EP0352393A1 - Food-sweetening compound based on sucrose and a strong sweetener, and process to prepare it - Google Patents

Food-sweetening compound based on sucrose and a strong sweetener, and process to prepare it Download PDF

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Publication number
EP0352393A1
EP0352393A1 EP88403366A EP88403366A EP0352393A1 EP 0352393 A1 EP0352393 A1 EP 0352393A1 EP 88403366 A EP88403366 A EP 88403366A EP 88403366 A EP88403366 A EP 88403366A EP 0352393 A1 EP0352393 A1 EP 0352393A1
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EP
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Prior art keywords
sucrose
sweetener
particles
granulation
average diameter
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EP88403366A
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German (de)
French (fr)
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EP0352393B1 (en
Inventor
Gérard Genermont
Guy Lepiètre
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Eridania Beghin Say SA
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Beghin Say SA
Eridania Beghin Say SA
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Priority to AT88403366T priority Critical patent/ATE90114T1/en
Publication of EP0352393A1 publication Critical patent/EP0352393A1/en
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Publication of EP0352393B1 publication Critical patent/EP0352393B1/en
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    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B50/00Sugar products, e.g. powdered, lump or liquid sugar; Working-up of sugar
    • C13B50/002Addition of chemicals or other foodstuffs

Definitions

  • the present invention relates to a novel food sweetener based on sucrose and an intense sweetener as well as methods for preparing it. More specifically, the present invention relates to a new granular sweetener product containing sucrose and at least one intense sweetener, the amount of which can reach 50% by weight of said sweetener product.
  • Intense sweeteners such as saccharin, saccharinates, acesulfame, and especially sweeteners of the dipeptide type, i.e. esters of aspartyl-phenylalanine, the most used of which is methyl ester, ⁇ -L-aspartyl-L- phenylalanine methyl ester, known as aspartame (AP), are widely used in the food industry due to their high sweetening power - at least about 150 times that of sucrose. Certain properties of intense sweeteners can however make their use difficult and in particular cause problems during their incorporation in food products.
  • part of the intense sweetener is added at the granulation step a1), the complement being added at the step b).
  • the addition of water mentioned in step a1) of the methods of the invention may consist of an injection of water vapor or a spraying of water or a granulation solution.
  • saccharin As an intense sweetener which can be used in the present invention, there may be mentioned, by way of example, saccharin, saccharinates, acesulfame, and sweeteners of the dipeptide type, that is to say the esters of aspartylphenylalanine the most used of which is ⁇ -L-aspartyl-L-phenylalanine methyl ester known as aspartame (AP).
  • AP aspartame
  • the new food product of the present invention based on sucrose and intense sweetener may also comprise a complementary support composed of one or more constituents such as gelling agents, texturizers, stabilizers, examples of such constituents are pectins, animal and vegetable proteins, in particular dairy proteins, fibers, carboxymethyl cellulose, cyclodextrins, etc.
  • the sweetening product of the present invention containing a complementary support can be prepared in various ways.
  • Said additional support can be added during step b) of mixing under moderate conditions, either with all of the intense sweetener, in the case of the first process above, or with part of the intense sweetener , in the case of the third method above, either alone in the case of the second method above (in the latter case, step b) is added to the method).
  • part of the latter can be added at step a1), the rest being added at step b).
  • the addition of water mentioned in step a1) of the methods of the invention can consist of an injection of water vapor or a spraying of water or of a granulation solution.
  • Said granulation solution can for example be a sucrose syrup or an aqueous solution of a complementary support, for example example a gelling solution of pectin.
  • a complementary support for example example a gelling solution of pectin.
  • Icing sugar that is to say, crystallized sucrose having an average diameter between 80 and 100 ⁇ m, is fed by means of a volumetric or gravimetric dosing device, for example a screw doser, at the top of the 'a granulation chamber.
  • This granulation chamber communicates with a fluidized bed in which air is blown, the temperature of which decreases from upstream to downstream, from a temperature> 100 ° C (hot air) to a temperature from 15 - 20 ° C (cold air).
  • Water vapor is injected into the granulation chamber, substantially at the level of the incorporation of icing sugar, which creates, together with the hot air blown upstream of the fluidized bed, a turbulence which causes the particles to agglomerate. icing sugar between them and their subsequent granulation.
  • the agglomerated and granulated particles fall by gravity to the lower part of the granulation chamber and are taken up by the air stream from the fluidized bed; they advance on the fluidized bed and are cooled by the cold air stream to 15 - 20 ° C before being evacuated from the fluidized bed to be sent to sieving, to provide sucrose particles having an appropriate granulation (average diameter included between 150 and 500 ⁇ m).
  • sucrose particles are then mixed with the intense sweetener in powder form in a "soft" mixer, for example a ribbon or coulter mixer, having a low speed of rotation.
  • the required amount of intense sweetener can be incorporated one or more times.
  • a 200-liter ribbon mixer can be used, the rotation speed of which is 30-40 revolutions / min.
  • the time for mixing the sieved sucrose particles after leaving the fluidized bed with the intense sweetener will be determined to be sufficient to obtain complete incorporation of the intense sweetener into the sucrose particles and a total homogeneity of the product.
  • the product of the invention obtained for example according to a process as described above, is not a simple mixture of sucrose and intense sweetener.
  • ultrasound sedimentation tests were carried out on a product according to the invention containing 40% by weight of AP and 60% by weight of sucrose. Dosages at different heights did not reveal any significant deviation of the components.
  • the new sweetener product of the invention does not contain fines and is therefore easy to handle. It is stable in storage, and does not form agglomerates. It is easy to dose precisely because of both its granular shape and its low apparent density. It dissolves very well in water and its wettability is excellent.
  • a product according to the invention containing 1.5 g of sucrose and 1 g of AP dissolve in a liter of water at 20 ° C 4 times faster than 1 g of 'AP alone.
  • the product according to the invention provides only a reduced number of calories, even negligible.
  • a product according to the invention containing 60% by weight of sucrose and 40% by weight of AP will have a sweetening power equal to approximately 80 times that of sucrose; in other words, with a sweetening power equal to that of sucrose, this product will only provide a number of calories corresponding to less than 1% of that which would have been provided by sucrose, which is negligible.
  • the new sweetener product of the invention can be added to various food products, such as for example drinks, ice creams, dairy products such as yogurts and fromage blanc, confectionery, as well as to food products in the form of powder, etc ...
  • the present invention makes it possible to produce a formulation adapted to each specific specific case, by choosing in particular the intense sweetener (s) present (s) and by adjusting their dosage.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Biochemistry (AREA)
  • Organic Chemistry (AREA)
  • Seasonings (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Seeds, Soups, And Other Foods (AREA)
  • Dairy Products (AREA)
  • Saccharide Compounds (AREA)
  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

Abstract

New granular sweetening food product comprising saccharose and at least one intense sweetener, characterized in that it contains from 50 to 99 % by weight of saccharose and from 1 to 50 % of at least one intense or strong sweetener, in that its apparent density is between 0.4 and 0.7 g/cm<3>, preferably between 0.45 and 0.55 g/cm<3>, and in that the mean diameter of the grains is between 150 and 500 mu m, preferably equal to about 200 mu m. The new product of the invention is stable in storage conditions. It is easy to handle. It is also easy to dose accurately and has a sweetening power equal to that of saccharose and brings in a reduced, practically negligible number of calories. The sweetening product may be added to various food products such as beverages, ice creams, dairy products such as yaourts and white cheese, confectionery, as well as food products in the form of powders.

Description

La présente invention concerne un nouveau produit édulcorant alimentaire à base de saccharose et d'édulcorant intense ainsi que des procédés pour le préparer. Plus spécifiquement, la présente invention concerne un nouveau produit édulcorant granulaire contenant du saccharose et au moins un édulcorant intense dont la quantité peut atteindre 50 % en poids dudit produit édulcorant.The present invention relates to a novel food sweetener based on sucrose and an intense sweetener as well as methods for preparing it. More specifically, the present invention relates to a new granular sweetener product containing sucrose and at least one intense sweetener, the amount of which can reach 50% by weight of said sweetener product.

Les édulcorants intenses, tel la saccharine, les saccharinates, l'acésulfame, et surtout les édulcorants du type dipeptide, c'est à dire les esters de l'aspartyl-phénylalanine dont le plus utilisé est l'ester de méthyle, l'α-L-aspartyl-L- phénylalanine méthyl ester, connu sous l'appellation d'aspartame (AP), sont largement utilisés dans l'industrie alimentaire du fait de leur pouvoir sucrant élevé - au moins égal à en­viron 150 fois celui du saccharose.
Certaines propriétés des édulcorants intenses peuvent toutefois rendre leur utilisation difficile et en particulier engendrer des problèmes lors de leur incorporation dans des produits alimentaires. Parmi celles-ci, on peut citer :
- leur solubilité médiocre et leur faible mouillabilité ;
- le fait qu'ils deviennent collants à l'humidité et tendent à former des agglomérats ;
- leur pouvoir sucrant extrêmement élevé qui rend leur dosage délicat (alors que celui-ci doit être très précis) ;
- la présence de fines qui rend leur manipulation malaisée ;
- leur instabilité au stockage.
Intense sweeteners, such as saccharin, saccharinates, acesulfame, and especially sweeteners of the dipeptide type, i.e. esters of aspartyl-phenylalanine, the most used of which is methyl ester, α -L-aspartyl-L- phenylalanine methyl ester, known as aspartame (AP), are widely used in the food industry due to their high sweetening power - at least about 150 times that of sucrose.
Certain properties of intense sweeteners can however make their use difficult and in particular cause problems during their incorporation in food products. Among these, we can cite:
- their poor solubility and low wettability;
- the fact that they become sticky to humidity and tend to form agglomerates;
- their extremely high sweetening power which makes their dosage delicate (although this must be very precise);
- the presence of fines which makes their handling difficult;
- their instability during storage.

Diverses solutions ont été proposées pour palier les inconvénients liés à l'utilisation des édulcorants intenses dans l'industrie alimentaire. Les travaux récents ont été surtout dirigés sur l'aspartame qui est un édulcorant intense dont l'utilisation est très répandue.Various solutions have been proposed to overcome the drawbacks associated with the use of intense sweeteners in the food industry. Recent work has been mainly directed to aspartame which is an intense sweetener whose use is very widespread.

L'EP-A-0102032 décrit un produit édulcorant liquide comprenant de l'aspartame et un agent dispersant aqueux, comprenant de préférence un sucre. Un tel produit liquide n'est ni facile à stocker ni facile à do­ser de façon précise.
L'EP-A-0106910 décrit un produit édulcorant solide sous forme de pro­duits moulés, par exemple sous forme de cubes, contenant un édulcorant à base de dipeptide, l'aspartame étant préféré, et au moins un excipient pouvant être du saccharose. La quantité d'édulcorant à base de dipeptide est de 0,3 à 30 % en poids par rapport à l'excipient. Cependant, quand l'excipient comprend principalement du saccharose, la quantité d'édul­corant intense à base de dipeptide doit être de 2,0 - 10 % en poids par rapport à l'excipient ; dans le cas où la proportion d'excipient est plus faible, la solubilité et la mouillabilité de l'édulcorant à base de dipeptide ne sont que médiocrement améliorées. En outre, le produit ob­tenu est alors trop fin et sa manipulation devient de ce fait très mal­aisée (page 3, l. 21 à page 4, l. 1 et page 5, l. 19 à page 6, l. 9). Autrement dit, dans le cas d'une composition contenant un édulcorant à base de dipeptide, par example de l'aspartame, et du saccharose, la quantité d'aspartame ne doit pas dépasser 9 % en poids de la composition totale. De plus, le produit de l'EP-A-0106910 est sous une forme moulée, par exemple en cubes, ce qui empêche de l'incorporer tel quel de façon homogène dans les produits alimentaires comme par exemple des glaces, des yaourts ou des produits sous forme de poudre.
Un objet de la présente invention est de fournir un produit édulcorant ayant un pouvoir sucrant largement supérieur à celui du saccharoise et pouvant être incorporé de façon précise et homogène dans divers produits alimentaires, que ces produits soient liquides, semi-liquides, sous forme de pâte ou de poudre.
Un autre objet de l'invention est de fournir un tel produit qui soit stable au stockage et qui soit de manipulation aisée.
Un object de l'invention est encore de fournir un tel produit ayant une solubilité et mouillabilité satisfaisantes.
Un objet de l'invention est aussi de fournir un produit édulcorant à base de saccharose et d'édulcorant intense pouvant contenir jusqu'à 50 % en poids d'édulcorant intense.
Un objet de l'invention est en outre de fournir un produit édulcorant à base de saccharose et d'édulcorant intense pouvant comprendre plusieurs édulcorants intenses.
D'autres objets et avantages de l'invention apparaîtront à la lecture de la description ci-après.
La présente invention répond aux objets ci-dessus et fournit un produit édulcorant granulaire comprenant du saccharose et au moins un édulcorant intense caractérisé en ce qu'il contient de 50 à 99 % en poids de saccharose et de 1 à 50 % d'au moins un édulcorant intense, en ce que sa densité apparente est comprise entre 0,4 et 0,7 g/cm³, de préférence entre 0,45 et 0,55 g/cm³, et en ce que le diamètre moyen des grains est compris entre 150 et 500 µm, de préférence égal à environ 200 µm.
Pour des raisons de simplification de la terminologie, l'expression "édulcorant intense" devra être comprise dans la présente description ainsi que dans les revendications comme pouvant définir un ou plusieurs édulcorants intenses.
La présente invention fournit également plusieurs procédés de préparation de ce nouveau produit édulcorant.
Le premier selon l'invention comprend les étapes suivantes:

  • a) préparation de particules de saccharose de diamètre moyen compris entre 150 et 500 µm comprenant les étapes de
    • a1) granulation du saccharose en phase humide dans un appareil de granulation en continu dans lequel est alimenté, à sa partie supérieure, le saccharose cristallisé ayant un diamètre moyen compris entre 80 et 100 µm et on procède à une addition d'eau, sensiblement au niveau de l'alimentation dudit saccharose cristallisé, de l'air chaud étant soufflé de façon ascendante dans ledit appareil de granulation ;
    • a2) séchage et refroidissement, sur un lit fluidisé relié à la partie inférieure dudit appareil de granulation, des particules de saccharose formées dans l'étape a1) ;
    • a3) tamisage des particules provenant de l'étape a2) de façon à obtenir des particules de saccharose ayant un diamètre moyen compris entre 150 et 500 µm ;
  • b) mélange des particules de saccharose provenant de l'étape a3) avec l'édulcorant intense sous forme de poudre, dans des conditions modérées pendant un temps suffisant pour obtenir le produit souhaité.
EP-A-0102032 describes a liquid sweetening product comprising aspartame and an aqueous dispersing agent, preferably comprising a sugar. Such a liquid product is neither easy to store nor easy to dose precisely.
EP-A-0106910 describes a solid sweetener in the form of molded products, for example in the form of cubes, containing a dipeptide-based sweetener, aspartame being preferred, and at least one excipient which may be sucrose. The amount of dipeptide-based sweetener is 0.3 to 30% by weight relative to the excipient. However, when the excipient mainly comprises sucrose, the amount of intense dipeptide-based sweetener should be 2.0 - 10% by weight relative to the excipient; in the case where the proportion of excipient is lower, the solubility and wettability of the dipeptide sweetener are only poorly improved. In addition, the product obtained is then too thin and its handling therefore becomes very difficult (page 3, l. 21 to page 4, l. 1 and page 5, l. 19 to page 6, l. 9). In other words, in the case of a composition containing a dipeptide-based sweetener, for example aspartame, and sucrose, the amount of aspartame should not exceed 9% by weight of the total composition. In addition, the product of EP-A-0106910 is in a molded form, for example in cubes, which prevents it from being incorporated homogeneously as it is into food products such as ice creams, yogurts or products in powder form.
An object of the present invention is to provide a sweetening product having a sweetening power far superior to that of Saccharoise and which can be incorporated in a precise and homogeneous manner into various food products, whether these products are liquid, semi-liquid, in the form of a paste. or powder.
Another object of the invention is to provide such a product which is stable in storage and which is easy to handle.
It is also an object of the invention to provide such a product having satisfactory solubility and wettability.
An object of the invention is also to provide a sweetener product based on sucrose and an intense sweetener which may contain up to 50% by weight of intense sweetener.
It is further an object of the invention to provide a sweetener based on sucrose and an intense sweetener which may include several intense sweeteners.
Other objects and advantages of the invention will appear on reading the description below.
The present invention meets the above objects and provides a granular sweetener product comprising sucrose and at least one intense sweetener characterized in that it contains from 50 to 99% by weight of sucrose and from 1 to 50% at least. an intense sweetener, in that its apparent density is between 0.4 and 0.7 g / cm³, preferably between 0.45 and 0.55 g / cm³, and in that the average grain diameter is between 150 and 500 µm, preferably about 200 µm.
For reasons of simplification of the terminology, the expression "intense sweetener" should be understood in the present description as in the claims as being able to define one or more intense sweeteners.
The present invention also provides several methods of preparing this new sweetener.
The first according to the invention comprises the following steps:
  • a) preparation of sucrose particles with an average diameter of between 150 and 500 μm comprising the steps of
    • a1) granulation of the sucrose in the wet phase in a continuous granulation apparatus into which is fed, at its upper part, the crystallized sucrose having an average diameter of between 80 and 100 μm and an addition of water is carried out, substantially at feeding level of said crystallized sucrose, hot air being blown upwardly into said granulator;
    • a2) drying and cooling, on a fluidized bed connected to the lower part of said granulation apparatus, of the sucrose particles formed in step a1);
    • a3) sieving the particles from step a2) so as to obtain sucrose particles having an average diameter between 150 and 500 μm;
  • b) mixing the sucrose particles from step a3) with the intense sweetener in powder form, under moderate conditions for a time sufficient to obtain the desired product.

Le deuxième procédé selon l'invention comprend les étapes suivantes :

  • a1) granulation en phase humide dans un appareil de granulation en continu dans lequel on alimente à sa partie supérieure le saccharose cristallisé ayant un diamètre moyen compris entre 80 et 100 µm avec l'édulcorant intense cristallisé ayant un diamètre moyen inférieur à environ 500 µm, éventuellement prémélangé audit saccharose cristallisé, et on procède à une addition d'eau sensiblement au niveau de l'alimentation des produits de départ cristallisés, de l'air chaud étant soufflé de façon ascendante dans ledit appareil de granulation ;
  • a2) séchage et refroidissement, sur un lit fluidisé relié à la partie inférieure dudit appareil de granulation, des particules d'édulcorant granulaire formées dans l'étape a1) ;
  • a3) tamisage des particules provenant de l'étape a2) de façon à obtenir des particules de l'édulcorant granulaire souhaité ayant un diamètre moyen compris entre 150 et 500 µm.
The second method according to the invention comprises the following steps:
  • a1) wet granulation in a continuous granulation apparatus in which the crystalline sucrose having an average diameter of between 80 and 100 μm is fed at its upper part with the intense crystallized sweetener having an average diameter of less than approximately 500 μm, optionally premixed with said crystallized sucrose, and a water addition is carried out substantially at the level of the supply of the crystallized starting products, hot air being blown upwardly into said granulation apparatus;
  • a2) drying and cooling, on a fluidized bed connected to the lower part of said granulation apparatus, of the granular sweetener particles formed in step a1);
  • a3) sieving the particles from step a2) so as to obtain particles of the desired granular sweetener having an average diameter between 150 and 500 μm.

Selon une variante du premier procédé ci-dessus, constituant le troisième procédé selon l'invention, une partie de l'édulcorant intense est ajoutée au niveau de l'étape de granulation a1), le complément étant ajouté au niveau de l'étape b).
L'addition d'eau mentionnée dans l'étape a1) des procédés de l'invention peut consister en une injection de vapeur d'eau ou en une pulvérisation d'eau ou d'une solution de granulation.
Comme édulcorant intense utilisable dans la présente invention on peut citer, à titre d'exemple, la saccharine, les saccharinates, l'acésulfame, et les édulcorants de type dipeptide, c'est-à-dire les esters de l'aspartyl-phénylalanine dont le plus utilisé est l'α-L-aspartyl-L-phénylalanine méthyl ester connu sous le nom d'as­partame (AP). Cette liste n'est pas limitative.
Le nouveau produit alimentaire de la présente invention à base de saccharose et d'édulcorant intense peut en outre comprendre un support complémentaire composé d'un ou plusieurs constituants tels les gélifiants, les texturants, les stabilisants, des exemples de tels constituants sont les pectines, les protéines animales et végétales, en particulier les protéines laitières, les fibres, la carboxyméthyl-cellulose, les cyclodextrines, etc...
Le produit édulcorant de la présente invention contenant un support complémentaire peut-être préparé de diverses façons. Ledit support complémentaire peut être ajouté au cours de l'étape b) de mélange dans des conditions modérées, soit avec la totalité de l'édulcorant intense, dans le cas du premier procédé ci-dessus, soit avec une partie de l'édulcorant intense, dans le cas du troisième procédé ci-dessus, soit seul dans le cas du deuxième procédé ci-dessus (dans ce dernier cas, l'étape b) est ajoutée au procédé).
Selon une variante des procédés de préparation du produit édulcorant de la présente invention contenant un support complémentaire, une partie de ce dernier peut être ajoutée au niveau de l'étape a1), le reste étant ajouté au niveau de l'étape b).
Comme indiqué plus haut, l'addition d'eau mentionnée dans l'étape a1) des procédés de l'invention peut consister en une injection de vapeur d'eau ou en une pulvérisation d'eau ou d'une solution de granulation. Ladite solution de granulation peut par exemple être un sirop de saccharose ou bien une solution aqueuse d'un support complémentaire, par exemple une solution gélifiante de pectine.
Ainsi, il est possible dans certains cas d'introduire tout ou partie de l'éventuel support complémentaire via la pulvérisation dans l'étape de granulation a1) du procédé d'une solution dudit support complémentaire. Pour mieux illustrer la présente invention un mode d'obtention d'un produit édulcorant alimentaire granulaire selon l'invention est décrit plus en détails ci-dessous, à titre d'exemple.
Du sucre glace, c'est à dire, du saccharose cristallisé ayant un diamé­tre moyen compris entre 80 et 100 µm, est alimenté au moyen d'un dispo­sitif de dosage volumétrique ou gravimétrique, par exemple un doseur à vis, à la partie supérieure d'une chambre de granulation. La partie in­férieure de cette chambre de granulation communique avec un lit fluidisé dans lequel on souffle de l'air dont la température décroît de l'amont vers l'aval, depuis une température > 100 °C (air chaud) jusqu'à une température de 15 - 20 ° C (air froid). On injecte dans la chambre de granulation, sensiblement au niveau de l'incorporation du sucre glace, de la vapeur d'eau qui crée, conjointement avec l'air chaud soufflé en amont du lit fluidisé, une turbulence qui provoque l'agglomération des particules de sucre glace entre elles et leur granulation subséquente. Les particules agglomérées et granulées tombent par gravité à la partie inférieure de la chambre de granulation et sont reprises par le courant d'air du lit fluidisé ; elles avancent sur le lit fluidisé et sont re­froidies par le courant d'air froid à 15 - 20 °C avant d'être évacuées du lit fluidisé pour être envoyées au tamisage, pour fournir des parti­cules de saccharose ayant une granulation appropriée (diamètre moyen compris entre 150 et 500 µm). Ces particules de saccharose sont ensuite mélangées avec l'édulcorant intense sous forme de poudre dans un mélangeur "doux", par exemple un mélangeur à ruban ou à socs, ayant une vitesse de rotation peu élevée. On peut incorporer la quantité requise d'édulcorant intense en une ou plusieurs fois.
A titre d'exemple, pour fabriquer 50 kg de produit selon l'invention contenant 30 kg de saccharose et 20 kg d'édulcorant intense, on peut utiliser un mélangeur à ruban de 200 litres dont la vitesse de rotation est 30-40 tours/mn. On peut incorporer aux 30 kg de particules saccharose tamisées, les 20 kg d'édulcorant intense en une seule fois, en effectuant le mélange pendant 15 à 20 mn, ou bien incorporer 3 fois 6,7 kg d'édulcorant intense, le temps de mélange entre chaque ajout étant de 5 mn et le mélange final étant fixé à 10 mn. D'une façon générale, le temps de mélange des particules de saccharose tamisées après leur sortie du lit fluidisé avec l'édulcorant intense sera déterminé de façon à être suffisant pour obtenir une incorporation complète de l'édulcorant intense dans les particules de saccharose et une homogénéité totale du produit.
Le produit de l'invention, obtenu par exemple selon un procédé tel que décrit ci-dessus, n'est pas un simple mélange de saccharose et d'édul­corant intense. On a effectué à cet égard des essais de sédimentation par ultra-sons sur un produit selon l'invention contenant 40 % en poids d'AP et 60 % en poids de saccharose. Des dosages à différentes hauteurs n'ont révélé aucun écart significatif des composants.
Le nouveau produit édulcorant de l'invention ne comprend pas de fines et est de ce fait de manipulation aisée. Il est stable au stockage, et ne forme pas d'agglomérats.
Il est facile à doser de façon précise du fait à la fois de sa forme granulaire et de sa faible densité apparente.
Il se dissout très bien dans l'eau et sa mouillabilité est excellente. A titre d'exemple, 2,5 g de produit selon l'invention contenant 1,5 g de saccharose et 1 g d'AP se dissolvent dans un litre d'eau à 20 °C 4 fois plus rapidement qu'1 g d'AP seul.
En outre, à pouvoir sucrant égal à celui du saccharose, le produit selon l'invention n'apporte qu'un nombre de calories réduit, voire négligea­ble. Ainsi par exemple, un produit selon l'invention contenant 60 % en poids de saccharose et 40 % en poids d'AP aura un pouvoir sucrant égal à environ 80 fois celui du saccharose ; en d'autres termes, à pouvoir su­crant égal à celui du saccharose, ce produit n'apportera q'un nombre de calories correspondant à moins de 1 % de celui qui aurait été apporté par le saccharose, ce qui est négligeable.
Le nouveau produit édulcorant de l'invention peut être ajouté à des produits alimentaires divers, comme par exemple les boissons, les glaces, les produits laitiers tels les yaourts et le fromage blanc, la confiserie, ainsi qu'à des produits alimentaires sous forme de poudre, etc ....
La présente invention permet de réaliser une formulation adaptée à cha­que cas particulier spécifique éventuel, en choisissant notamment le(s) édulcorant(s) intense(s) présent(s) et en ajustant leur dosage.
According to a variant of the first method above, constituting the third method according to the invention, part of the intense sweetener is added at the granulation step a1), the complement being added at the step b).
The addition of water mentioned in step a1) of the methods of the invention may consist of an injection of water vapor or a spraying of water or a granulation solution.
As an intense sweetener which can be used in the present invention, there may be mentioned, by way of example, saccharin, saccharinates, acesulfame, and sweeteners of the dipeptide type, that is to say the esters of aspartylphenylalanine the most used of which is α-L-aspartyl-L-phenylalanine methyl ester known as aspartame (AP). This list is not exhaustive.
The new food product of the present invention based on sucrose and intense sweetener may also comprise a complementary support composed of one or more constituents such as gelling agents, texturizers, stabilizers, examples of such constituents are pectins, animal and vegetable proteins, in particular dairy proteins, fibers, carboxymethyl cellulose, cyclodextrins, etc.
The sweetening product of the present invention containing a complementary support can be prepared in various ways. Said additional support can be added during step b) of mixing under moderate conditions, either with all of the intense sweetener, in the case of the first process above, or with part of the intense sweetener , in the case of the third method above, either alone in the case of the second method above (in the latter case, step b) is added to the method).
According to a variant of the methods for preparing the sweetening product of the present invention containing a complementary support, part of the latter can be added at step a1), the rest being added at step b).
As indicated above, the addition of water mentioned in step a1) of the methods of the invention can consist of an injection of water vapor or a spraying of water or of a granulation solution. Said granulation solution can for example be a sucrose syrup or an aqueous solution of a complementary support, for example example a gelling solution of pectin.
Thus, it is possible in certain cases to introduce all or part of the possible additional support via spraying in the granulation step a1) of the method of a solution of said additional support. To better illustrate the present invention, a method of obtaining a granular food sweetening product according to the invention is described in more detail below, by way of example.
Icing sugar, that is to say, crystallized sucrose having an average diameter between 80 and 100 μm, is fed by means of a volumetric or gravimetric dosing device, for example a screw doser, at the top of the 'a granulation chamber. The lower part of this granulation chamber communicates with a fluidized bed in which air is blown, the temperature of which decreases from upstream to downstream, from a temperature> 100 ° C (hot air) to a temperature from 15 - 20 ° C (cold air). Water vapor is injected into the granulation chamber, substantially at the level of the incorporation of icing sugar, which creates, together with the hot air blown upstream of the fluidized bed, a turbulence which causes the particles to agglomerate. icing sugar between them and their subsequent granulation. The agglomerated and granulated particles fall by gravity to the lower part of the granulation chamber and are taken up by the air stream from the fluidized bed; they advance on the fluidized bed and are cooled by the cold air stream to 15 - 20 ° C before being evacuated from the fluidized bed to be sent to sieving, to provide sucrose particles having an appropriate granulation (average diameter included between 150 and 500 µm). These sucrose particles are then mixed with the intense sweetener in powder form in a "soft" mixer, for example a ribbon or coulter mixer, having a low speed of rotation. The required amount of intense sweetener can be incorporated one or more times.
By way of example, to make 50 kg of product according to the invention containing 30 kg of sucrose and 20 kg of intense sweetener, a 200-liter ribbon mixer can be used, the rotation speed of which is 30-40 revolutions / min. We can incorporate the 30 kg of saccharose sieved particles, the 20 kg of intense sweetener in one go, by mixing for 15 to 20 minutes, or else incorporate 6.7 kg of intense sweetener 3 times, the mixing time between each addition being 5 minutes and the final mixture being fixed at 10 minutes. Generally, the time for mixing the sieved sucrose particles after leaving the fluidized bed with the intense sweetener will be determined to be sufficient to obtain complete incorporation of the intense sweetener into the sucrose particles and a total homogeneity of the product.
The product of the invention, obtained for example according to a process as described above, is not a simple mixture of sucrose and intense sweetener. In this regard, ultrasound sedimentation tests were carried out on a product according to the invention containing 40% by weight of AP and 60% by weight of sucrose. Dosages at different heights did not reveal any significant deviation of the components.
The new sweetener product of the invention does not contain fines and is therefore easy to handle. It is stable in storage, and does not form agglomerates.
It is easy to dose precisely because of both its granular shape and its low apparent density.
It dissolves very well in water and its wettability is excellent. For example, 2.5 g of product according to the invention containing 1.5 g of sucrose and 1 g of AP dissolve in a liter of water at 20 ° C 4 times faster than 1 g of 'AP alone.
In addition, with a sweetening power equal to that of sucrose, the product according to the invention provides only a reduced number of calories, even negligible. Thus, for example, a product according to the invention containing 60% by weight of sucrose and 40% by weight of AP will have a sweetening power equal to approximately 80 times that of sucrose; in other words, with a sweetening power equal to that of sucrose, this product will only provide a number of calories corresponding to less than 1% of that which would have been provided by sucrose, which is negligible.
The new sweetener product of the invention can be added to various food products, such as for example drinks, ice creams, dairy products such as yogurts and fromage blanc, confectionery, as well as to food products in the form of powder, etc ...
The present invention makes it possible to produce a formulation adapted to each specific specific case, by choosing in particular the intense sweetener (s) present (s) and by adjusting their dosage.

Claims (14)

1. Produit édulcorant alimentaire granulaire comprenant du saccharose et au moins un édulcorant intense caractérisé en ce qu'il contient de 50 à 99 % en poids de saccharose et de 1 à 50 % en poids d'au moins un édulcorant intense, en ce que sa densité apparente est comprise entre 0,4 et 0,7 g/cm³ et en ce que le diamètre moyen des grains est compris entre 150 et 500 µm.1. Granular food sweetener product comprising sucrose and at least one intense sweetener characterized in that it contains from 50 to 99% by weight of sucrose and from 1 to 50% by weight of at least one intense sweetener, in that its apparent density is between 0.4 and 0.7 g / cm³ and in that the average grain diameter is between 150 and 500 µm. 2. Produit édulcorant selon la revendication 1 caractérisé par le fait que sa densité apparente est comprise entre 0,45 et 0,55 g/cm².2. Sweetening product according to claim 1 characterized in that its apparent density is between 0.45 and 0.55 g / cm². 3. Produit édulcorant selon l'une des revendications 1 et 2 caractérisé par le fait que le diamètre moyen des grains est égal à environ 200 µm.3. Sweetening product according to one of claims 1 and 2 characterized in that the average grain diameter is approximately 200 µm. 4. Produit édulcorant selon l'une quelconque des revendications 1 à 3 caractérisé par le fait qu'il comprend en outre un support complémentaire.4. Sweetening product according to any one of claims 1 to 3 characterized in that it further comprises an additional support. 5. Produit édulcorant selon la revendication 4 caractérisé par le fait que ledit support complémentaire est composé d'un ou plusieurs constituant choisis parmi les gélifiants, les texturants et let stabilisants tels les pectines, les protéines animales et végétales, en particulier les protéines laitières, les fibres, la carboxyméthyl-cellulose et les cyclodextrines.5. Sweetening product according to claim 4, characterized in that the said additional support is composed of one or more constituents chosen from gelling agents, texturizers and let stabilizers such as pectins, animal and vegetable proteins, in particular dairy proteins, fibers, carboxymethyl cellulose and cyclodextrins. 6. Procédé de préparation d'un produit édulcorant selon l'une des re­vendications 1 à 5 comprenant les étapes suivantes : a) préparation de particules de saccharose de diamètre moyen com­pris entre 150 et 500 µm comprenant les étapes de
a1) granulation du saccharose en phase humide dans un appareil de granulation en continu dans lequel est alimenté, à sa partie supérieure, le saccharose cristallisé ayant un dia­métre moyen compris entre 80 et 100 µm et on procéde à une addition d'eau, sensiblement au niveau de l'alimentation dudit saccharose cristallisé, de l'air chaud étant soufflé de façon ascendante dans ledit appareil de granulation :
a2) séchage et refroidissement, sur un lit fluidisé relié à la partie inférieure dudit appareil de granulation, des parti­cules de saccharose formées dans l'étape a1)
a3) tamisage des particules provenant de l'étape a2) de façon à obtenir des particules de saccharose ayant un diamètre moyen compris entre 150 et 500 µm ;
b) mélange des particules de saccharose provenant de l'étape a3) avec l'édulcorant intense sous forme de poudre et l'éventuel support complémentaire, dans des conditions modérées pendant un temps suffisant pour obtenir le produit souhaité.
6. Method for preparing a sweetening product according to one of claims 1 to 5 comprising the following steps: a) preparation of sucrose particles with an average diameter of between 150 and 500 μm comprising the steps of
a1) granulation of sucrose in the wet phase in a continuous granulation apparatus into which is fed, at its upper part, the crystallized sucrose having an average diameter of between 80 and 100 μm and an addition of water is carried out, substantially at the level of the supply of said crystallized sucrose, hot air being blown upwardly into said apparatus granulation:
a2) drying and cooling, on a fluidized bed connected to the lower part of said granulation apparatus, of the sucrose particles formed in step a1)
a3) sieving the particles from step a2) so as to obtain sucrose particles having an average diameter between 150 and 500 μm;
b) mixing the sucrose particles from step a3) with the intense sweetener in powder form and the optional additional support, under moderate conditions for a time sufficient to obtain the desired product.
7. Procédé de préparation d'un produit édulcorant selon l'une des revendications 1 à 5 comprenant les étapes de : a1) granulation en phase humide dans un appareil de granulation en continu dans lequel on alimente à sa partie supérieure le saccharose cristallisé ayant un diamètre moyen compris entre 80 et 100 µm avec l'édulcorant intense cristallisé ayant un diamètre moyen inférieur à environ 500 µm et le cas échéant le support complémentaire, éventuellement prémélangés audit saccharose cristallisé, et on procède à une addition d'eau sensiblement au niveau de l'alimentation des produits de départ cristallisés, de l'air chaud étant soufflé de façon ascendante dans ledit appareil de granulation ; a2) séchage et refroidissement, sur un lit fluidisé relié à la partie inférieure dudit appareil de granulation, des particules d'édulcorant granulaire formées dans l'étape a1) ; a3) tamisage des particules provenant de l'étape a2) de façon à obtenir des particules de l'édulcorant granulaire souhaité ayant un diamètre moyen compris entre 150 et 500 µm. 7. Method for preparing a sweetening product according to one of claims 1 to 5 comprising the steps of: a1) wet granulation in a continuous granulation apparatus in which the crystalline sucrose having an average diameter of between 80 and 100 μm is fed at its upper part with the intense crystallized sweetener having an average diameter of less than approximately 500 μm and if necessary, the additional support, possibly premixed with said crystallized sucrose, and a water addition is carried out substantially at the level of the supply of the crystallized starting products, hot air being blown upwardly into said granulation apparatus ; a2) drying and cooling, on a fluidized bed connected to the lower part of said granulation apparatus, of the granular sweetener particles formed in step a1); a3) sieving the particles from step a2) so as to obtain particles of the desired granular sweetener having an average diameter between 150 and 500 μm. 8. Procédé de préparation d'un produit édulcorant selon l'une des revendications 1 à 5 comprenant les étapes de : a) Préparation de particules d'édulcorant de diamètre moyen compris entre 150 et 500 µm comprenant les étapes de :
a1) granulation en phase humide dans un appareil de granulation en continu dans lequel on alimente à sa partie supérieure le saccharose cristallisé ayant un diamètre moyen compris entre 80 et 100 µm avec tout ou partie de l'édulcorant intense ayant un diamètre moyen inférieur à environ 500 µm et le cas échéant tout ou partie du support complémentaire, éventuellement prémélangés audit saccharose cristallisé, et on procède à une addition d'eau sensiblement au niveau de l'alimentation des produits de départ cristallisés, de l'air chaud étant soufflé de façon ascendante dans ledit appareil de granulation ;
a2) séchage et refroidissement, sur un lit fluidisé relié à la partie inférieure dudit appareil de granulation, des particules d'édulcorant granulaire formées dans l'étape a1) ;
a3) tamisage des particules provenant de l'étape a2) de façon à obtenir des particules d'édulcorant granulaire ayant un diamètre moyen compris entre 150 et 500 µm ;
b) mélange des particules d'édulcorant granulaire provenant de l'étape a3) avec le reste de l'édulcorant intense sous forme de poudre et le reste de l'éventuel support complémentaire, dans des conditions modérées pendant un temps suffisant pour obtenir le produit souhaité.
8. Method for preparing a sweetening product according to one of claims 1 to 5 comprising the steps of: a) Preparation of sweetener particles with an average diameter of between 150 and 500 μm comprising the steps of:
a1) wet phase granulation in a continuous granulation apparatus in which the crystalline sucrose having an average diameter between 80 and 100 μm is fed at its upper part with all or part of the intense sweetener having an average diameter less than approximately 500 μm and, if appropriate, all or part of the additional support, possibly premixed with said crystallized sucrose, and a water addition is carried out substantially at the level of the supply of the crystallized starting products, hot air being blown so ascending in said granulator;
a2) drying and cooling, on a fluidized bed connected to the lower part of said granulation apparatus, of the granular sweetener particles formed in step a1);
a3) sieving the particles from step a2) so as to obtain granular sweetener particles having an average diameter between 150 and 500 μm;
b) mixing the particles of granular sweetener from step a3) with the rest of the intense sweetener in powder form and the rest of the optional additional support, under moderate conditions for a time sufficient to obtain the product wish.
9. Procédé selon la revendication 8 dans lequel la totalité de l'édulcorant intense est ajoutée lors de l'étape b).9. The method of claim 8 wherein all of the intense sweetener is added in step b). 10. Procédé selon la revendication 8 dans lequel la totalité de l'éventuel support complémentaire est ajoutée au cours de l'étape b).10. The method of claim 8 wherein all of the possible additional support is added during step b). 11. Procédé selon l'une quelconque des revendications 6 à 10 dans lequel ladite addition d'eau de l'étape a1) consiste en une injection de vapeur d'eau.11. Method according to any one of claims 6 to 10 wherein said addition of water from step a1) consists of an injection of steam. 12. Procédé selon l'une quelconque des revendications 6 à 10 dans lequel ladite addition d'eau de l'étape a1) consiste en une pulvérisation d'eau ou d'une solution de granulation.12. Method according to any one of claims 6 to 10 wherein said addition of water from step a1) consists of spraying water or a granulation solution. 13. Procédé selon la revendication 12 dans lequel ladite solution de granulation est un sirop de saccharose.13. The method of claim 12 wherein said granulation solution is a sucrose syrup. 14. procédé selon la revendication 12 dans lequel ladite solution de granulation est une solution du support complémentaire, par exemple une solution de gélifiant.14. The method of claim 12 wherein said granulation solution is a solution of the complementary support, for example a gelling solution.
EP88403366A 1988-07-25 1988-12-30 Food-sweetening compound based on sucrose and a strong sweetener, and process to prepare it Expired - Lifetime EP0352393B1 (en)

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AT88403366T ATE90114T1 (en) 1988-07-25 1988-12-30 FOOD SWEETENERS BASED ON SUCROSE AND INTENSIVE SWEETENERS, AND PROCESS FOR THE MANUFACTURE OF THE SAME.

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FR8810004 1988-07-25
FR8810004A FR2634355B1 (en) 1988-07-25 1988-07-25 NOVEL FOOD SWEETENER BASED ON SUCROSE AND INTENSE SWEETENER AND PROCESS FOR PREPARING THE SAME

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AT (1) ATE90114T1 (en)
AU (1) AU619242B2 (en)
CA (1) CA1340757C (en)
DE (1) DE3881517T2 (en)
DK (1) DK171849B1 (en)
ES (1) ES2040882T3 (en)
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Cited By (2)

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Publication number Priority date Publication date Assignee Title
EP1166651A1 (en) * 1996-02-29 2002-01-02 Fujisawa Pharmaceutical Co., Ltd. Synthetic sweetener
US7785646B2 (en) * 2001-06-26 2010-08-31 Beghin-Say Method for drying a saccharose solution, product thus obtained and use thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITMI972556A1 (en) * 1997-11-18 1999-05-18 B Ma S N C Di Cafano Giuseppe PROCEDURE AND MEANS OF IMPROVEMENT OF BEVERAGES IN GENERAL AS A RESULT OF THEIR EDUCATION AT THE TIME OF CONSUMPTION

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EP0052919A2 (en) * 1980-10-22 1982-06-02 Amstar Corporation Crystallized, readily water-dispersible sugar product
EP0102032A1 (en) * 1982-08-17 1984-03-07 Ajinomoto Co., Inc. Stabilized aspartame compositions
EP0106910A1 (en) * 1982-10-22 1984-05-02 Ajinomoto Co., Inc. Dipeptide sweeteners in the form of shaped bodies and process for their production
EP0218570A1 (en) * 1985-05-06 1987-04-15 "Raffinerie Tirlemontoise", société anonyme: Sugaring product, process to prepare it and apparatus for carrying out this process
EP0219150A2 (en) * 1985-09-18 1987-04-22 "Raffinerie Tirlemontoise", société anonyme: Sweetening product

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FR2581515B1 (en) * 1985-05-07 1991-01-18 Polive Wuhrlin Sa Laboratoires PROCESS FOR INCORPORATING A LOW-WATER-SOLUBLE HYGROSCOPIC SUBSTANCE, IN PARTICULAR ASPARTAME, IN A SUGAR-BASED FOOD PRODUCT

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EP0052919A2 (en) * 1980-10-22 1982-06-02 Amstar Corporation Crystallized, readily water-dispersible sugar product
EP0102032A1 (en) * 1982-08-17 1984-03-07 Ajinomoto Co., Inc. Stabilized aspartame compositions
EP0106910A1 (en) * 1982-10-22 1984-05-02 Ajinomoto Co., Inc. Dipeptide sweeteners in the form of shaped bodies and process for their production
EP0218570A1 (en) * 1985-05-06 1987-04-15 "Raffinerie Tirlemontoise", société anonyme: Sugaring product, process to prepare it and apparatus for carrying out this process
EP0219150A2 (en) * 1985-09-18 1987-04-22 "Raffinerie Tirlemontoise", société anonyme: Sweetening product

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1166651A1 (en) * 1996-02-29 2002-01-02 Fujisawa Pharmaceutical Co., Ltd. Synthetic sweetener
US7785646B2 (en) * 2001-06-26 2010-08-31 Beghin-Say Method for drying a saccharose solution, product thus obtained and use thereof

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NO177951C (en) 1995-12-27
DK75990A (en) 1990-03-23
DE3881517T2 (en) 1993-09-23
ATE90114T1 (en) 1993-06-15
NO177951B (en) 1995-09-18
NO901367D0 (en) 1990-03-23
FI901323A0 (en) 1990-03-16
DK75990D0 (en) 1990-03-23
JPH02502252A (en) 1990-07-26
FI100449B (en) 1997-12-15
JPH0614840B2 (en) 1994-03-02
ES2040882T3 (en) 1993-11-01
AU619242B2 (en) 1992-01-23
FR2634355A1 (en) 1990-01-26
FR2634355B1 (en) 1990-09-14
EP0352393B1 (en) 1993-06-02
NO901367L (en) 1990-03-23
AU2912089A (en) 1990-02-19
CA1340757C (en) 1999-09-21
DK171849B1 (en) 1997-07-07
WO1990001070A1 (en) 1990-02-08
DE3881517D1 (en) 1993-07-08

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