EP4333642A1 - Continuous binder liquid agglomeration method - Google Patents

Continuous binder liquid agglomeration method

Info

Publication number
EP4333642A1
EP4333642A1 EP22728118.5A EP22728118A EP4333642A1 EP 4333642 A1 EP4333642 A1 EP 4333642A1 EP 22728118 A EP22728118 A EP 22728118A EP 4333642 A1 EP4333642 A1 EP 4333642A1
Authority
EP
European Patent Office
Prior art keywords
powder
steam
binder
agglomerated
food
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP22728118.5A
Other languages
German (de)
French (fr)
Inventor
Bruno Edgar Chavez Montes
Michael Fritz
Leandro Martins
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Societe des Produits Nestle SA
Nestle SA
Original Assignee
Societe des Produits Nestle SA
Nestle SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Societe des Produits Nestle SA, Nestle SA filed Critical Societe des Produits Nestle SA
Publication of EP4333642A1 publication Critical patent/EP4333642A1/en
Pending legal-status Critical Current

Links

Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Preparation or treatment thereof
    • A23L2/385—Concentrates of non-alcoholic beverages
    • A23L2/39—Dry compositions
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
    • A23B2/00—Preservation of foods or foodstuffs, in general
    • A23B2/90—Preservation of foods or foodstuffs, in general by drying or kilning; Subsequent reconstitution
    • A23B2/95—Fluidised-bed drying
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; PREPARATION THEREOF
    • A23C11/00—Milk substitutes, e.g. coffee whitener compositions
    • A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
    • A23C11/10—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing or not lactose but no other milk components as source of fats, carbohydrates or proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
    • A23L11/00—Pulses, i.e. fruits of leguminous plants, for production of food; Products from legumes; Preparation or treatment thereof
    • A23L11/60—Drinks from legumes, e.g. lupine drinks
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/20—Agglomerating; Granulating; Tabletting
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/20—Agglomerating; Granulating; Tabletting
    • A23P10/22—Agglomeration or granulation with pulverisation of solid particles, e.g. in a free-falling curtain
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/40—Shaping or working of foodstuffs characterised by the products free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/40—Shaping or working of foodstuffs characterised by the products free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added
    • A23P10/47—Shaping or working of foodstuffs characterised by the products free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added using additives, e.g. emulsifiers, wetting agents or dust-binding agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/02—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
    • B01J2/04—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a gaseous medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/12—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried

Definitions

  • the present invention relates to a method for continuously producing soluble agglomerated food powder, in particular soluble agglomerated food powder comprising plant-based powder and sugar.
  • the invention also relates to the use of the soluble agglomerated food powder in cold beverages.
  • Soluble food powders such as chocolate or malt powders are currently used for preparing beverages by mixing water or milk with these powders.
  • the existing beverage dispenser devices which make use of the above outlined principle suffer the inconvenience that the beverage soluble powder is not always fully dissolved, particularly when a cold beverage is prepared by dissolving the powder with a cold diluent, either cold water or cold milk.
  • a cold diluent either cold water or cold milk.
  • residua of the undispersed or undissolved powder are present in the prepared beverage; this leads to a non-uniform and thus to a non-inviting appearance of the prepared beverage.
  • the final beverage does not present the expected taste; actually, there exists a fine tuning between the diluent volume and the powder quantity to get the best final beverage. If the dissolution is not efficient, the final beverage will not reach the expected taste. Undissolved material can also lead to a feeling of sandiness in the mouth and/or result in leftovers at the bottom of the cup when the drink is finished, with the consequent negative impression for the consumer.
  • WO 2007/088195 proposes to add flowing agents to food powders in order to improve their cold dissolution characteristics.
  • EP 740 904 describes a method to improve the wettability of agglomerated cocoa and sugar containing powders which consists in exposing the powders to electromagnetic radiation. Yet, improving the wettability is not sufficient to get a good dissolution of the powders at the moment of preparation of the beverages.
  • WO 2012/095121 proposes coating a cocoa powder or a cocoa cake with a hydrophilic agent like sugar. Yet such a solution increases the ratio of sugar in the beverage powder. It can affect the original taste of the cocoa and it increases the rate of sugar taken by the consumer unnecessarily.
  • the objective of the present invention is to improve the state of the art and in particular to provide a food powder that can be used e.g. as dairy alternative.
  • the object of the invention is also to provide a food powder that contains cocoa, malt or other plant material a good flowability and dispersibility and which can be used in powder dispensers.
  • the invention provides the improvement by the subject matter of the independent claims.
  • the dependent claims further develop the idea of the present invention.
  • the invention relates to a method for continuously producing soluble agglomerated food powder comprising plant-based powder, said method comprises the steps of: -providing food powder, -pre-wetting the food powder with steam in a continuous mixer, -providing a liquid binder, -feeding the pre- wetted powder via a steam nozzle into an air-drying system while spraying the liquid binder via a liquid binder nozzle onto the pre-wetted powder and injecting steam into the pre-wetted powder and at the same time to form agglomerates of the pre-wetted powder, - drying and cooling the soluble agglomerated food powder.
  • the invention relates to the use of the agglomerated food powder in a cold liquid.
  • the method of the present invention achieves the objective of the present invention in particular that the agglomerated food powder shows good reconstitution properties in cold liquid.
  • Figure 1 shows schematically the method according to the invention for agglomerated food powders including optional process units: mixing, milling, drying, cooling and sieving.
  • the method according to the invention replaces the conventional steam agglomeration unit at the top of the tower.
  • Figure 2 shows semantically the design and functionality of the method according to the invention.
  • Figure 3 shows pictures from picture analysis, analyzing how much powder stays over time on the surface of beverages.
  • the figure shows the difference between the samples 30, 60, 90 and 120 seconds after the preparation from a conventional method compared with samples prepared with the method according to the invention.
  • Figure 4 shows a chart comparing the particle size distribution of a cocoa beverage sample made according to the invention (curve 3) against a conventionally steam agglomerated sample (curve 2) and the powder before agglomeration (curve 1).
  • the method according to the invention reduces the quantity of small particles ( ⁇ 90 pm) by more than 50 %.
  • Figure 5 is a chart with the particle size distribution of the powder before agglomeration (curve 1) and the size enlargement and fines reduction effects of the present invention (curve 3 squares) compared to a standard steam process (curve 2 empty circles) for a plant protein beverage.
  • Figure 6 is a chart comparing the reconstitution performance of the agglomerated powder according to the present invention (squares) compared to agglomerated powder of a standard steam process (empty circles). The chart shows an improvement of reconstitution as measured by conductivity under stirring.
  • Figure 7 shows pictures of a beverage with the same composition, comparing the reconstitution performance of the agglomerated powder according to the present invention (2) or agglomerated with a standard steam process (1). The pictures show an improvement of reconstitution when observing the powder behavior.
  • the present invention relates a method for continuously producing soluble agglomerated food powder comprising plant-based powder said method comprises the steps of -providing food powder, -pre-wetting the food powder with steam in a continuous mixer, -providing a liquid binder, -feeding the pre-wetted powder via a steam nozzle into a air-drying system, preferably a drying or agglomeration tower and spraying the liquid binder via a liquid binder nozzle onto the pre-wetted powder while injecting steam into the pre-wetted powder and at the same time to form agglomerates of the pre-wetted powder, drying and cooling the soluble agglomerated food powder.
  • the dried and cooled agglomerated powder may be packed and stored.
  • the powder pre-wetting in a continuous mixer changes the particle surface properties, making the particles more sticky. It has further been found that the particles stick together and form pre-agglomerates.
  • the binder liquid and steam are completing the wetting process at the outlet of the steam and binder liquid nozzle. Without wishing to be bound by theory, it is believed that the particle surfaces get liquid and form liquid bridges between the individual particles in the agglomerates. These bridges are dried in the air-drying system.
  • the hardness of the agglomerates depends on the quantity of material in the inter-particle bridges. It has been found to be influenced by the type of binder material, its concentration in the liquid and the spraying quantity.
  • steam additionally contributes to the agglomeration. It has been found that only the two-step process (pre-wetting before agglomeration) and the combination of steam and binder liquid in the main agglomeration step delivers a sufficiently strong agglomerated product.
  • a product according to the invention has less than 25% of fine particles ( ⁇ 90 pm) and low fragility.
  • the continuous mixer is working at high speed, preferably at 1000 - 4000 rpm, more preferably at 2000 rpm.
  • the agglomerated powder is preferably dried with hot air in the air-drying system, preferably a drying or agglomeration tower, and then optionally further dried in a fluidized bed.
  • the cooling takes place in a fluidized bed, preferably with dry cold air.
  • the cooling is preferably to a temperature 40 - 48°C.
  • the cooling is to a temperature below 40°C.
  • the food powder comprises dairy component a cooling to a temperature below 35°C is preferred.
  • the liquid binder comprises 20 to 75 wt. % dry matter, preferably from 30 to 60 wt. % dry matter.
  • the amount of dry matter may be lower e.g. 10 wt. % but it may not be beneficial since cleaning of the nozzles would be required without any substantial improvement of the agglomeration.
  • the liquid binder comprises carbohydrates and/or protein.
  • the liquid binder is a solution in water of carbohydrates, the carbohydrates preferably being selected from the group consisting of sugars, polysaccharides or a combination thereof.
  • the liquid binder consists only of carbohydrate and/or protein, and water.
  • sugars may be fructose, glucose, maltose, sucrose, lactose, dextrose or a combination thereof.
  • the polysaccharides may be maltodextrin, polydextrose, oligofmctose, soluble fibers or other oligosaccharides or a combination thereof.
  • Sugar substitutes like e.g. sorbitol, mannitol, xylitol or combinations thereof, maltodextrins, dried glucose syrups, malt extracts, starches, trehalose, raftiline, raftilose, galactose, maltose, oligosaccharides, honey powders, and mixtures of same, and/or a non-carbohydrate based sweetener like e.g. Splenda®, Acesulfame K®, aspartame or Stevia®, and mixtures of same, may be added to the liquid binder.
  • sorbitol sorbitol, mannitol, xylitol or combinations thereof
  • maltodextrins dried glucose syrups
  • malt extracts starches, trehalose, raftiline, raftilose, galactose, maltose, oligosaccharides, honey powders, and mixtures of same
  • the liquid binder is free from emulsifiers or "dissolution agent" such as emulsifiers.
  • emulsifiers are ethoxylated mono and di-glycerides, and propylene glycol.
  • the present invention does not require special ingredients to constitute the liquid binder.
  • the prior art recommends a high intensity agglomerator delivering dense particles, whereas the present invention delivers agglomerates with an open structure while being resistant to mechanical attrition.
  • the binder liquid has the unique function of binding together the particles in the agglomeration. These particles would otherwise not stick together.
  • the excellent reconstitution properties are obtained as a result of the structure formed in the process. This make the invention particular useful for components that are not inherently soluble such as plant-based protein ingredients.
  • the liquid binder may be water only.
  • the liquid binder is a fruit concentrate or juice.
  • the agglomerated powder according to the invention may also be combined with sweeteners to form a product.
  • the final product may comprise the agglomerated powder and - a carbohydrate base sweetener selected from the group consisting of: sugars such as fructose, glucose, maltose, sucrose, lactose, dextrose, high fructose com symp or sugar substitutes like e.g.
  • sorbitol mannitol, xylitol or combinations thereof, maltodextrins, dried glucose symps, malt extracts, starches, trehalose, raftiline, raftilose, galactose, maltose, oligosaccharides, honey powders, and mixtures of same, and/or - a non-carbohydrate based sweetener like e.g. Splenda®, Acesulfame K®, aspartame or Stevia®, and mixtures of same.
  • Splenda® Acesulfame K®, aspartame or Stevia®
  • the temperature of binder liquid preferably is 5 - 60 °C when sprayed on the pre-wetter powder. Above 60°C the powder may get too humid.
  • the plant-based powder is milled to a mean particle size of 20 to 80 microns, preferably 30 to 60 microns before pre-wetting.
  • the steam to pre wet the product is 2 to 6 kg steam for 100 kg powder, preferably 3 to 4 kg steam.
  • the method according to the invention for every 100 kg of wet powder going into the air-drying system are added 5 to 16 kg of binder, preferably 8 to 14 kg. Below the 5 kg there is no advantage of the method according to the invention compared to conventional processes and above, the powder gets too humid and this would lead to nozzle blockages and fouling in the air-drying system such as the drying or agglomeration tower. The drying of the product would be difficult.
  • the agglomerated powder is dried to below 0.3 water activity aw.
  • the plant-based powder is selected from the group consisting of plant protein flours, concentrates or isolates.
  • Plant-based powders may be selected from the group consisting of powder of soy, oat, canola, faba bean, chickpea, pea, cocoa, cereal or gain flours, oat flour, rice, wheat, millet, barley or a combination thereof.
  • a further agglomeration, drying or cooling step can take place in a fluid bed supplied with a gas that is preferably air.
  • the operating parameters of the fluid bed are set according to the knowledge of the man skilled in the art.
  • the air temperature can be comprised between 60 and 150°C for the drying of the agglomerated food powder.
  • the product temperature can be comprised between 25 and 65°C.
  • the invention also relates to the soluble agglomerated food powder obtained by the method such as described above.
  • the soluble agglomerated food powder according to the invention comprises a granulometry comprised between 100 and 1500 pm and quantity of fine particles of less than 25% volume based ( ⁇ 90pm) with an optimum between 10-20% fines.
  • the granulometry can be measured by laser diffraction, within dry dispersion in air stream.
  • the soluble agglomerated food powder according to the invention has a dissolution time in water at 40°C in less than 15 s with moderate stirring without lump formation.
  • the soluble agglomerated food powder according to the invention has a wettability time in milk at 10°C of less than 45 s without stirring, without lump formation. Wettability being the time it takes for the powder to drown in the milk without stirring.
  • food shall be understood in accordance with Codex Alimentarius as any substance, whether processed, semi-processed or raw, which is intended for human consumption, and includes drink, chewing gum and any substance which has been used in the manufacture, preparation or treatment of "food” but does not include cosmetics or tobacco or substances used only as drugs.
  • composition of the present invention may further be enriched with vitamins, for example vitamins A, C, D, Bl, B2, B3, B6, B7, B9 and/or B 12, and minerals, for example, Fe, Ca, Zn.
  • vitamins for example vitamins A, C, D, Bl, B2, B3, B6, B7, B9 and/or B 12
  • minerals for example, Fe, Ca, Zn.
  • the method comprises providing an agglomeration system for continuously producing soluble agglomerated food powder comprising plant-based powder, said system comprises - an air-drying system, - a pre-wetting unit comprising a continuous mixer and a first steam nozzle for injecting steam into the continuous mixer, - a fluidization unit, - a second steam nozzle, and - a binder nozzle adapted to spray liquid binder into the powder from second steam nozzle, and injecting agglomerated powder into the air-drying system.
  • Figure 1 shows the method according to the invention for agglomerated food powders including the optional process units: mixing, milling, drying, cooling and sieving.
  • the method according to the invention replaces the conventional steam agglomeration unit at the top of the tower.
  • Fig. 2 describes the system, which is installed on top of the agglomeration tower cover. It comprises a vertical continuous mixer which allows continuous mixing of steam into the base powder stream. The pre-wetted base powder is then passing into a cone, which simply reduces the cross section from the mixer outlet to the binder nozzle inlet. The cone is jacketed and the inside surface is a membrane, which allows regular fluidization with compressed air to reduce powder fouling effects.
  • a cylindrical adaptor is installed, which is equipped with the liquid binder and atomizing gas supply pipe.
  • the supply pipe passes in a 90° angle to the outlet of the system and is equipped with an atomizing nozzle. Binder liquid is sprayed onto the powder from the center of the tube, and at the same time steam is injected from an annular opening around the powder tube.
  • a preferred embodiment of the method according to the invention uses an agglomeration system as shown in Fig. 1 and Fig. 2.
  • the agglomeration system according to the invention comprises an air-drying system in the form of a drying and agglomeration tower (10), and a pre-wetting unit (1).
  • the pre-wetting unit comprises a powder inlet (11) and a powder outlet (12), a continuous mixer (13) and a first steam nozzle (14) for injecting steam into the continuous mixer (13).
  • the agglomeration system also comprises a connection element (7) connecting the powder outlet (12) to an inlet (8), and a fluidization unit (2) comprising the inlet (8) and a outlet (16) and conveying means (15)for receiving powder from the pre-wetting unit powder outlet (12) via the connection element (7).
  • the fluidization unit is a fluidization cone comprising a cone shaped hopper (15).
  • a second steam nozzle (3) comprising a powder inlet (17) for receiving the pre-wetted powder, a steam injection orifice arranged for spraying steam onto the pre-wetted powder at a powder outlet (19).
  • a binder nozzle (4) arranged below the second steam nozzle (3), and comprising a supply pipe (6) adapted to spray liquid binder with compressed air into the powder at the powder outlet (19) of the second steam nozzle (3), and injecting agglomerated powder from outlet (19) into the air-drying system (10) in the form of an drying and agglomeration tower (10).
  • the air-drying system (10) is a drying or agglomeration tower, a fluidized bed or a combination thereof.
  • the air-drying system is a drying or agglomeration tower.
  • the drying and agglomeration tower is connected to a continuous fluidized bed for powder after drying and/or cooling.
  • the fluidization unit is a fluidization cone and the conveying means in the unit is a cone shaped hopper.
  • the powdered raw materials were dry mixed with the liquid lecithin and then milled in a high impact mill (e.g. Hosokawa Ultraplex UPZ).
  • the base powder particle size was analyzed using a Laser PSD analyzer with dry dispersion. The results shown in the table below. Table 2
  • the fine powder was then steam agglomerated using a conventional steam tower process. In this operation, 13.3 kg of steam was used for 100 kg of power. Then the second part of the base powder was agglomerated with the method according to the invention.
  • the method included a pre-agglomeration with steam (4.7 kg of steam for 100 kg of powder), followed by a second agglomeration with simultaneous steam and binder liquid addition (10.6 kg of steam and 12.91 of binder for 100 kg of powder).
  • the binder liquid was made of oligofmctose at 50% dry matter. Both agglomerated test products were dried to a similar final product moisture (water activity aw ⁇ 0.3).
  • PSD Particle Size Distribution
  • the reconstitution properties were analyzed using picture analysis, analyzing how much powder stays over time on the surface of the beverages, which a robot had prepared with cold milk.
  • the robot is using a well-defined protocol, which allows eliminating all preparation differences.
  • Figure 3 shows the difference between the samples 30, 60, 90 and 120 seconds after the preparation.
  • the sample from the method according to the invention shows a surface free of powder directly after preparation.
  • the surface of the sample manufactured with the conventional process stays covered all over the 120 seconds. Only a slight change from dry to wet powder was observed in form of a bright to darker surface. With the high cocoa content and the high quantity of polysaccharides in the recipe, the solubility of the powder is insufficient, if only steam agglomerated.
  • the food powder according to the invention shows better reconstitution and solubility than the powder prepared with the conventional process.
  • Table 4 Plant based composition with plant-based protein Powders were dry-mixed then milled before the agglomeration method. In one case the mix was agglomerated following the standard agglomeration with steam. In another case the mix was agglomerated with the method according to the invention, including a pre-agglomeration with steam, followed by a second agglomeration with simultaneous steam and binder liquid addition. Other ingredients comprise flavor, minerals, vitamins etc.

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Abstract

The present invention relates to method for continuously producing soluble agglomerated food powder comprising plant-based powder, said method comprises the steps of -providing food powder, -pre-wetting the food powder with steam in a continuous mixer, -providing a liquid binder, -feeding the prewetted powder via a steam nozzle into an air-drying system while spraying the liquid binder via a binder liquid nozzle onto the pre-wetted powder and injecting steam into the pre-wetted powder in at the same time to form agglomerates of the pre-wetted powder, - drying and cooling the soluble agglomerated food powder. The invention also relates to the method making use of an agglomeration system said system comprises - an air-drying system (10), - a pre-wetting unit (1) comprising a continuous mixer (13) and a first steam nozzle (14) for injecting steam into the continuous mixer (13), - a fluidization unit (2), - a second steam nozzle (3), and - a binder nozzle (4) adapted to spray liquid binder into the powder from second steam nozzle (3) and injecting agglomerated powder into the airdrying system. (10).

Description

CONTINUOUS BINDER LIQUID AGGLOMERATION METHOD
Field of the invention
The present invention relates to a method for continuously producing soluble agglomerated food powder, in particular soluble agglomerated food powder comprising plant-based powder and sugar. The invention also relates to the use of the soluble agglomerated food powder in cold beverages.
Background
Soluble food powders such as chocolate or malt powders are currently used for preparing beverages by mixing water or milk with these powders. However, the existing beverage dispenser devices which make use of the above outlined principle suffer the inconvenience that the beverage soluble powder is not always fully dissolved, particularly when a cold beverage is prepared by dissolving the powder with a cold diluent, either cold water or cold milk. Thus, residua of the undispersed or undissolved powder are present in the prepared beverage; this leads to a non-uniform and thus to a non-inviting appearance of the prepared beverage. Besides, since the whole dose of soluble powder is not totally dissolved, the final beverage does not present the expected taste; actually, there exists a fine tuning between the diluent volume and the powder quantity to get the best final beverage. If the dissolution is not efficient, the final beverage will not reach the expected taste. Undissolved material can also lead to a feeling of sandiness in the mouth and/or result in leftovers at the bottom of the cup when the drink is finished, with the consequent negative impression for the consumer.
Solutions have been proposed to add additives in the beverage soluble powders compositions to improve their dissolution, but these additives may have an impact on the taste of the beverages or increase the costs of production of the existing powders. For example, WO 2007/088195 proposes to add flowing agents to food powders in order to improve their cold dissolution characteristics.
EP 740 904 describes a method to improve the wettability of agglomerated cocoa and sugar containing powders which consists in exposing the powders to electromagnetic radiation. Yet, improving the wettability is not sufficient to get a good dissolution of the powders at the moment of preparation of the beverages.
In WO 2011/042356 it has been proposed to improve solubility in cold water by heating the powder just before its dissolution. But such a process can only be implemented in a beverage preparation machine specifically designed for this purpose.
It is also known that sugar boosts the dissolution of chocolate mixes. For example, WO 2012/095121 proposes coating a cocoa powder or a cocoa cake with a hydrophilic agent like sugar. Yet such a solution increases the ratio of sugar in the beverage powder. It can affect the original taste of the cocoa and it increases the rate of sugar taken by the consumer unnecessarily.
Furthermore, certain consumers wish to consume less milk or do not want to consume milk at all, for example, because of its animal origin, due to lactose intolerance or due to dairy allergies. They may also see potential environmental sustainability issues.
As a consequence, consumers seek alternatives to milk. Alternatives to milk do exist with good nutrition and taste. However, the problem discussed above also applies to these kinds of beverages.
There is a need for plant-based powder with a good solubility that can provide an alternative to milk based powders.
There is need for improving the solubility of soluble chocolate or malt beverage powders when they are dissolved with a cold diluent.
It would be advantageous to shorten the dissolution time of soluble chocolate or malt beverage powders and the reconstitution time of the beverages.
It would be advantageous to improve the solubility of soluble chocolate or malt beverage powders without using additive components in important ratios.
It would be advantageous to improve solubility of soluble chocolate beverage powders while keeping good flowability for these powders, essentially to enable a consistent dosing of the powder when used in a beverage machine dispenser.
Similar considerations apply to other plant-based powder such as plant-based protein powders.
Any reference to prior art documents in this specification is not to be considered an admission that such prior art is widely known or forms part of the common general knowledge in the field.
Object of the invention
The objective of the present invention is to improve the state of the art and in particular to provide a food powder that can be used e.g. as dairy alternative. The object of the invention is also to provide a food powder that contains cocoa, malt or other plant material a good flowability and dispersibility and which can be used in powder dispensers.
Summary of the invention
The present invention provides the improvement by the subject matter of the independent claims. The dependent claims further develop the idea of the present invention. In a first aspect, the invention relates to a method for continuously producing soluble agglomerated food powder comprising plant-based powder, said method comprises the steps of: -providing food powder, -pre-wetting the food powder with steam in a continuous mixer, -providing a liquid binder, -feeding the pre- wetted powder via a steam nozzle into an air-drying system while spraying the liquid binder via a liquid binder nozzle onto the pre-wetted powder and injecting steam into the pre-wetted powder and at the same time to form agglomerates of the pre-wetted powder, - drying and cooling the soluble agglomerated food powder.
In another aspect, the invention relates to the use of the agglomerated food powder in a cold liquid.
As used in this specification, the words “comprises”, “comprising”, and similar words, are not to be interpreted in an exclusive or exhaustive sense. In other words, they are intended to mean “including, but not limited to”.
It has been found that the method of the present invention achieves the objective of the present invention in particular that the agglomerated food powder shows good reconstitution properties in cold liquid.
Brief Description of the Drawings
Figure 1 shows schematically the method according to the invention for agglomerated food powders including optional process units: mixing, milling, drying, cooling and sieving. The method according to the invention replaces the conventional steam agglomeration unit at the top of the tower.
Figure 2 shows semantically the design and functionality of the method according to the invention.
Figure 3 shows pictures from picture analysis, analyzing how much powder stays over time on the surface of beverages. The figure shows the difference between the samples 30, 60, 90 and 120 seconds after the preparation from a conventional method compared with samples prepared with the method according to the invention.
Figure 4 shows a chart comparing the particle size distribution of a cocoa beverage sample made according to the invention (curve 3) against a conventionally steam agglomerated sample (curve 2) and the powder before agglomeration (curve 1). Compared to the conventionally agglomerated product, the method according to the invention reduces the quantity of small particles (< 90 pm) by more than 50 %.
Figure 5 is a chart with the particle size distribution of the powder before agglomeration (curve 1) and the size enlargement and fines reduction effects of the present invention (curve 3 squares) compared to a standard steam process (curve 2 empty circles) for a plant protein beverage.
Figure 6 is a chart comparing the reconstitution performance of the agglomerated powder according to the present invention (squares) compared to agglomerated powder of a standard steam process (empty circles). The chart shows an improvement of reconstitution as measured by conductivity under stirring.
Figure 7 shows pictures of a beverage with the same composition, comparing the reconstitution performance of the agglomerated powder according to the present invention (2) or agglomerated with a standard steam process (1). The pictures show an improvement of reconstitution when observing the powder behavior.
Detailed description of the invention
Consequently, the present invention relates a method for continuously producing soluble agglomerated food powder comprising plant-based powder said method comprises the steps of -providing food powder, -pre-wetting the food powder with steam in a continuous mixer, -providing a liquid binder, -feeding the pre-wetted powder via a steam nozzle into a air-drying system, preferably a drying or agglomeration tower and spraying the liquid binder via a liquid binder nozzle onto the pre-wetted powder while injecting steam into the pre-wetted powder and at the same time to form agglomerates of the pre-wetted powder, drying and cooling the soluble agglomerated food powder. The dried and cooled agglomerated powder may be packed and stored.
According to the invention it has been found that the powder pre-wetting in a continuous mixer changes the particle surface properties, making the particles more sticky. It has further been found that the particles stick together and form pre-agglomerates. Further, according to the invention the binder liquid and steam are completing the wetting process at the outlet of the steam and binder liquid nozzle. Without wishing to be bound by theory, it is believed that the particle surfaces get liquid and form liquid bridges between the individual particles in the agglomerates. These bridges are dried in the air-drying system. The hardness of the agglomerates depends on the quantity of material in the inter-particle bridges. It has been found to be influenced by the type of binder material, its concentration in the liquid and the spraying quantity. Furthermore, according to the invention by heating up the powder and adding further moisture, steam additionally contributes to the agglomeration. It has been found that only the two-step process (pre-wetting before agglomeration) and the combination of steam and binder liquid in the main agglomeration step delivers a sufficiently strong agglomerated product. Advantageously, it has been found that such a product according to the invention has less than 25% of fine particles (< 90 pm) and low fragility.
In the method according to the invention, it is preferred that the continuous mixer is working at high speed, preferably at 1000 - 4000 rpm, more preferably at 2000 rpm.
According to the present invention it has been found that with an increased binder concentration (viscosity) better agglomeration is obtained. Even with sugar binder, non-amorphous ingredients that are conventionally very challenging to agglomerate (no measurable glass transition temperature, no viscous bridge) can be agglomerated. This requires good bulking agent wettability.
In the method according to the invention the agglomerated powder is preferably dried with hot air in the air-drying system, preferably a drying or agglomeration tower, and then optionally further dried in a fluidized bed. Advantageously, the cooling takes place in a fluidized bed, preferably with dry cold air.
If the food powder comprises cocoa powder, the cooling is preferably to a temperature 40 - 48°C. For other plant-based powders such as a plant-based powder comprising plant protein it is preferred that the cooling is to a temperature below 40°C.
When the food powder comprises dairy component a cooling to a temperature below 35°C is preferred.
In a preferred embodiment of the invention, the liquid binder comprises 20 to 75 wt. % dry matter, preferably from 30 to 60 wt. % dry matter. The amount of dry matter may be lower e.g. 10 wt. % but it may not be beneficial since cleaning of the nozzles would be required without any substantial improvement of the agglomeration.
Advantageously, the liquid binder comprises carbohydrates and/or protein. Preferably, the liquid binder is a solution in water of carbohydrates, the carbohydrates preferably being selected from the group consisting of sugars, polysaccharides or a combination thereof. In a preferred embodiment of the invention the liquid binder consists only of carbohydrate and/or protein, and water.
In the present context sugars may be fructose, glucose, maltose, sucrose, lactose, dextrose or a combination thereof. The polysaccharides may be maltodextrin, polydextrose, oligofmctose, soluble fibers or other oligosaccharides or a combination thereof.
Sugar substitutes like e.g. sorbitol, mannitol, xylitol or combinations thereof, maltodextrins, dried glucose syrups, malt extracts, starches, trehalose, raftiline, raftilose, galactose, maltose, oligosaccharides, honey powders, and mixtures of same, and/or a non-carbohydrate based sweetener like e.g. Splenda®, Acesulfame K®, aspartame or Stevia®, and mixtures of same, may be added to the liquid binder.
In a preferred embodiment of the invention the liquid binder is free from emulsifiers or "dissolution agent" such as emulsifiers. Examples of such emulsifiers are ethoxylated mono and di-glycerides, and propylene glycol. The present invention does not require special ingredients to constitute the liquid binder. The prior art recommends a high intensity agglomerator delivering dense particles, whereas the present invention delivers agglomerates with an open structure while being resistant to mechanical attrition. In the present invention the binder liquid has the unique function of binding together the particles in the agglomeration. These particles would otherwise not stick together. The excellent reconstitution properties are obtained as a result of the structure formed in the process. This make the invention particular useful for components that are not inherently soluble such as plant-based protein ingredients.
In an alternative embodiment, the liquid binder may be water only.
In a further alternative embodiment, the liquid binder is a fruit concentrate or juice.
The agglomerated powder according to the invention may also be combined with sweeteners to form a product. The final product may comprise the agglomerated powder and - a carbohydrate base sweetener selected from the group consisting of: sugars such as fructose, glucose, maltose, sucrose, lactose, dextrose, high fructose com symp or sugar substitutes like e.g. sorbitol, mannitol, xylitol or combinations thereof, maltodextrins, dried glucose symps, malt extracts, starches, trehalose, raftiline, raftilose, galactose, maltose, oligosaccharides, honey powders, and mixtures of same, and/or - a non-carbohydrate based sweetener like e.g. Splenda®, Acesulfame K®, aspartame or Stevia®, and mixtures of same.
In the method for producing agglomerated food powder according to the invention, the temperature of binder liquid preferably is 5 - 60 °C when sprayed on the pre-wetter powder. Above 60°C the powder may get too humid.
In order to obtain a good mouthfeel of the final product, it is preferred that the plant-based powder is milled to a mean particle size of 20 to 80 microns, preferably 30 to 60 microns before pre-wetting.
When running the method according to the invention, preferably the steam to pre wet the product is 2 to 6 kg steam for 100 kg powder, preferably 3 to 4 kg steam.
Advantageously, in the method according to the invention for every 100 kg of wet powder going into the air-drying system are added 5 to 16 kg of binder, preferably 8 to 14 kg. Below the 5 kg there is no advantage of the method according to the invention compared to conventional processes and above, the powder gets too humid and this would lead to nozzle blockages and fouling in the air-drying system such as the drying or agglomeration tower. The drying of the product would be difficult.
To get a good shelf life of the final agglomerated powder, the agglomerated powder is dried to below 0.3 water activity aw.
Preferably, the plant-based powder is selected from the group consisting of plant protein flours, concentrates or isolates. Plant-based powders may be selected from the group consisting of powder of soy, oat, canola, faba bean, chickpea, pea, cocoa, cereal or gain flours, oat flour, rice, wheat, millet, barley or a combination thereof. Optionally a further agglomeration, drying or cooling step can take place in a fluid bed supplied with a gas that is preferably air. The operating parameters of the fluid bed are set according to the knowledge of the man skilled in the art. The air temperature can be comprised between 60 and 150°C for the drying of the agglomerated food powder. The product temperature can be comprised between 25 and 65°C.
The invention also relates to the soluble agglomerated food powder obtained by the method such as described above.
The soluble agglomerated food powder according to the invention comprises a granulometry comprised between 100 and 1500 pm and quantity of fine particles of less than 25% volume based (< 90pm) with an optimum between 10-20% fines. The granulometry can be measured by laser diffraction, within dry dispersion in air stream.
The soluble agglomerated food powder according to the invention has a dissolution time in water at 40°C in less than 15 s with moderate stirring without lump formation.
In a wettability assessment, the soluble agglomerated food powder according to the invention has a wettability time in milk at 10°C of less than 45 s without stirring, without lump formation. Wettability being the time it takes for the powder to drown in the milk without stirring.
The term “food” shall be understood in accordance with Codex Alimentarius as any substance, whether processed, semi-processed or raw, which is intended for human consumption, and includes drink, chewing gum and any substance which has been used in the manufacture, preparation or treatment of "food" but does not include cosmetics or tobacco or substances used only as drugs.
The composition of the present invention may further be enriched with vitamins, for example vitamins A, C, D, Bl, B2, B3, B6, B7, B9 and/or B 12, and minerals, for example, Fe, Ca, Zn.
In a preferred embodiment of the invention the method comprises providing an agglomeration system for continuously producing soluble agglomerated food powder comprising plant-based powder, said system comprises - an air-drying system, - a pre-wetting unit comprising a continuous mixer and a first steam nozzle for injecting steam into the continuous mixer, - a fluidization unit, - a second steam nozzle, and - a binder nozzle adapted to spray liquid binder into the powder from second steam nozzle, and injecting agglomerated powder into the air-drying system.
Those skilled in the art will understand that they can freely combine all features of the present invention disclosed herein. In particular, features described for the product of the present invention may be combined with the use of the present invention and vice versa. Further, features described for different embodiments of the present invention may be combined.
Although the invention has been described by way of example, it should be appreciated that variations and modifications may be made without departing from the scope of the invention as defined in the claims.
Furthermore, where known equivalents exist to specific features, such equivalents are incorporated as if specifically referred in this specification. Further advantages and features of the present invention are apparent from the figures and non-limiting examples.
Figure 1 shows the method according to the invention for agglomerated food powders including the optional process units: mixing, milling, drying, cooling and sieving. The method according to the invention replaces the conventional steam agglomeration unit at the top of the tower. Agglomeration method according to the invention in two step process: Fig. 2 describes the system, which is installed on top of the agglomeration tower cover. It comprises a vertical continuous mixer which allows continuous mixing of steam into the base powder stream. The pre-wetted base powder is then passing into a cone, which simply reduces the cross section from the mixer outlet to the binder nozzle inlet. The cone is jacketed and the inside surface is a membrane, which allows regular fluidization with compressed air to reduce powder fouling effects. In between the mixer and the fluidization cone, a cylindrical adaptor is installed, which is equipped with the liquid binder and atomizing gas supply pipe. The supply pipe passes in a 90° angle to the outlet of the system and is equipped with an atomizing nozzle. Binder liquid is sprayed onto the powder from the center of the tube, and at the same time steam is injected from an annular opening around the powder tube.
A preferred embodiment of the method according to the invention uses an agglomeration system as shown in Fig. 1 and Fig. 2. In the figures the agglomeration system according to the invention comprises an air-drying system in the form of a drying and agglomeration tower (10), and a pre-wetting unit (1). The pre-wetting unit comprises a powder inlet (11) and a powder outlet (12), a continuous mixer (13) and a first steam nozzle (14) for injecting steam into the continuous mixer (13). The agglomeration system also comprises a connection element (7) connecting the powder outlet (12) to an inlet (8), and a fluidization unit (2) comprising the inlet (8) and a outlet (16) and conveying means (15)for receiving powder from the pre-wetting unit powder outlet (12) via the connection element (7). In a preferred embodiment, the fluidization unit is a fluidization cone comprising a cone shaped hopper (15). Also comprised in the system according to the invention is a second steam nozzle (3) comprising a powder inlet (17) for receiving the pre-wetted powder, a steam injection orifice arranged for spraying steam onto the pre-wetted powder at a powder outlet (19). Furthermore, comprised in the agglomeration system according to the invention is a binder nozzle (4) arranged below the second steam nozzle (3), and comprising a supply pipe (6) adapted to spray liquid binder with compressed air into the powder at the powder outlet (19) of the second steam nozzle (3), and injecting agglomerated powder from outlet (19) into the air-drying system (10) in the form of an drying and agglomeration tower (10). Preferably, in the agglomeration system according to the invention the air-drying system (10) is a drying or agglomeration tower, a fluidized bed or a combination thereof.
In a particular preferred embodiment according to the invention the air-drying system is a drying or agglomeration tower. Advantageously, the drying and agglomeration tower is connected to a continuous fluidized bed for powder after drying and/or cooling.
In a preferred embodiment of the invention the fluidization unit is a fluidization cone and the conveying means in the unit is a cone shaped hopper.
Examples Example 1
Agglomeration trials were performed using a sugar reduced cocoa beverage mix, containing 30% of cocoa and 68% of carbohydrates (see table below).
Table 1
The powdered raw materials were dry mixed with the liquid lecithin and then milled in a high impact mill (e.g. Hosokawa Ultraplex UPZ). The base powder particle size was analyzed using a Laser PSD analyzer with dry dispersion. The results shown in the table below. Table 2
Malvern Powder Size Distribution (PSD) base powder properties
One part of the fine powder was then steam agglomerated using a conventional steam tower process. In this operation, 13.3 kg of steam was used for 100 kg of power. Then the second part of the base powder was agglomerated with the method according to the invention. The method included a pre-agglomeration with steam (4.7 kg of steam for 100 kg of powder), followed by a second agglomeration with simultaneous steam and binder liquid addition (10.6 kg of steam and 12.91 of binder for 100 kg of powder). The binder liquid was made of oligofmctose at 50% dry matter. Both agglomerated test products were dried to a similar final product moisture (water activity aw < 0.3).
The Particle Size Distribution (PSD) of both method samples were analyzed with the same Malver Laser method, used for the base powder analysis already. The PSD results (table 3) show a significant difference. The mean particle size of the sample from the method according to the invention is much larger, and the d50 was found to be more than twice as big and the quantity of fine particles (< 90 pm) is more than cut in half. This has the effect that the product according to the invention is significantly improved in its reconstitution properties in cold liquids and as well in its flowability properties, means in its behavior in dispensing machine. Table 3 Malvern PSD test sample properties
The reconstitution properties were analyzed using picture analysis, analyzing how much powder stays over time on the surface of the beverages, which a robot had prepared with cold milk. The robot is using a well-defined protocol, which allows eliminating all preparation differences. Figure 3 shows the difference between the samples 30, 60, 90 and 120 seconds after the preparation. The sample from the method according to the invention shows a surface free of powder directly after preparation. The surface of the sample manufactured with the conventional process stays covered all over the 120 seconds. Only a slight change from dry to wet powder was observed in form of a bright to darker surface. With the high cocoa content and the high quantity of polysaccharides in the recipe, the solubility of the powder is insufficient, if only steam agglomerated. The food powder according to the invention shows better reconstitution and solubility than the powder prepared with the conventional process.
To analyze, if the samples also differentiate in their fragility, a transport test was performed and compared the quantity of fine particles (< 90 pm), which the transport generated additionally. After a pneumatic transport of 70 m with seven 90° bends and an air velocity of 5.5 m/s, it was found that there was a clear difference between the samples. For the conventionally produced sample, the fine particle quantity increased by 10% from 53 to 63%, whereas the sample from the method according to the invention only showed an increase of 3% from 20 to 23%. A clear difference in fragility was observed.
To analyze the optional sensorial impact of the method according to the invention, the samples were subjected to sensory evaluation. Both samples passed first through an internal panel and then an external expert panel evaluation. Both panels came to the conclusion that there are no major differences between both samples. There may be some slight sensory differences depending on the type of binder component added as an additional ingredient in the final recipe. Example 2
Table 4 - Plant based composition with plant-based protein Powders were dry-mixed then milled before the agglomeration method. In one case the mix was agglomerated following the standard agglomeration with steam. In another case the mix was agglomerated with the method according to the invention, including a pre-agglomeration with steam, followed by a second agglomeration with simultaneous steam and binder liquid addition. Other ingredients comprise flavor, minerals, vitamins etc.
It was observed that the size enlargement and fines reduction effects of the present invention were significantly higher than for the standard steam process (Figure 5). As a consequence, the reconstitution performance was also significantly improved when observing the powder behavior and as measured by conductivity under stirring (Figure 6).
Table 5

Claims

Claims
1. A method for continuously producing soluble agglomerated food powder comprising plant-based powder, said method comprises the steps of -providing food powder,
-pre-wetting the food powder with steam in a continuous mixer,
-providing a liquid binder,
-feeding the pre-wetted powder via a steam nozzle into an air-drying system while spraying the liquid binder via a binder liquid nozzle onto the pre-wetted powder and injecting steam into the pre-wetted powder in at the same time to form agglomerates of the pre-wetted powder,
- drying and cooling the soluble agglomerated food powder.
2. A method for producing agglomerated food powder according to claim 1, wherein the agglomerated powder is dried with hot air in the air-drying system, and optionally further dried in a fluidized bed.
3. A method for producing agglomerated food powder according to any of the preceding claims, wherein the cooling takes place in a fluidized bed, preferably with dry cold air.
4. A method for producing agglomerated food powder according to any of the preceding claims, wherein the dry matter in the binder liquid is 20 to 75 wt. %, preferably from 30 to 60 wt. %.
5. A method for producing agglomerated powder according to any of the preceding claims, wherein a liquid binder comprises carbohydrates and/or protein.
6. A method for producing agglomerated food according to any of the preceding claims, wherein the liquid binder is a solution in water of carbohydrates, the carbohydrates preferably being selected from the group consisting of sugars, polysaccharides or a combination thereof.
7. A method for producing agglomerated food powder according to any of claims 1 to 3, wherein the binder liquid is water.
8. A method for producing agglomerated food powder according to any of the preceding claims, wherein the temperature of binder liquid is 5 to 60 °C when sprayed on the pre-wetter powder.
9. A method for producing agglomerated food powder according to any of the preceding claims, wherein plant-based powder is milled to a mean particle size of 25 to 80 microns, preferably 30 to 60 microns before pre-wetting.
10. A method for producing agglomerated food powder according to any of the preceding claims, wherein steam to pre-wet the product 2 to 6 kg steam for 100 kg powder, preferably 3 to 4 kg steam.
11. A method for producing agglomerated food powder according to any of the preceding claims, wherein for every 100 kg of wet powder going into the air drying system are added 5 to 16 kg of binder, preferably 8 to 14 kg.
12. A method for producing agglomerated food powder according to any of the preceding claims, wherein for every 100 kg of wet powder going into the air drying system are added 5 to 15 kg of steam, preferably 7.5 to 10 kg.
13. A method for producing agglomerated food according to any of the preceding claims, wherein the agglomerated powder is dried to below 0.35 water activity.
14. A method for producing agglomerated food according to any of the preceding claims, wherein the plant-based powder is plant protein selected from the group consisting of plant protein flours, protein concentrates or protein isolates.
15. A method for producing agglomerated food according to any of the preceding claims, wherein the plant-based powder is cocoa powder.
16. A method for producing agglomerated food powder according to any of the preceding claims, wherein the method comprises providing an agglomeration system for continuously producing soluble agglomerated food powder comprising plant-based powder, said system comprises - an air-drying system (10),
- a pre-wetting unit (1) comprising a continuous mixer (13) and a first steam nozzle (14) for injecting steam into the continuous mixer (13),
- a fluidization unit (2),
- a second steam nozzle (3), and - a binder nozzle (4) adapted to spray liquid binder into the powder from second steam nozzle (3) and injecting agglomerated powder into the air-drying system
(10).
EP22728118.5A 2021-05-07 2022-05-05 Continuous binder liquid agglomeration method Pending EP4333642A1 (en)

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SU1170242A1 (en) * 1984-05-29 1985-07-30 Ордена Трудового Красного Знамени Институт Тепло- И Массообмена Им.А.В.Лыкова Device for granulating and drying powder-like materials
US4640839A (en) * 1985-07-01 1987-02-03 Nestec S.A. Agglomeration process
ES2083981T3 (en) * 1990-05-18 1996-05-01 Nestle Sa PROCEDURE AND DEVICE TO TREAT A SOLUBLE POWDER MATERIAL.
EP0740904A1 (en) 1995-05-02 1996-11-06 Societe Des Produits Nestle S.A. Improving wettability of powders by microwave treatment
EP0796567A1 (en) * 1996-02-07 1997-09-24 Societe Des Produits Nestle S.A. Granular food product
EP0800860B1 (en) * 1996-04-09 2001-11-14 Bayer Ag Process and device for the agglomeration of products sensitive to hydrolysis using steam
US6291006B1 (en) * 1999-07-30 2001-09-18 The Procter & Gamble Co. Dissolution agent and process for making rapidly soluble instant beverage products
EP1815752A1 (en) 2006-02-02 2007-08-08 Nestec S.A. Improvement of cold liquid solubility of fat-containing powders
PH12012500688A1 (en) 2009-10-05 2015-05-20 Nestec Sa Method for preparing a beverage from a beverage powder and apparatus for implementing the method
CN103298355A (en) 2011-01-12 2013-09-11 卡吉尔公司 Cocoa powder compositions
WO2016124792A1 (en) * 2015-02-06 2016-08-11 Nestec S.A. Powdered beverage composition

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Free format text: CASE NUMBER: APP_58259/2024

Effective date: 20241025