and tubers. It is used for about 50 to 80% by weight (dry matter) in the composition of cereals, for about 25 to 50% by weight (dry matter) in that of legumes, and for about 60 to 95% by weight (dry matter) in that of tubers. It is in the form of dense granular entities (its volumetric mass which is approximately 1.5 g / cm 3 ), which are insoluble in cold water and whose shape and dimensions vary depending on the species and state of maturity. These grains normally consist of a mixture of two polysaccharides, namely amylose and amylopectin, as well as lipid (in an amount of about 0.1 to 1.5% by weight) and protein (in the amount of about 0.1 to 0.6% by weight). Native starch grains have a molecular organization with a tangential axis at the surface of the grain. In addition, areas crystals give the whole a very strong cohesion in the native state.
Soumis à un chauffage en excès d'eau, ces grains d'amidon absorbent de l'eau, à raison de 50 à 59 fois leur poids d'eau, et une partie de leur contenu, essentiellement constituée par de l'amylose, se solubilise. Ces deux transformations provoquent une augmentation de la viscosité apparente de la suspension d'amidon, ce qui constitue l'empesage. Globalement, un empois doit toujours être considéré comme un mélange de grains gonflés, fragmentés (fantômes) et de macromolécules dispersées, qui ont diffusé hors des granules. La dis- persibilité de l'amidon dans des milieux aqueux à haute température reste souvent problématique, en raison de la difficulté d'obtention de milieux homogènes. Cependant, l'état de dispersion ainsi obtenu est strictement instable au-dessous de 60-65°C. La solution d'amylose et d'amylopectine se sépare en deux phases, à savoir une phase riche en polymères gonflés par le solvant et une phase appauvrie en polymères. Un second phénomène est l'apparition ultérieure de zones cristallines par formation de liaisons hydrogène entre des chaînons d'amylose et/ou d'amylopeptine: les gels ainsi formés sont de type composite, avec des particules riches en amylopeptine enserrées dans un réseau d'amylose.When subjected to excess water heating, these starch grains absorb water, at a rate of 50 to 59 times their weight of water, and part of their content, essentially consisting of amylose, solubilizes. These two transformations cause an increase in the apparent viscosity of the starch suspension, which constitutes starching. Overall, a job should always be considered as a mixture of swollen, fragmented (ghost) grains and dispersed macromolecules, which have spread out of the granules. The dispersibility of starch in aqueous media at high temperature often remains problematic, due to the difficulty of obtaining homogeneous media. However, the state of dispersion thus obtained is strictly unstable below 60-65 ° C. The amylose and amylopectin solution separates into two phases, namely a phase rich in polymers swollen by the solvent and a phase depleted in polymers. A second phenomenon is the subsequent appearance of crystalline zones by the formation of hydrogen bonds between amylose and / or amylopeptin links: the gels thus formed are of the composite type, with particles rich in amylopeptin contained in a network of amyloidosis.
Pour les différentes applications industrielles des amidons, en particulier comme additifs pour plats cuisinés, les propriétés (a) et (b) rappelées ci-dessus sont importantes. Du point de vue de la mise en oeuvre des procédés, la propriété (c) est importante pour obtenir l'effet recherché, à savoir le caractère épaississant et gélifiant de l'amidon après une étape de dispersion. De cette nature épaississante et gélifiante, découlent directement les propriétés liantes de l'amidon. Pour faciliter la dispersion et/ou modifier les propriétés fonctionnelles, différentes technologies physiques ont été proposées jusqu' ici, lesquelles conduisent à des amidons modifiés. Le premier type de technologie que l'on peut mentionner est celui du séchage de l'amidon natif sur un ou des cylindre(s) chauffant(s), ce séchage étant précédé éventuellement par un traitement par "jet-cooker". Cette technique conduit à des produits gélatinisés, à fort pouvoir absorbant d'eau. Cependant, il présente l' inconvénient d'une mise en oeuvre délicate en raison de la formation de grumeaux et d'être très coûteux au plan énergétique. On peut indiquer que cette technique permet d'obtenir la propriété (c) mentionnée ci-dessus, mais non les propriétés (a) et (b).For the various industrial applications of starches, in particular as additives for ready meals, the properties (a) and (b) mentioned above are important. From the point of view of the implementation of the methods, property (c) is important for obtaining the desired effect, namely the thickening and starch gelling agent after a dispersion step. From this thickening and gelling nature, the binding properties of starch flow directly. To facilitate the dispersion and / or modify the functional properties, various physical technologies have been proposed so far, which lead to modified starches. The first type of technology that can be mentioned is that of drying the native starch on one or more heating cylinders, this drying possibly being preceded by a treatment by "jet-cooker". This technique leads to gelatinized products, with a high water absorbing power. However, it has the drawback of being difficult to use due to the formation of lumps and of being very costly from an energy point of view. It can be indicated that this technique makes it possible to obtain the property (c) mentioned above, but not the properties (a) and (b).
On connaît également la technique de cuisson-extrusion, laquelle conduit à des produits gélatinisés, très hydrosolubles, mais de faible pouvoir épaississant, en raison de la rupture des chaînes d'amylose et d'amylopectine. Par ailleurs, on observe la formation de grumeaux à toutes températures. Il en résulte que l'on obtient sans doute la propriété (b), mais non les propriétés (a) et (c) indiquées ci-dessus.The cooking-extrusion technique is also known, which leads to gelatinized products, very water-soluble, but of low thickening power, due to the breaking of the amylose and amylopectin chains. Furthermore, we observe the formation of lumps at all temperatures. As a result, we probably obtain property (b), but not properties (a) and (c) indicated above.
Enfin, on peut mentionner les procédés de traitement thermique en humidité contrôlée, c'est-à-dire les procédés dits HMT (Heat Moisture Treatment). Dans ces procédés, on n'observe pas de rupture des macromolécules, la structure fantôme des grains étant conservée. Egalement, la formation de grumeaux à haute température est observée. Dans ce cas, au moins la propriété (a) n'est pas obtenue. On connaît par ailleurs, par exemple par le brevet US-A-4491483, la modification chimique des amidons par formation de complexes avec des acides gras ou des monoglycérides, pour répondre à la nécessité d'une bonne dispersibilité. Une autre référence illustrant l'art antérieur est l'article paru dans Journal of the Korean Society of Food and Nutrition vol.13 n° 3 p. 268-274, cited in Food Science and Technology Abstracts 85-05-10043 Mai 1985, nº 8502 81 84. Cet article concerne le chauffage par microondes de l'amidon de pomme de terre, mais il n'enseigne pas les conditions de traitement permettant d'obtenir un produit sec, ayant des propriétés particulières du type décrit ci-après. En fait un tel article ne contient qu'une étude générale des effets physicochimiques du chauffage par microondes sur l'amidon de pomme de terre, sans fournir aucune indication sur les caractéristiques des produits à réaliser. EP-0059050 concerne un traitement d'amidon par rayonnement UHF, qui donne des résultats voisins de celui dénommé "heat-moisture treatment", bien connu pour modifier légèrement l'amidon. Dans le procédé décrit, l'amidon est essentiellement présenté sous forme granulaire. Ainsi l'art antérieur ne co n t ien t pas l'enseignement d'une phase de traitement aux micro-ondes pour gélatiniser l'amidon, couplée à une phase de séchage. On ne trouve pas non plus d' indication sur une matière amylacée qui, en même temps: - est aisément dispersible dans l'eau à toute température,Finally, we can mention the heat treatment processes in controlled humidity, that is to say the so-called HMT (Heat Moisture Treatment) processes. In these methods, no macromolecule rupture, the phantom structure, is observed grains being preserved. Also, the formation of lumps at high temperature is observed. In this case, at least property (a) is not obtained. We also know, for example from US-A-4491483, the chemical modification of starches by formation of complexes with fatty acids or monoglycerides, to meet the need for good dispersibility. Another reference illustrating the prior art is the article published in Journal of the Korean Society of Food and Nutrition vol.13 n ° 3 p. 268-274, cited in Food Science and Technology Abstracts 85-05-10043 May 1985, no. 8502 81 84. This article concerns microwave heating of potato starch, but it does not teach the processing conditions making it possible to obtain a dry product, having particular properties of the type described below. In fact, such an article contains only a general study of the physicochemical effects of microwave heating on potato starch, without providing any indication of the characteristics of the products to be produced. EP-0059050 relates to a starch treatment by UHF radiation, which gives results close to that called "heat-moisture treatment", well known for slightly modifying starch. In the process described, the starch is essentially presented in granular form. Thus, the prior art does not entail the teaching of a microwave treatment phase to gelatinize the starch, coupled with a drying phase. There is also no indication on a starchy material which, at the same time: - is easily dispersible in water at any temperature,
- absorbe fortement l'eau avec une vitesse lente de solubilisation, ce qui conduit à un pouvoir épaississant élevé.- strongly absorbs water with a slow rate of solubilization, which leads to a high thickening power.
La présente invention a pour but de surmonter les inconvénients de l'état de la technique constatés dans les procédés de modification physique de l'amidon, afin d'obtenir la combinaison des trois propriétés (a) à (c) précédemment indiquées, ces propriétés étant encore améliorées par rapport aux amidons complexés à des monoglycérides, tels que décrits dans le brevet américain précité.The object of the present invention is to overcome the drawbacks of the state of the art observed in the processes for physical modification of starch, in order to obtain the combination of the three properties (a) to (c) previously indicated, these properties being further improved compared to starches complexed with monoglycerides, as described in the aforementioned US patent.
Cet objectif est atteint par un amidon modifié physiquement, se présentant sous la forme de particules macroscopiques, facilement dispersible dans l'eau à toutes températures, présentant un fort pouvoir épaississant par absorption d'eau, se dissolvant lentement aux températures é l e v é e s et étant insoluble à la température ambiante.This objective is achieved by a physically modified starch, in the form of macroscopic particles, easily dispersible in water at all temperatures, having a strong thickening power by absorption of water, dissolving slowly at high temperatures and being insoluble at room temperature.
La nouvelle matière amylacée qui fait l'objet de la présente invention est caractérisée par le fait qu'elle se présente sous la forme de particules macroscopiques de dimension comprise entre environ 0,5 et 5 mm, dont la solubilité (S) dans l'eau est comprise entre 15 et 65% environ, et le taux de gonflement (G) dans l'eau est compris entre 15 et 45% environ, (S) et (G) étant calculés selon les formules ci-après, sur des échantillons de 0,5 g de matière sèche, agitée dans 50 ml d'eau pendant 1/2 heure au bain-marie à 65°C, le milieu subissant ensuite une centrifugation:
Figure imgf000008_0001
The new starchy material which is the subject of the present invention is characterized in that it is in the form of macroscopic particles with a size of between approximately 0.5 and 5 mm, the solubility (S) of which water is between 15 and 65% approximately, and the swelling rate (G) in water is between 15 and 45% approximately, (S) and (G) being calculated according to the formulas below, on samples 0.5 g of dry matter, stirred in 50 ml of water for 1/2 hour in a water bath at 65 ° C, the medium then undergoing centrifugation:
Figure imgf000008_0001
Figure imgf000008_0002
Figure imgf000008_0002
La matière amylacée selon l'invention peut être également caractérisée par sa consistance au viscoamylographe Brabender, qui est comprise entre environ 30 et 900 cmg au début du cycle thermique et entre environ 900 et 1500 cmg à la fin du cycle thermique, les échantillons étant étudiés à une concentration de 6-7% et le cycle thermique étant défini comme suit: - chauffage à progression constante, à raison de + 1,5°C/minute jusqu'à 96ºC;The starchy material according to the invention can also be characterized by its consistency with the Brabender viscoamylograph, which is between approximately 30 and 900 cmg at the start of the thermal cycle and between approximately 900 and 1500 cmg at the end of the thermal cycle, the samples being studied. at a concentration of 6-7% and the thermal cycle being defined as follows: - heating with constant progression, at a rate of + 1.5 ° C / minute up to 96ºC;
- maintien de cette température pendant 15 minutes; et- maintaining this temperature for 15 minutes; and
- refroidissement à progression constante, à raison de - 1,5°C/minute jusqu'à 30°C.- constant progression cooling, at a rate of - 1.5 ° C / minute to 30 ° C.
Elle peut être également caractérisée par la consistance au faronographe Brabender d'une suspension de 75g de ladite matière dans 100 ml d'eau, qui a été soumise à un pétrissage intensif, qui est comprise entre environ 300 et 1000 minute au bout de 15 minutes.It can also be characterized by the consistency with the Brabender faronograph of a suspension of 75 g of said material in 100 ml of water, which has been subjected to intensive kneading, which is between approximately 300 and 1000 minutes after 15 minutes. .
Par ailleurs, on peut également mentionner comme autre caractéristique de la matière amylacées selon l'invention, son degré de gélatinisation, mesuré par le test de gonflement en milieu potasse 0,01 N, qui est compris entre environ 50 et 100. Dans ce test, l'accroissement de volume du sédiment est corrélé à l'endommagement des grains d'amidon.Furthermore, it is also possible to mention as another characteristic of the starchy material according to the invention, its degree of gelatinization, measured by the swelling test in a 0.01 N potassium hydroxide medium, which is between approximately 50 and 100. In this test , increased sediment volume is correlated with grain damage starch.
La matière amylacée selon l'invention est issue notamment de l'amidon de manioc ou d'amidon de pomme de terre, qui sont des amidons courants d'origine industrielle.The starchy material according to the invention comes in particular from cassava starch or potato starch, which are common starches of industrial origin.
Enfin, l'humidité de la matière amylacée est notamment inférieure à 10% en poids par rapport à la matière totale.Finally, the humidity of the starchy material is in particular less than 10% by weight relative to the total material.
La matière amylacée de l' invention peut renfermer au moins un agent complexant de l'amylose, à raison d'au plus 3% en poids par rapport à ladite matière amylacée.The starchy material of the invention may contain at least one amylose complexing agent, at a rate of at most 3% by weight relative to said starchy material.
Un procédé de fabrication de la matière amylacée de l'invention consiste à: (1) soumettre à un traitement par ondes ayant une fréquence comprise entre 0,9 et 300 GHz, un milieu contenant de l'amidon, de l'eau à raison de 39 à 50% en poids par rapport à la masse de l'amidon, et, éventuellement, au moins un agent complexant de l'amylose à raison d'au plus 3% en poids par rapport à la masse de l'amidon;A process for the manufacture of the starchy material of the invention consists in: (1) subjecting to a wave treatment having a frequency between 0.9 and 300 GHz, a medium containing starch, water at a rate from 39 to 50% by weight relative to the mass of the starch, and, optionally, at least one amylose complexing agent at a rate of at most 3% by weight relative to the mass of the starch;
(2) fragmenter la pâte ainsi obtenue en éléments de taille comprise entre environ 0,5 et 5 mm; et(2) fragmenting the dough thus obtained into elements of size between approximately 0.5 and 5 mm; and
(3) sécher pour ramener l'humidité du produit à une valeur désirée.(3) dry to bring the humidity of the product to a desired value.
A l'étape (1), on utilise en particulier la fréquence de 2,45 GHz; on conduit le traitement jusqu'à gélatinisation d'au minimum 50% de l'amidon, et de préférence, de la totalité de l'amidon, pendant une durée d'environ 0,5 à 15 minutes, notamment de 3 à 4 minutes, et à une température de l'ordre de 50 à 98°C, en particulier de 80 à 98°C. Quant au séchage de l'étape (3), il peut être conduit à une température de l'ordre de 80 à 130°C, dans un appareillage constitué notamment par un four, continu ou non, avec une circulation d'air chaud, dont l'humidité peut être contrôlée ou non.In step (1), the frequency of 2.45 GHz is used in particular; the treatment is carried out until gelatinization of at least 50% of the starch, and preferably all of the starch, for a period of approximately 0.5 to 15 minutes, in particular from 3 to 4 minutes , and at a temperature of the order of 50 to 98 ° C, in particular from 80 to 98 ° C. As for the drying of step (3), it can be carried out at a temperature of the order of 80 to 130 ° C., in an apparatus constituted in particular by an oven, continuous or not, with a circulation of hot air, whose humidity can be controlled or not.
La matière amylacée selon l'invention est utilisée avantageusement comme additif pour produits alimentaires, en raison de ses propriétés liantes, et, en particulier, elle peut constituer un additif pour plats cuisinés, charcuterie, sauces, etc., où elle se substitue à la matière grasse de la formulation, de façon à obtenir des aliments basses calories. Dans les exemples qui suivent, on a illustré la préparation de la matière amylacée selon l'invention, telle qu'elle vient d'être définie ci-dessus.The starchy material according to the invention is advantageously used as an additive for food products, because of its binding properties, and, in particular, it can constitute an additive for cooked dishes, cold meats, sauces, etc., where it replaces the fat of the formulation, so as to obtain low calorie foods. In the examples which follow, the preparation of the starchy material according to the invention is illustrated, as it has just been defined above.
Tous les essais ont été réalisés sur des échantillons d'une masse totale de 150g. L'amidon, préalablement mélangé à l'eau, est soumis à l'action des micro-ondes jusqu'au degré de gélatinisation indiqué, avec une température finale de 96 °C Le générateur de micro-ondes utilisé était un générateur GHF 1211 Thomson-CSF, de puissance réglable de façon continue de 20 à 1500 W, à une fréquence de fonctionnement de 2,45 GHz.All tests were carried out on samples with a total mass of 150g. The starch, previously mixed with water, is subjected to the action of microwaves up to the degree of gelatinization indicated, with a final temperature of 96 ° C. The microwave generator used was a GHF 1211 Thomson generator -CSF, power continuously adjustable from 20 to 1500 W, at an operating frequency of 2.45 GHz.
Les résultats obtenus sont rapportés dans le Tableau suivant:
Figure imgf000011_0001
The results obtained are reported in the following table:
Figure imgf000011_0001
Figure imgf000012_0001
Figure imgf000012_0001
Les exemples suivants illustrent l'utilisation de la matière selon l'invention comme additif dans des produits de charcuterie. EXEMPLE 1 :The following examples illustrate the use of the material according to the invention as an additive in charcuterie products. EXAMPLE 1:
On prépare du pâté de campagne selon les deux formulations ci-après:Country pâté is prepared according to the two formulations below:
Composants (%) Témo in Produit avec substitution des matières grasses par la matière amylacée de l' inventionComponents (%) Sample in Product with substitution of fatty substances by the starchy material of the invention
Farce fineFine stuffing
Foie de porc 4 4 Couenne cuite froide 5 5Pork liver 4 4 Cold cooked rind 5 5
Caséniate 1,25 1,25Casenate 1.25 1.25
Gorges de porc 11 4,5Pork throat 11 4.5
Oignons 6 6Onions 6 6
Eau 8,75 11 ,75Water 8.75 11.75
Matière amylacée de l'invention 0 1,5Starchy material of the invention 0 1.5
Grain grossierCoarse grain
Fo ie de porc 16 16 Bardière découennée 22 11Pork liver 16 16 Rindless shingles 22 11
Gorges 26 14Gorges 26 14
Eau 0 17Water 0 17
Matière amylacée de l' invention 0 8Starchy material of the invention 0 8
+ épices+ spices
La préparation est effectuée par simple mélange des ingrédients, le mélange étant ensuite soumis de façon classique à la cuisson. Dans le cas du produit renfermant la matière amylacée de l'invention, cette dernière est incorporée le plus tard possible dans le mélange. La comparaison des deux produits montre que les qualités or gano 1 ep t iques sont conservées et que la valeur calorique du produit renfermant la matière amylacée de l'invention est d iminué e de 20 à 40%.The preparation is carried out by simple mixing of the ingredients, the mixture then being conventionally subjected to cooking. In the case of the product containing the starchy material of the invention, the latter is incorporated as late as possible in the mixture. The comparison of the two products shows that the or gano 1 ep tic qualities are preserved and that the caloric value of the product containing the starchy material of the invention is reduced from 20 to 40%.
Des résultats identiques ont été obtenus avec des mousses de foie. EXEMPLE 2:Identical results have been obtained with liver foams. EXAMPLE 2:
On prépare des saucisses de Strasbourg selon les deux formulations ci-après:Strasbourg sausages are prepared according to the two formulations below:
Composants (%) Témoin Produit avec substitution des matières grasses par la matière amylacée de l'inventionComponents (%) Control Product with substitution of fat by starchy material of the invention
Ma igre de porc 36 35My pork igre 36 35
Caséinate 1 1Caseinate 1 1
Gras bardière 19 4Fat bardière 19 4
Gorges de porc 15 9Pork throat 15 9
Eau 27 42Water 27 42
Matière amylacée de l'invention 0 7 qsp 100 avec épices, lactose, acide ascorbique, polyphosphatesStarchy material of the invention 0 7 qs 100 with spices, lactose, ascorbic acid, polyphosphates
La préparation est effectuée comme indiquée à l'Exemple 1 et les résultats concernant les qualités organoleptiques et la valeur calorique sont analogues à ceux de l'Exemple 1. The preparation is carried out as indicated in Example 1 and the results concerning the organoleptic qualities and the caloric value are similar to those of Example 1.

Claims

REVENDICATIONS 1. Matière amylacée, caractérisée par le fait qu'elle se présente sous la forme de particules macroscopiques de dimension comprise entre environ 0,5 et 5 mm, dont la solubilité (S) dans 1 'eau est comprise entre 15 et 65% environ, et le taux de gonflement (G) dans l'eau est compris entre 15 et 45% environ, (S) et (G) étant calculés selon les formules ci-après, sur des échantillons de 0,5g de matière sèche, agités dans 50 ml d'eau pendant 1/2 heure au bain-marie à 65ºC, le milieu subissant ensuite une centrifugation: CLAIMS 1. Starchy material, characterized in that it is in the form of macroscopic particles with a size of between approximately 0.5 and 5 mm, the solubility (S) of which in water is between 15 and 65% approximately, and the swelling rate (G) in water is between approximately 15 and 45%, (S) and (G) being calculated according to the formulas below, on samples of 0.5 g of dry matter, stirred in 50 ml of water for 1/2 hour in a water bath at 65ºC, the medium then undergoing centrifugation:
Figure imgf000015_0001
Figure imgf000015_0001
Figure imgf000015_0002
Figure imgf000015_0002
2. Matière amylacée selon la revendication 1, caractérisée par le fait que sa consistance au viscoamylographe Brabender est comprise entre environ 30 et 900 cmg, au début du cycle thermique, et entre environ 900 et 1500 cmg, à la fin du cycle thermique, les échantillons étant étudiés à une concentration de 6-7% en poids dans l'eau, et le cycle thermique étant défini comme suit:2. Starchy material according to claim 1, characterized in that its consistency with the Brabender viscoamylograph is between approximately 30 and 900 cmg, at the start of the thermal cycle, and between approximately 900 and 1500 cmg, at the end of the thermal cycle, the samples being studied at a concentration of 6-7% by weight in water, and the thermal cycle being defined as follows:
- chauffage à progression constante, à raison de + 1,5°C/minute jusqu'à 96°C;- heating with constant progression, at a rate of + 1.5 ° C / minute up to 96 ° C;
- maintien de cette température pendant 15 minutes; et - refroidissement à progression constante, à raison de - 1,5°C/minute jusqu'à 30°C.- maintaining this temperature for 15 minutes; and - constant progression cooling, at a rate of - 1.5 ° C / minute to 30 ° C.
3. Matière amylacée selon l'une des revendications 1 et 2, caractérisée par le fait que la consistance au farinographe Brabender d'une suspension de 75 g de ladite matière dans 100 ml d'eau, qui a été soumise à un pétrissage intensif, est comprise entre environ 300 et 1000 au bout de 15 minutes. 3. Starchy material according to one of claims 1 and 2, characterized in that the consistency of the Brabender farinograph of a suspension of 75 g of said material in 100 ml of water, which has been subjected to intensive kneading, is between approximately 300 and 1000 after 15 minutes.
4. Matière amylacée selon l'une des revendications 1 à 3, caractérisée par le fait que le degré de gélatinisation, mesuré par le test de gonflement en milieu potasse 0,01 N, est compris entre environ 50 et 100. 4. Starchy material according to one of claims 1 to 3, characterized in that the degree of gelatinization, measured by the swelling test in 0.01 N potassium hydroxide medium, is between approximately 50 and 100.
5. Matière amylacée selon l'une des revendications 1 à 4, caractérisée par le fait qu'elle est issue de l'amidon de manioc ou de l'amidon de pomme de terre.5. Starchy material according to one of claims 1 to 4, characterized in that it comes from cassava starch or potato starch.
6. Matière amylacée selon l'une des revendications 1 à 5, caractérisée par le fait que son humidité est inférieure à 10% en poids par rapport à la matière totale.6. Starchy material according to one of claims 1 to 5, characterized in that its humidity is less than 10% by weight relative to the total material.
7. Matière amylacée selon l'une des revendications 1 à 5, caractérisée par le fait qu'elle renferme en outre au moins un agent complexant de l'amylose, à raison d'au plus 3% en poids par rapport à ladite matière amylacée.7. Starchy material according to one of claims 1 to 5, characterized in that it also contains at least one amylose complexing agent, at a rate of at most 3% by weight relative to said starchy material .
8. Procédé de fabrication d'une matière amylacée telle que définie à l'une des revendications 1 à 7, caractérisé par le fait que:8. A method of manufacturing a starchy material as defined in one of claims 1 to 7, characterized in that:
(1) on soumet à un traitement par ondes ayant une fréquence comprise entre 0,9 et 300 GHz, un milieu contenant de l'amidon, de l'eau à raison de 30 à 50% en poids par rapport à la masse de l'amidon, et, éventuellement, au moins un agent complexant de l 'amylose à raison d'au plus 3% en poids par rapport à la masse de l 'amidon;(1) is subjected to a wave treatment having a frequency between 0.9 and 300 GHz, a medium containing starch, water at a rate of 30 to 50% by weight relative to the mass of l starch, and possibly at least an amylose complexing agent in an amount of at most 3% by weight relative to the mass of the starch;
(2) on fragment la pâte ainsi obtenue en éléments de taille comprise entre environ 0,5 et 5 mm; et(2) the dough thus obtained is fragmented into elements of size between approximately 0.5 and 5 mm; and
(3) on sèche pour ramener l'humidité du produit à une valeur désirée.(3) drying to bring the humidity of the product to a desired value.
9. Procédé selon la revendication 8, caractérisé par le fait qu'on utilise à l'étape (1) la fréquence de 2,45 GHz.9. Method according to claim 8, characterized in that one uses in step (1) the frequency of 2.45 GHz.
10. Procédé selon l'une des revendications 8 et 9, caractérisé par le fait qu'on conduit le traitement de l'étape (1 ) jusqu'à gélatinisation d'au minimum 50% de l'amidon.10. Method according to one of claims 8 and 9, characterized in that the treatment of step (1) is carried out until gelatinization of at least 50% of the starch.
11. Procédé selon l'une des revendications 8 à 10, caractérisé par le fait qu'on conduit le traitement de l'étape (1) pendant une durée d'environ 0,5 à 15 minutes. 11. Method according to one of claims 8 to 10, characterized in that the treatment of step (1) is carried out for a period of approximately 0.5 to 15 minutes.
12. Procédé selon l'une des revendications 8 à 11, caractérisé par le fait qu'on conduit le traitement de l'étape (1) à une température de l'ordre de 50 à 98°C.12. Method according to one of claims 8 to 11, characterized in that the treatment of step (1) is carried out at a temperature of the order of 50 to 98 ° C.
13. Procédé selon l'une des revendications 8 à 12, caractérisé par le fait qu'on conduit le séchage de l'étape (3) à une température de l'ordre de 80 à 130°C.13. Method according to one of claims 8 to 12, characterized in that the drying of step (3) is carried out at a temperature of the order of 80 to 130 ° C.
14. Utilisation de la matière amylacée telle que définie à l'une des revendications 1 à 7, comme additifs pour produits alimentaires, en particulier pour plats cuisinés, charcuterie, sauces et similaires. 14. Use of the starchy material as defined in one of claims 1 to 7, as additives for food products, in particular for ready meals, cold meats, sauces and the like.
PCT/FR1989/000153 1988-04-06 1989-04-04 Amylaceous material and process for producing it WO1989009793A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR88/04528 1988-04-06
FR8804528A FR2629684B1 (en) 1988-04-06 1988-04-06 AMYLACEOUS MATERIAL AND MANUFACTURING METHOD THEREOF

Publications (1)

Publication Number Publication Date
WO1989009793A1 true WO1989009793A1 (en) 1989-10-19

Family

ID=9365001

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FR1989/000153 WO1989009793A1 (en) 1988-04-06 1989-04-04 Amylaceous material and process for producing it

Country Status (4)

Country Link
EP (1) EP0374208A1 (en)
AU (1) AU3419289A (en)
FR (1) FR2629684B1 (en)
WO (1) WO1989009793A1 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991007106A1 (en) * 1989-11-22 1991-05-30 Opta Food Ingredients, Inc. A starch-derived, food-grade, insoluble bulking agent
FR2661317A1 (en) * 1990-04-27 1991-10-31 Tipiak Sa Process for obtaining a starchy (amylaceous) product, product obtained and its applications
US5194284A (en) * 1988-10-14 1993-03-16 National Starch And Chemical Investment Holding Corporation Foods opacified with debranched starch
US5291877A (en) * 1991-06-21 1994-03-08 Nestec S.A. Low starch concentration gel and preparation thereof
US5496861A (en) * 1990-11-19 1996-03-05 National Starch And Chemical Investment Holding Corporation Cosmetics containing enzymatically debranched starch
WO1996006866A1 (en) * 1994-08-31 1996-03-07 Rijksuniversiteit Te Groningen Method of modifying starch
US5711986A (en) * 1988-10-14 1998-01-27 National Starch And Chemical Investment Holding Corporation Method of replacing fats with short chain amylose
US5962047A (en) * 1996-06-14 1999-10-05 Opta Food Ingredients, Inc. Microcrystalline starch-based product and use in foods

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2242564A1 (en) * 1996-01-16 1997-07-24 Opta Food Ingredients, Inc. Starch-emulsifier composition and methods of making
US6017388A (en) * 1996-01-16 2000-01-25 Opta Food Ingredients, Inc. Starch-emulsifier composition and methods of making
US6228419B1 (en) 1998-10-20 2001-05-08 Opta Food Ingredients, Inc. High-amylose starch-emulsifier composition and methods of making

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3904429A (en) * 1974-01-28 1975-09-09 Nat Starch Chem Corp Process for preparing dried, precooked starch products with microwaves
EP0059050A2 (en) * 1981-02-23 1982-09-01 Cpc International Inc. Method of modifying starch by UHF radiation
US4508576A (en) * 1983-10-18 1985-04-02 Cpc International Inc. Hot-water dispersible corn starch having high paste viscosity

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3904429A (en) * 1974-01-28 1975-09-09 Nat Starch Chem Corp Process for preparing dried, precooked starch products with microwaves
EP0059050A2 (en) * 1981-02-23 1982-09-01 Cpc International Inc. Method of modifying starch by UHF radiation
US4508576A (en) * 1983-10-18 1985-04-02 Cpc International Inc. Hot-water dispersible corn starch having high paste viscosity

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Food Science and Technology Abstracts, 85-05-10043, mai 1985, (New York, US), O.J. Choi et al.: "A study on the effect of microwave heating on starch food. I. The physicochemical effects of microwave heating on potato starch and purified potato starch", voir abrege no. 85028184, & Journal of the Korean Society of Food and Nutrition, vol. 13, no. 3, p. 268-274, 25 Ref. 1984 *

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5194284A (en) * 1988-10-14 1993-03-16 National Starch And Chemical Investment Holding Corporation Foods opacified with debranched starch
US5711986A (en) * 1988-10-14 1998-01-27 National Starch And Chemical Investment Holding Corporation Method of replacing fats with short chain amylose
WO1991007106A1 (en) * 1989-11-22 1991-05-30 Opta Food Ingredients, Inc. A starch-derived, food-grade, insoluble bulking agent
FR2661317A1 (en) * 1990-04-27 1991-10-31 Tipiak Sa Process for obtaining a starchy (amylaceous) product, product obtained and its applications
US5496861A (en) * 1990-11-19 1996-03-05 National Starch And Chemical Investment Holding Corporation Cosmetics containing enzymatically debranched starch
US5291877A (en) * 1991-06-21 1994-03-08 Nestec S.A. Low starch concentration gel and preparation thereof
WO1996006866A1 (en) * 1994-08-31 1996-03-07 Rijksuniversiteit Te Groningen Method of modifying starch
NL9401412A (en) * 1994-08-31 1996-04-01 Rijksuniversiteit Method for modifying starch.
US5962047A (en) * 1996-06-14 1999-10-05 Opta Food Ingredients, Inc. Microcrystalline starch-based product and use in foods

Also Published As

Publication number Publication date
FR2629684B1 (en) 1991-06-07
AU3419289A (en) 1989-11-03
FR2629684A1 (en) 1989-10-13
EP0374208A1 (en) 1990-06-27

Similar Documents

Publication Publication Date Title
US5882713A (en) Non-separable compositions of starch and water-immiscible organic materials
EP0150715B1 (en) Process for the preparation of a starch dispersible in boiling water
JP2008524372A (en) Xanthan gum-containing composition dispersible in water
WO1989009793A1 (en) Amylaceous material and process for producing it
JPWO2008047846A1 (en) Cooked rice quality improver and its application
US6613370B1 (en) Breadcrumb coating for food products
RU2242901C2 (en) Dry product to be reduced by aqueous liquids and method for producing the same
EP1283241A1 (en) Starch/carboxylated polymer composites
WO2013054461A1 (en) Granular substance, food or beverage obtained using same, and process for producing granular substance
JP5127826B2 (en) Starch-containing composition and method for producing the same
JP4410238B2 (en) Dry extract with improved hygroscopic deliquescence during storage
JP5770545B2 (en) Fishery paste product and method for producing fish paste product
WO1995002969A1 (en) A maltodextrin composition
FR2661317A1 (en) Process for obtaining a starchy (amylaceous) product, product obtained and its applications
JP3383012B2 (en) Modified starch derivatives and processed flour products containing the same
KR860001811B1 (en) Cellulose food filler
JPH0923835A (en) Powder for fry batter
JP3995573B2 (en) Spring roll skin and manufacturing method thereof
EP0896004B1 (en) Process for the manufacture of modified starch and its use
RU2785127C2 (en) Pregelatinized starches with high technological stability and methods for their production and use
JP4221894B2 (en) Corn powder with excellent dispersibility and method for producing the same
JPH0841105A (en) Method for granulating water-soluble polysaccharide
AU759028B2 (en) Consumable, viscoebastic, stringy composition, process for its production and dry product for use in the process
JP4184878B2 (en) Gellan gum coated starch and food using the same
CN112040789A (en) Food composition

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AU JP

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE FR GB IT LU NL SE

WWE Wipo information: entry into national phase

Ref document number: 1989904573

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1989904573

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 1989904573

Country of ref document: EP