WO2007074196A1 - Dehydrated grape must and spray method for obtaining same - Google Patents

Dehydrated grape must and spray method for obtaining same Download PDF

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Publication number
WO2007074196A1
WO2007074196A1 PCT/ES2006/000715 ES2006000715W WO2007074196A1 WO 2007074196 A1 WO2007074196 A1 WO 2007074196A1 ES 2006000715 W ES2006000715 W ES 2006000715W WO 2007074196 A1 WO2007074196 A1 WO 2007074196A1
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Prior art keywords
grape
dehydrated
product
air
atomization
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PCT/ES2006/000715
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Spanish (es)
French (fr)
Inventor
Maria Soledad PÉREZ COELLO
María Consuelo DÍAZ MAROTO
Carmen DE TORRES SÁNCHEZ-SIMÓN
Original Assignee
Universidad De Castilla-La Mancha (Uclm)
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Priority claimed from ES200503218A external-priority patent/ES2299323B1/en
Application filed by Universidad De Castilla-La Mancha (Uclm) filed Critical Universidad De Castilla-La Mancha (Uclm)
Publication of WO2007074196A1 publication Critical patent/WO2007074196A1/en

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Classifications

    • 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
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/02Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation containing fruit or vegetable juices
    • A23L2/08Concentrating or drying of juices
    • A23L2/10Concentrating or drying of juices by heating or contact with dry gases
    • A23L2/102Spray-drying
    • 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
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/385Concentrates of non-alcoholic beverages
    • A23L2/39Dry compositions

Definitions

  • the present invention relates to the food industry and the wine industry sector.
  • the dehydration of products constitutes a highly recommended way of preserving them by offering a longer prolongation over time than other options, such as the pasteurization of fruit juices whose storage does not exceed twelve months, while from an economic point of view dehydration is more profitable as regards the storage and transport of the dehydrated product compared to processes such as freezing and concentration that entail additional costs for maintenance and handling, while requiring refrigeration in the transport of the product, which does not happen with dehydration .
  • the present invention relates to grape must that is dehydrated in order to be able to preserve it for long periods of time in order to reduce the problem of loss of large surpluses of grape must during the harvest seasons, in which it takes place the maximum production of the same, and that is lost quickly due to its high capacity to ferment.
  • Dehydration of grape must is also advisable from an economic point of view as it is more profitable in terms of storage and transport, due to the notable reduction in its volume, compared to other procedures, such as freezing and concentration, which they are more expensive and their handling is more complicated, since dehydration allows grape must to be stored at room temperature and its transport does not require refrigeration mechanisms.
  • dehydration of grape must, when performed under mild conditions, ensures high retention of its properties organoleptic which are those that give it its value.
  • a dehydrated grape must in powdery and very low hygroscopic form containing 2% moisture is added to the indicated state of the art relating to the conservation of fruit juices.
  • the volume of the grape must decreases to 90% and the weight to 70%. Its water activity is between 0.140-0.250, which prevents the growth of microorganisms. In the same way it is not possible to generate chemical reactions of degradation of nutrients as well as compounds responsible for the organoleptic characteristics of grape must. From the above characteristics it follows that it is a product whose storage and transport is much simpler and cheaper than in the case of the original product since it requires less space, weighs less and does not need refrigeration.
  • the present invention provides the obtaining of a dehydrated grape must capable of being preserved for long periods of time and that, in addition, it has almost the full potential of the grape for winemaking.
  • the present invention relates to obtaining the said dehydrated grape must by means of the atomization process, which implies a reduction of liquid size in small droplets, thereby increasing the surface-volume ratio, which increases the speed of dehydration
  • the atomization process consists in obtaining a powder product from a liquid material that is finely pulverized and enters .in contact with a stream of hot air, allowing rapid drying and obtaining a dry powder.
  • the main characteristics of this process are therefore the uniformity of the final product and very short drying times, of the order of 1 second. This is possible because of the small particle size, a diameter of 10-200 ⁇ m, which gives the drying air a very large surface area per unit volume.
  • the residence time of the dried particles in the drying chamber can be controlled to be minimal and thus overheating of the dry product does not occur.
  • This product transformation behavior into something Gummy is due to a low Vitreous Transition Temperature (Tg) presented by the low molecular weight sugars that constitute the juice of feints.
  • Tg Vitreous Transition Temperature
  • the Vitrea Transition is an intermolecular phenomenon in which cooperative movements of segments of the chain take place depending on the capacity of movement within the system, this being considered a second-order phase transition, unlike the melting point that would be first .
  • This transition is generally characterized by discontinuities in the physical, mechanical and thermal properties of food.
  • the measurement of thermal and mechanical properties is the essence of the techniques used to study this phenomenon.
  • Differential Scanning Calorimetry DSC Differential Scanning Calorimetry
  • the principle on which the method is based is the measurement of the difference in energy flow between two substances, one of them reference, when subjected to the same controlled temperature program.
  • the present invention introduces a modification of the product in the process with the intention of raising the glass transition temperature of the feed liquid.
  • this invention incorporates an anti-caking agent, Maltodextrin, as an additive to the feed liquid.
  • Maltodextrin an anti-caking agent
  • the concentration of these should not be any since the technical limits of operation of the system will have to be taken into account, since they increase the viscosity interfering with the operation of the atomizer.
  • the indicated Maltodextrin is a glucose polymer that is used as an additive that lacks smell, color and taste, in addition to having an affordable price.
  • Maltodextrins that differ fundamentally by their DE: Equivalent Dextrose, which is defined as the percentage of reduced sugar calculated as dextrose based on its dry weight. In other words, the number of glucoses that make up the polymer chain. This union between glucose units is usually through ⁇ -type links (l-> 4) and ED less than 20.
  • the time required to dehydrate the grape must by lyophilization is 18 hours, while dehydration by atomization takes about 1 hour, requiring no additional process.
  • the dehydrated grape must object of the present invention dehydrated through a claimed atomization process, is obtained from the preparation of a homogeneous solution consisting of original must and a percentage between 10 % and 25% of Maltodextrin anti-caking additive, which will depend on the percentage of dry extract present in the grape must juice that is intended to dehydrate.
  • the mixture is then introduced to the head of atomization through a peristaltic pump.
  • the spraying or disintegration of the liquid in the atomizer head is produced by the pressure exerted by a gas, in this case the air, which is introduced at a pressure between 400-800 L / h.
  • the sprayed liquid is introduced into a drying chamber in which it comes into contact with hot air causing very rapid drying.
  • the inlet temperature to which the air is applied is between 110-160 0 C, thus ensuring the practical elimination of water, which results in a dehydrated product with a water activity between 0.14 and 0.25, the temperature being output between 60-85 0 C.
  • the separation of the humid air from the dry product is produced by the action of an air vacuum that drags the product into the collecting chamber. As drying is so rapid, no deterioration occurs due to high temperatures as in other dehydration methods.
  • the final product of dehydrated grape must obtained by means of the now claimed atomization process is powdery, very little hygroscopic, with the greatest possible stability, in the form of white powder of easy handling, with a density between 0.4 and 0.6 g / cm 3 , with a water activity between 0.14 and 0.25, which prevents microbial growth, which is easily reconstitutable and decreases the volume of grape must up to 90% and up to 70% in weight, keeping the product dehydrated properties
  • Organoleptic grape must by offering a very high retention of volatile compounds.

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  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Seasonings (AREA)
  • Preparation Of Fruits And Vegetables (AREA)

Abstract

The invention relates to dehydrated grape must and to a spray method for obtaining same in powder form. The dehydrated grape must takes the form of an easy-to-handle, very stable white powder having a density of between 0.4-06 g/cm3, which is not very hygroscopic and which has a moisture content of 2 %. The volume of the inventive dehydrated grape must has been reduced by up to 90 %, while the weight thereof has been reduced by up to 70 %. In addition, the grape must has a water activity of between 0.14-0.25. The grape must has a prolonged storage life and can be transported easily and economically since it occupies less space, weighs less and does not require refrigeration. The must does not experience a significant loss of volatile compounds, while conserving C6 alcohols, terpenes and benzenes. The must is a good flavour enhancer which can be used in the production of food products, in confectionery and as a sweetener in the food industry. The invention also relates to grape must which has been dehydrated using the spray method and which includes the anti-caking additive maltodextrin at a percentage of 10 %-25 % in homogeneous solution with the must. The liquid spray is introduced into a drying chamber with hot air at between 110-160 °C, such as to obtain very fast drying. The water activity of the dehydrated product is less than 0.25 and the outlet temperature is between 60-85 °C.

Description

MOSTO DE UVA DESHIDRATADO MUST OF DEHYDRATED GRAPE
Y PROCEDIMIENTO DE ATOMIZACIÓNAND ATOMIZATION PROCEDURE
PARA SU OBTENCIÓNFOR YOUR OBTAINING
Sector de la técnicaTechnical sector
Se refiere la presente invención al sector de la industria alimentaria y a la vitivinícola.The present invention relates to the food industry and the wine industry sector.
Estado de Ia técnica La presente invención tiene como antecedente y prioridad laState of the art The present invention has as background and priority the
Patente Divisional española n° P200601890, titulada: "Mosto de uva deshidratado y procedimiento de atomización para su obtención", depositada el 14 de julio de 2006 ante la Oficina Española de Patentes y Marcas, procedente de la originaria Patente de Invención española n° 200503218, titulada: "Obtención de mosto en polvo mediante las técnicas de atomización y liofilización", que a nombre de la misma Universidad de Castilla-La Mancha (UCLM) se depositó el 28 de diciembre de 2005 ante la misma citada Oficina Española de Patentes y Marcas.Spanish Divisional Patent No. P200601890, entitled: "Dehydrated grape must and atomization procedure for obtaining it", filed on July 14, 2006 before the Spanish Patent and Trademark Office, from the original Spanish Invention Patent No. 200503218 , entitled: "Obtaining powdered must by atomization and lyophilization techniques", which on behalf of the same University of Castilla-La Mancha (UCLM) was deposited on December 28, 2005 before the same Spanish Patent Office and Marks
Explicación de Ia invenciónExplanation of the invention
La deshidratación de productos, tales como las frutas, constituye una forma de conservación de los mismos altamente recomendable al ofrecer una mayor prolongación en el tiempo que otras opciones, tal como sucede con la pasteurización de zumos de frutas cuyo almacenaje no sobrepasa los doce meses, al tiempo que desde un punto de vista económico la deshidratación es más rentable por lo que afecta al almacenamiento y transporte del producto deshidratado en comparación con procesos como la congelación y la concentración que conllevan costes adicionales para el mantenimiento y la manipulación, al tiempo que requieren refrigeración en el transporte del producto, lo que no sucede con la deshidratación.The dehydration of products, such as fruits, constitutes a highly recommended way of preserving them by offering a longer prolongation over time than other options, such as the pasteurization of fruit juices whose storage does not exceed twelve months, while from an economic point of view dehydration is more profitable as regards the storage and transport of the dehydrated product compared to processes such as freezing and concentration that entail additional costs for maintenance and handling, while requiring refrigeration in the transport of the product, which does not happen with dehydration .
La presente invención se refiere a mosto de uva que es deshidratado con el fin de poder conservarlo durante largos períodos de tiempo a fin de reducir el problema de pérdida de los grandes excedentes de mosto de uva durante las temporadas de vendimia, en las que tiene lugar la máxima producción del mismo, y que se pierde rápidamente debido a su elevada capacidad para fermentar.The present invention relates to grape must that is dehydrated in order to be able to preserve it for long periods of time in order to reduce the problem of loss of large surpluses of grape must during the harvest seasons, in which it takes place the maximum production of the same, and that is lost quickly due to its high capacity to ferment.
Para evitar el problema de la rápida fermentación y consecuente pérdida del mosto de uva en el estado de la técnica se conoce la utilización de sulfuroso, que evita también el crecimiento microbiano, pero los porcentajes en que actualmente se permite la utilización legal de ese producto son cada vez más bajos y de otro lado no siempre soluciona los problemas que se pretenden evitar con su utilización.To avoid the problem of rapid fermentation and consequent loss of grape must in the state of the art, the use of sulfur is known, which also prevents microbial growth, but the percentages in which the legal use of that product is currently allowed are increasingly low and on the other hand does not always solve the problems that are intended to be avoided with its use.
La deshidratación del mosto de uva es también aconsejable desde un punto de vista económico al ser más rentable en cuanto al almacenamiento y transporte, debido a la notable reducción de su volumen, en comparación con otros procedimientos, tales como la congelación y la concentración, que son más caros y su manipulación es más complicada, dado que la deshidratación permite que el mosto de uva sea almacenado a temperatura ambiente y su transporte no requiere mecanismos de refrigeración.Dehydration of grape must is also advisable from an economic point of view as it is more profitable in terms of storage and transport, due to the notable reduction in its volume, compared to other procedures, such as freezing and concentration, which they are more expensive and their handling is more complicated, since dehydration allows grape must to be stored at room temperature and its transport does not require refrigeration mechanisms.
Asimismo, la deshidratación del mosto de uva, al realizarse bajo condiciones suaves, asegura una elevada retención de sus propiedades organolépticas que son las que le otorgan su valor.Also, dehydration of grape must, when performed under mild conditions, ensures high retention of its properties organoleptic which are those that give it its value.
Solución técnica aportada por esta invenciónTechnical solution provided by this invention
Con la presente invención se aporta al indicado estado de la técnica relativo a la conservación de los zumos de fruta un mosto de uva deshidratado en forma pulverulenta y muy poco higroscópico que contiene una humedad del 2%.With the present invention, a dehydrated grape must in powdery and very low hygroscopic form containing 2% moisture is added to the indicated state of the art relating to the conservation of fruit juices.
Con la eliminación de prácticamente el total del agua, el volumen del mosto de uva disminuye hasta el 90% y el peso hasta un 70%. Su actividad de agua está comprendida entre el 0.140-0.250, lo que imposibilita el crecimiento de microorganismos. Del mismo modo no es posible que se generen reacciones químicas de degradación de nutrientes así como de compuestos responsables de las características organolépticas del mosto de uva. De las expuestas características se deduce que se trata de un producto cuyo almacenaje y transporte resulta mucho más sencillo y económico que en el caso del producto original puesto que requiere menos espacio, pesa menos y no necesita refrigeración.With the elimination of practically the total water, the volume of the grape must decreases to 90% and the weight to 70%. Its water activity is between 0.140-0.250, which prevents the growth of microorganisms. In the same way it is not possible to generate chemical reactions of degradation of nutrients as well as compounds responsible for the organoleptic characteristics of grape must. From the above characteristics it follows that it is a product whose storage and transport is much simpler and cheaper than in the case of the original product since it requires less space, weighs less and does not need refrigeration.
Los métodos de análisis de compuestos volátiles muestran que la pérdida o deterioro de los mismos no resulta significativa, conservando compuestos del tipo alcoholes Ce, terpenos así como compuestos bencénicos. Todos estos son responsables de notas aromáticas herbáceas, a flores, olor fresco etc. Todo ello le confiere al mosto de uva deshidratado conforme a la presente invención la capacidad de ser un buen potenciador de sabor en la elaboración de numerosos productos alimenticios, lo que unido a su presentación en forma de sólido pulverulento determina que sea particularmente utilizable para la preparación de productos de repostería, o bien como edulcorante en la industria alimentaria.The methods of analysis of volatile compounds show that the loss or deterioration thereof is not significant, preserving compounds such as Ce alcohols , terpenes as well as benzene compounds. All these are responsible for herbaceous aromatic notes, flowers, fresh smell etc. All this gives the dehydrated grape must according to the present invention the ability to be a good flavor enhancer in the manufacture of numerous food products, which together with its presentation as a powdery solid determines that it is particularly usable for preparation of pastry products, or as a sweetener in the food industry.
En los procesos habitualmente utilizados para la eliminación de agua se utilizan altas temperaturas, lo que provoca, por la existencia de gran cantidad de azúcares junto con la presencia de aminoácidos, la formación de compuestos, tal como los derivados de furfural que aportan aromas desagradables, así como derivados de lactonas que dan lugar a los mismos resultados. Sin embargo, en el caso del mosto de uva deshidratado conforme al procedimiento reivindicado en la presente patente divisional, al utilizar condiciones suaves y al emplear un secado rápido, la formación de los mencionados compuestos no es significativa.In the processes normally used for the elimination of water, high temperatures are used, which causes, due to the existence of a large amount of sugars together with the presence of amino acids, the formation of compounds, such as those derived from furfural that provide unpleasant aromas, as well as derivatives of lactones that give rise to the same results. However, in the case of dehydrated grape must according to the procedure claimed in this divisional patent, when using mild conditions and when using rapid drying, the formation of said compounds is not significant.
De lo anterior se concluye que la presente invención aporta la obtención de un mosto de uva deshidratado capaz de ser conservado durante largos periodos de tiempo y que, además, posee la práctica totalidad del potencial de la uva para la elaboración de vino.From the foregoing it is concluded that the present invention provides the obtaining of a dehydrated grape must capable of being preserved for long periods of time and that, in addition, it has almost the full potential of the grape for winemaking.
Lo anterior también permite que el mosto de uva deshidratado objeto de la presente invención sea utilizado en zonas de clima frío, particularmente en los países del norte de Europa, en el proceso deThe foregoing also allows the dehydrated grape must object of the present invention to be used in cold weather areas, particularly in northern European countries, in the process of
"Chaptalización", que es la adición de azúcar procedente de mosto a mostos con bajo contenido en azúcares."Chaptalización", which is the addition of sugar from must to musts with low sugar content.
La presente invención se refiere a la obtención del comentado mosto de uva deshidratado mediante el procedimiento de atomización, el cual implica una reducción de tamaño de líquidos en pequeñas gotitas, consiguiendo de este modo aumentar la relación superficie- volumen, lo que incrementa la velocidad de deshidratación.The present invention relates to obtaining the said dehydrated grape must by means of the atomization process, which implies a reduction of liquid size in small droplets, thereby increasing the surface-volume ratio, which increases the speed of dehydration
El proceso de atomización consiste en obtener un producto en polvo a partir de un material líquido que se pulveriza finamente y entra .en contacto con una corriente de aire caliente, lo que permite una desecación rápida y la obtención de un polvo seco.The atomization process consists in obtaining a powder product from a liquid material that is finely pulverized and enters .in contact with a stream of hot air, allowing rapid drying and obtaining a dry powder.
Las características principales de este proceso son por tanto la uniformidad del producto final y tiempos de desecación muy cortos, del orden de 1 segundo. Esto es posible por el pequeño tamaño de las partículas, un diámetro de 10-200 μm, lo que ofrece al aire de desecación un área superficial muy grande por unidad de volumen.The main characteristics of this process are therefore the uniformity of the final product and very short drying times, of the order of 1 second. This is possible because of the small particle size, a diameter of 10-200 μm, which gives the drying air a very large surface area per unit volume.
La mayor parte de la desecación ocurre en condiciones que favorecen un secado a velocidad constante y por tanto la temperatura de los sólidos apenas se eleva por encima de la temperatura del bulbo húmedo.Most of the drying occurs in conditions that favor drying at a constant speed and therefore the temperature of the solids barely rises above the temperature of the wet bulb.
Si las condiciones de operación son correctas y el equipo está bien diseñado, el tiempo de permanencia de las partículas secas en la cámara de desecación puede controlarse para que sea mínimo y así no se produzca el sobrecalentamiento del producto seco.If the operating conditions are correct and the equipment is well designed, the residence time of the dried particles in the drying chamber can be controlled to be minimal and thus overheating of the dry product does not occur.
De este modo se consigue que las sustancias responsables del aroma y el sabor del alimento atomizado se retengan durante el proceso. Pero, además, en el proceso de secado por atomización es necesario tener en consideración el producto a deshidratar. Esto es, existen dos tipos de productos, los llamados "no gomosos" y los "gomosos". Estos últimos generan numerosos problemas a la hora de llevar a cabo el proceso. Este tipo de producto gomoso lo forman aquellos que son ricos en azúcares, tal como los jugos o purés de frutas, provocando que sea éste un proceso técnicamente difícil, debido a la elevada higroscopicidad y termoplasticidad de los mismos en condiciones de alta humedad y temperatura.In this way it is achieved that the substances responsible for the aroma and flavor of the atomized food are retained during the process. But, in addition, in the process of spray drying it is necessary to take into account the product to be dehydrated. That is, there are two types of products, the so-called "non-gummy" and the "gummy". The latter generate numerous problems when carrying out the process. This type of gummy product is formed by those that are rich in sugars, such as fruit juices or purees, causing this to be a technically difficult process, due to the high hygroscopicity and thermoplasticity of the same in conditions of high humidity and temperature.
Este comportamiento de transformación del producto en algo gomoso es debido a una baja Temperatura de Transición Vitrea (Tg) que presentan los azúcares de bajo peso molecular que constituyen los zumos de fintas. La Transición Vitrea es un fenómeno intermolecular en el que tienen lugar movimientos cooperativos de segmentos de la cadena en función de la capacidad de movimiento dentro del sistema, considerándose ésta una transición de fase de segundo orden, a diferencia del punto de fusión que seria de primero. Esta transición se caracteriza generalmente por las discontinuidades en las propiedades físicas, mecánicas y térmicas de los alimentos. La medida de las propiedades térmicas y mecánicas es la esencia de las técnicas usadas para el estudio de este fenómeno. En particular es utilizada la Calorimetría de Barrido Diferencial (DSC Differential Scanning Calorimetry). El principio en el que se basa el método es la medida de la diferencia de flujo de energía entre dos sustancias, una de ellas de referencia, cuando se someten a un mismo programa de temperatura controlada.This product transformation behavior into something Gummy is due to a low Vitreous Transition Temperature (Tg) presented by the low molecular weight sugars that constitute the juice of feints. The Vitrea Transition is an intermolecular phenomenon in which cooperative movements of segments of the chain take place depending on the capacity of movement within the system, this being considered a second-order phase transition, unlike the melting point that would be first . This transition is generally characterized by discontinuities in the physical, mechanical and thermal properties of food. The measurement of thermal and mechanical properties is the essence of the techniques used to study this phenomenon. In particular, Differential Scanning Calorimetry (DSC Differential Scanning Calorimetry) is used. The principle on which the method is based is the measurement of the difference in energy flow between two substances, one of them reference, when subjected to the same controlled temperature program.
Los problemas que provoca este fenómeno en el proceso de secado es que el líquido que va a ser secado se transforma en algo gomoso y altamente adherente a las paredes de la cámara de secado (lugar donde entra en contacto el producto inicial con el aire caliente) disminuyendo el rendimiento, dando lugar a la fusión completa del producto sin que llegue a formarse polvo.The problems caused by this phenomenon in the drying process is that the liquid to be dried is transformed into something rubbery and highly adherent to the walls of the drying chamber (place where the initial product comes into contact with the hot air) diminishing the yield, giving rise to the complete fusion of the product without getting to form dust.
Para evitar el comentado problema la presente invención introduce en el procedimiento una modificación del producto con la intención de elevar la Temperatura de Transición vitrea del líquido de alimentación. A tal fin, esta invención incorpora como aditivo al líquido de alimentación un antiapelmazante, la Maltodextrina. La consecuencia de utilizar este tipo de aditivo es que se eleva la Tg, lo que permite utilizar una temperatura mayor en el aire de secado, lo que da como resultado productos con menor humedad y más estables. Sin embargo la concentración de estos no debe ser cualquiera ya que habrá que tener en cuenta los límites técnicos de operación del sistema, ya que aumentan la viscosidad interfiriendo esto en el funcionamiento del atomizador.To avoid the aforementioned problem, the present invention introduces a modification of the product in the process with the intention of raising the glass transition temperature of the feed liquid. To this end, this invention incorporates an anti-caking agent, Maltodextrin, as an additive to the feed liquid. The consequence of using this type of additive is that the Tg rises, which allows a higher temperature to be used in the drying air, which results in products with lower humidity and more stable. However, the concentration of these should not be any since the technical limits of operation of the system will have to be taken into account, since they increase the viscosity interfering with the operation of the atomizer.
La indicada Maltodextrina es un polímero de glucosa que se utiliza como aditivo que carece de olor, color y sabor, además de tener un precio asequible. Existen distintos tipos de Maltodextrinas que se diferencian fundamentalmente por su DE: Dextrosa Equivalente, lo que se define como el porcentaje de azúcar reducido calculado como dextrosa en base a su peso seco. Es decir el número de glucosas que componen la cadena de polímero. Esta unión entre las unidades de glucosa suele ser a través de enlaces de tipo α(l->4) y el DE menor de 20.The indicated Maltodextrin is a glucose polymer that is used as an additive that lacks smell, color and taste, in addition to having an affordable price. There are different types of Maltodextrins that differ fundamentally by their DE: Equivalent Dextrose, which is defined as the percentage of reduced sugar calculated as dextrose based on its dry weight. In other words, the number of glucoses that make up the polymer chain. This union between glucose units is usually through α-type links (l-> 4) and ED less than 20.
Una vez obtenido el producto en forma de polvo hay que considerar una serie de propiedades físicas a las que hay que atribuir la facilidad con que se pueda reconstituir el producto y su estabilidad. Entre ellas está la actividad del agua, la densidad, la solubilidad y la mojabilidad. La densidad es un dato muy importante a tener en cuenta desde el punto de vista económico, ya que si es baja puede llegar a incrementar mucho los costes de envasado. Esta propiedad depende de la composición química, de la alimentación y del aire ocluido en las partículas.Once the product is obtained as a powder, a series of physical properties must be considered to which the ease with which the product can be reconstituted and its stability must be attributed. Among them is water activity, density, solubility and wettability. Density is a very important fact to take into account from an economic point of view, since if it is low it can greatly increase packaging costs. This property depends on the chemical composition, the feed and the air occluded in the particles.
Ventajas de la invenciónAdvantages of the invention
Las principales ventajas de la obtención de mosto de uva deshidratado a través del procedimiento de atomización objeto de la presente invención en contraste con el procedimiento de obtención de mosto de uva deshidratado mediante el procedimiento de liofilización objeto de la originaria Patente de Invención n° 200503218(2) son las siguientes:The main advantages of obtaining grape must dehydrated through the atomization process object of the present invention in contrast to the procedure for obtaining dehydrated grape must by the lyophilization process object of the original Invention Patent No. 200503218 (2) are the following:
En el proceso de liofilización es necesario congelar el producto para que la eliminación del agua se produzca por sublimación, lo que conlleva mas tiempo y más gasto energético en la preparación de las muestras. El liofilizador trabaja a presiones muy bajas, lo que supone un gasto económico elevado.In the lyophilization process it is necessary to freeze the product so that the elimination of water occurs by sublimation, which entails more time and more energy expenditure in the preparation of the samples. The lyophilizer works at very low pressures, which means a high economic expense.
El tiempo que se requiere para deshidratar el mosto de uva mediante liofilización es de 18 horas, mientras que la deshidratación mediante atomización supone alrededor de 1 hora, no necesitando ningún proceso adicional.The time required to dehydrate the grape must by lyophilization is 18 hours, while dehydration by atomization takes about 1 hour, requiring no additional process.
El mantenimiento de las características organolépticas es muy semejante en ambas técnicas.The maintenance of the organoleptic characteristics is very similar in both techniques.
Modo preferente de realización de Ia invención El mosto de uva deshidratado objeto de la presente invención, deshidratado a través de un reivindicado procedimiento de atomización, se obtiene a partir de la preparación de una disolución homogénea constituida por mosto original y un porcentaje comprendido entre el 10% y el 25% de aditivo antiapelmazante Maltodextrina, lo que dependerá del porcentaje de extracto seco presente en el zumo de mosto de uva que se pretende deshidratar.Preferred mode of implementation of the invention The dehydrated grape must object of the present invention, dehydrated through a claimed atomization process, is obtained from the preparation of a homogeneous solution consisting of original must and a percentage between 10 % and 25% of Maltodextrin anti-caking additive, which will depend on the percentage of dry extract present in the grape must juice that is intended to dehydrate.
A continuación se introduce la mezcla hasta la cabeza de atomización a través de una bomba peristáltica.The mixture is then introduced to the head of atomization through a peristaltic pump.
Seguidamente se produce la aspersión o disgregación del líquido en la cabeza del atomizador por la presión que ejerce un gas, en este caso el aire, el cual es introducido a una presión comprendida entre 400- 800 L/h.Subsequently, the spraying or disintegration of the liquid in the atomizer head is produced by the pressure exerted by a gas, in this case the air, which is introduced at a pressure between 400-800 L / h.
El líquido pulverizado es introducido en una cámara de secado en la que entra en contacto con aire caliente provocando un secado muy rápido. La temperatura de entrada a la que se aplica el aire está comprendida entre 110-1600C, asegurando así la práctica eliminación del agua, lo que da lugar a un producto deshidratado con una actividad de agua comprendida entre 0.14 y 0.25, siendo la temperatura de salida entre 60-850C.The sprayed liquid is introduced into a drying chamber in which it comes into contact with hot air causing very rapid drying. The inlet temperature to which the air is applied is between 110-160 0 C, thus ensuring the practical elimination of water, which results in a dehydrated product with a water activity between 0.14 and 0.25, the temperature being output between 60-85 0 C.
La separación del aire húmedo del producto seco se produce por la acción de un aspirador de aire que arrastra el producto a la cámara colectora. Al ser tan rápido el secado no se producen deterioros por efecto de las altas temperaturas como así ocurre en otros métodos de deshidratación.The separation of the humid air from the dry product is produced by the action of an air vacuum that drags the product into the collecting chamber. As drying is so rapid, no deterioration occurs due to high temperatures as in other dehydration methods.
El producto final de mosto de uva deshidratado obtenido mediante el ahora reivindicado procedimiento de atomización es pulverulento, muy poco higroscópico, con la mayor estabilidad posible, en forma de polvo blanco de fácil manejo, con una densidad entre 0.4 y 0.6 g/cm3, con una actividad de agua comprendida entre 0.14 y 0.25, lo que evita el crecimiento microbiano, que es fácilmente reconstituible y que disminuye el volumen del mosto de uva hasta un 90% y hasta un 70% en su peso, manteniendo el producto deshidratado las propiedades organolépticas del mosto de uva al ofrecer una muy alta retención de los compuestos volátiles. Cuanto ha quedado descrito constituye un fiel reflejo de la presente invención, debiendo considerarse las características de la misma que han sido expuestas en sentido amplio y no limitativo, siendo indiferentes y cambiantes las circunstancias de carácter meramente formal, secundario o accesorio que no alteren la esencialidad que a continuación es reivindicada. The final product of dehydrated grape must obtained by means of the now claimed atomization process is powdery, very little hygroscopic, with the greatest possible stability, in the form of white powder of easy handling, with a density between 0.4 and 0.6 g / cm 3 , with a water activity between 0.14 and 0.25, which prevents microbial growth, which is easily reconstitutable and decreases the volume of grape must up to 90% and up to 70% in weight, keeping the product dehydrated properties Organoleptic grape must by offering a very high retention of volatile compounds. What has been described constitutes a faithful reflection of the present invention, having to consider the characteristics of the same that have been exposed in a broad and non-limiting sense, being circumstances that are merely formal, secondary or accessory that do not alter the essentiality are indifferent and changing. which is then claimed.

Claims

REIVINDICACIONES
Ia. Mosto de uva deshidratado y procedimiento de atomización para su obtención, caracterizado por estar deshidratado en forma de polvo blanco muy poco higroscópico, de gran estabilidad, fácilmente manejable y reconstituible, que es almacenable a temperatura ambiente de forma prolongada y a bajo coste.I a . Dehydrated grape must and atomization procedure to obtain it, characterized by being dehydrated in the form of a very low hygroscopic white powder, of great stability, easily manageable and reconstitutable, which can be stored at room temperature for a long time and at low cost.
2a. Mosto de uva deshidratado, según reivindicación anterior, caracterizado por ofrecer una densidad de entre 0.4 y 0.6 g/cm3. 3a. Mosto de uva deshidratado, según reivindicaciones anteriores, caracterizado por una actividad de agua comprendida entre 0.14 y 0.25.2 a . Dehydrated grape must, according to the preceding claim, characterized by offering a density between 0.4 and 0.6 g / cm 3 . 3 a . Dehydrated grape must, according to previous claims, characterized by a water activity between 0.14 and 0.25.
4a. Mosto de uva deshidratado, según reivindicaciones anteriores, caracterizado porque con respecto al producto hidratado ofrece una disminución de hasta un 90% en cuanto a volumen, lo que favorece su almacenaje y transporte, así como de un 70% en lo que se refiere al peso.4 a . Dehydrated grape must, according to previous claims, characterized in that with respect to the hydrated product it offers a decrease of up to 90% in terms of volume, which favors its storage and transport, as well as of 70% in terms of weight .
5a. Mosto de uva deshidratado, según reivindicaciones anteriores, caracterizado por contener una gran cantidad de azúcar, glucosa y fructosa que permite su uso como edulcorante sin provocar aumento de volumen.5 a . Dehydrated grape must, according to previous claims, characterized by containing a large amount of sugar, glucose and fructose that allows its use as a sweetener without causing volume increase.
6a. Procedimiento de atomización para la obtención de mosto de uva deshidratado, según reivindicaciones anteriores, a través de un proceso de atomización en condiciones suaves, caracterizado porque mantiene las propiedades organolépticas del producto deshidratado al ofrecer una muy alta retención de los compuestos volátiles, alcanzando una estabilidad térmica mayor y una menor higroscopicidad del producto al utilizar como aditivo el antiapelmazante Maltodextrina a partir de una disolución homogénea constituida por mosto de uva original y un porcentaje de aditivo Maltodestrina comprendido entre el 10% y el 25%; la mezcla se introduce hasta la cabeza de atomización a través de una bomba peristáltica; seguidamente se produce la aspersión o disgregación del líquido en la cabeza del atomizador por la presión que ejerce un gas, en este caso el aire, el cual es introducido a una presión comprendida entre 400-800 L/h.; el líquido pulverizado es introducido en una cámara de secado en la que entra en contacto con aire caliente provocando un secado muy rápido; la temperatura de entrada a la que se aplica el aire está comprendida entre 110-1600C, asegurando así la práctica eliminación del agua, lo que da lugar a un producto deshidratado con una actividad de agua comprendida entre 0.14 y 0.25, siendo la temperatura de salida del aire de 60-850C; la separación del aire húmedo del producto seco se produce por la acción de un aspirador de aire que arrastra el producto a la cámara colectora; el producto obtenido con este procedimiento no sufre deterioros al ser tan rápido el proceso de secado por efecto de las altas temperaturas. 7a. Mosto de uva deshidratado obtenido por el procedimiento de atomización objeto de la precedente reivindicación 6a. 6 a . Atomization process for obtaining dehydrated grape must, according to previous claims, through an atomization process under mild conditions, characterized in that it maintains the organoleptic properties of the dehydrated product by offering a very high retention of volatile compounds, achieving stability major and minor thermal hygroscopicity of the product when using as an additive the anti-caking agent Maltodextrin from a homogeneous solution consisting of original grape must and a percentage of additive Maltodestrin between 10% and 25%; the mixture is introduced to the atomization head through a peristaltic pump; then the spraying or disintegration of the liquid in the atomizer head is produced by the pressure exerted by a gas, in this case the air, which is introduced at a pressure between 400-800 L / h .; the sprayed liquid is introduced into a drying chamber in which it comes into contact with hot air causing very rapid drying; the inlet temperature to which the air is applied is between 110-160 0 C, thus ensuring the practical elimination of water, which results in a dehydrated product with a water activity between 0.14 and 0.25, the temperature being 60-85 0 C air outlet; The separation of the humid air from the dry product is produced by the action of an air vacuum that drags the product into the collecting chamber; The product obtained with this procedure does not suffer deterioration because the drying process is so rapid due to the high temperatures. 7 a . Dehydrated grape must obtained by the atomization process object of the preceding claim 6 a .
PCT/ES2006/000715 2005-12-28 2006-12-27 Dehydrated grape must and spray method for obtaining same WO2007074196A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
ES200503218A ES2299323B1 (en) 2005-12-28 2005-12-28 OBTAINING MUST IN POWDER THROUGH ATOMIZATION AND LIOFILIZATION TECHNIQUES.
ESP200503218 2005-12-28
ESP200601890 2006-07-14
ES200601890A ES2310452B1 (en) 2005-12-28 2006-07-14 MUST OF DEHYDRATED GRAPE AND ATOMIZATION PROCEDURE FOR OBTAINING.

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WO2007074196A1 true WO2007074196A1 (en) 2007-07-05

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2816039A (en) * 1955-01-10 1957-12-10 Roderick K Eskew Process for making powdered fruit juices
FR2054229A5 (en) * 1969-07-11 1971-04-16 Geigy Ag J R Freeze dried grape juice
ES405455A1 (en) * 1971-08-03 1975-07-16 Coca Cola Co Method of drying
ES481355A1 (en) * 1978-06-07 1980-02-01 Gen Foods Corp Stable fruit juice powder low in hygroscopicity and method for preparing thereof
US5118517A (en) * 1991-07-15 1992-06-02 F&Mp Research And Development Laboratories, Inc. Method of manufacturing powdered fruit juice using dextran

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2816039A (en) * 1955-01-10 1957-12-10 Roderick K Eskew Process for making powdered fruit juices
FR2054229A5 (en) * 1969-07-11 1971-04-16 Geigy Ag J R Freeze dried grape juice
ES405455A1 (en) * 1971-08-03 1975-07-16 Coca Cola Co Method of drying
ES481355A1 (en) * 1978-06-07 1980-02-01 Gen Foods Corp Stable fruit juice powder low in hygroscopicity and method for preparing thereof
US5118517A (en) * 1991-07-15 1992-06-02 F&Mp Research And Development Laboratories, Inc. Method of manufacturing powdered fruit juice using dextran

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