Patent Application
20190153122
The present invention relates to a method of preparing a food product comprising hydrolysed starch. In particular, the present invention relates to a method of preparing a food product comprising hydrolysed starch and showing certain texture attributes, in particular a semolina texture.
Cereal products manufactured using common roller drying technologies are typically characterized by having smooth texture after reconstitution in liquids. Although such smooth texture is generally well perceived by consumers, in some geographies a more granular mouthfeel (semolina texture) is considered as a benefit.
Cereal products having semolina texture exist, but their manufacturing process present some technical challenges. For example, an ingredient providing coarse particles/pieces should be added (for example, durum wheat semolina) and such approach may limit the possibility to use cereals flours already existing in the manufacturing site. Additionally, the incorporation of the coarse particle ingredient in the required amount may often cause problems during processing (sedimentation and/or separation) that require strict process and recipe adaptations to be overcome.
Semolina texture can also be obtained by using agglomeration processes. Anyway, also this approach is not ideal due to microbiological issues which can develop in the final product.
Hence, a new process for hydrolysis of starch and preparation of cereal products having semolina texture would be advantageous. In particular, there would be a need for a process providing cereal products based on hydrolized starch and having such semolina texture, which process wouldn't require the addition of coarse particle ingredients and/or which would not request a strict adaptation of recipes and process manufacturing conditions.
Thus, an object of the present invention relates to providing a method for producing a food product comprising hydrolysed starch and having semolina texture.
In particular, it is an object of the present invention to provide a method that solves the above mentioned problems of the prior art concerned with semolina texture in foods comprising hydrolysed starch. More in particular, it is an object of the present invention to provide a method that provides food product comprising hydrolysed starch and having semolina texture.
Thus, one aspect of the invention relates to a method for producing a food product comprising hydrolysed starch, said method comprising the steps of:
A further aspect of the invention relates to a food product obtainable or obtained by the methods of the invention.
The present invention will now be described in more detail in the following.
Prior to discussing the present invention in further details, the following terms and conventions will first be defined:
The term ‘degrees C.’ refers to degrees Celsius.
The term “starch” as used herein refers to the polysaccharide macromolecules used for energy storage by most plants. It consists of a large number of glucose units joined by glycosidic bonds. The two high-molecular weight components of starch are amylose and amylopectin. Starch is found for example in cereals, tubers and legumes. Examples of tubers include potatoes, sweet potatoes, cassava, yams etc. Examples of legumes include beans (such as pinto, red, navy), peas, lentils, chickpeas, peanuts etc. When the term “starch” is used in the context of the present invention, it may indicate starch from one plant origin or a mixture of starches from different plant origins.
The term “cereal” as used herein refers to any grass cultivated for the edible components of its grain. Examples of cereal are wheat, rice, maize, barley, rye, oats, buckwheat, millet, quinoa, sorghum et cetera.
The term “food product” as used herein refers to a finished product suitable for human consumption and/or to a intermediate preparation which is meant to deliver a finished product after being subject to additional processing step(s), comprising a heat treatment. Specific non-limiting examples of finished food products are biscuits, wafers, cereals (breakfast and infant), especially cereals for porridge, bread, bakery products, pizza, cereal milk drink, baby food and the like. In particular, finished food products may be cereal (like Infant or all family Cereals) for porridge or cereals for Cereal Milk Drink. Specific non-limiting examples of preparation which are meant to deliver a finished product after being subject to additional processing steps are batters, doughs, slurries and the like.
Within the context of the present invention, “Infant cereal” products identifies compositions containing cereals to be administered to infants and identifies two main categories: complete cereal product which need to be reconstituted in water as they already contain all the necessary nutrients to be delivered with the meal; and standard cereal product which are meant to be reconstituted with milk (Whole or skimmed), infant formula, follow-on formula and/or GUMs.
Within the context of the present invention, the term “all family cereals” identifies compositions containing cereals to be consumed by children and adults. For example, all family cereals are reconstituted in milk (whole or skimmed) and consumed in the format of a porridge.
The term “gelatinization” as used herein refers to the process of swelling and opening of starch granules which are semi-crystalline in the native state, where the intermolecular bonds of starch molecules in a starch granule are broken, thus making the crystallinity disappear and leading to the binding of water and the irreversible dissolving of the starch granule macromolecules, i.e amylose and amylopectin, in water. The determination of the gelatinization temperature is well known to the skilled person, and may be performed by e.g. the Kofler hot stage microscopy (see further Table 1 and notes), or for example by Differential Scanning calorimetry (DSC).
The term “amylolytic enzymes” as used herein refers to any enzyme capable of converting starch into dextrins and sugar (mono- or disaccharides). Examples of amylolytic enzymes include amylases and pullulanase. Examples of amylases include alpha-amylases, beta-amylases, gamma-amylases.
The expression “fat” or “fats” or “fat source” or “lipid” or “lipid source” or “oil” or “oils” in the context of the present invention indicates an edible solid or liquid fat or mixtures thereof. Not limiting categories of fats are those from animal, microbial, algal or vegetable origins. Non limiting examples of fats which could be used according to the present invention are: fish oil, cocoa butter, cocoa butter equivalents (CBE), cocoa butter substitutes (CBS), vegetable oils (for example rapeseed oil, palm oil, corn oil, soy oil, coconut oil and/or sunflower oil) and butter oils amongst others.
The term “semolina texture” as used herein indicates a sensory attribute of the product obtained according to the present invention once such product is reconstituted (in water, milk or as above defined). The “semolina” attribute is defined as the “quantity, size and/or hardness of round particle perceived in mouth” and may be rated by a trained sensory panel on a scale between 0 and 10.
In the context of the present invention, one reference product having semolina texture has been used to train the panel for assessing this attribute; the product may prepared as follows:
This reference is at 8.5 of intensity for the semolina sensory attribute of quantity of round particles on 10 scale points,
This reference is at 2.5 of intensity for the semolina attribute of size of round particles on 10 scale points.
This reference is at 5 of intensity for the semolina attribute of hardness of round particles on 10 scale points.
The present invention is based on the surprising finding that implementation of the method of the invention yields a food product comprising hydrolysed starch and having a semolina texture as compared to a smooth mouthfeel provided by the product obtained via the conventional process.
It is believed that by the method of the invention semolina texture is delivered in the food product comprising hydrolysed starch thanks to the particular set up in terms of ingredients which are present in the mixture and the operating conditions employed.
It was in fact observed that the presence of fats is necessary to ensure that semolina texture is obtained in the food product. As demonstrated in Example 3 and 4, in the absence of fats the semolina texture attribute is not obtained in the product. Similarly, it was concluded that the high shear mixing conditions are necessary to ensure that semolina texture is obtained in the food product. As demonstrated in Example 3, in the absence of an equipment which can deliver high shear mixing during performance of step e), the semolina texture attribute is not obtained in the food product.
Without wishing to be bound by theory, is it thus believed that during the gelatinization process of starch, the high shear mixing conditions allow some specific arrangements of starch and lipids or interaction between the starch molecules and the lipids present in the mixture. This would induce the formation of the coarse particles during rehydration, which imparts a semolina texture to the finished food product.
It is in fact believed that high shear increases fat dispersion on the cereal/starch matrix and the higher the fat droplet dispersion, the smaller the fat droplets and the larger will be the contact surface of oil with the liquid during reconstitution. Accordingly, during reconstitution the imbibition of liquid in the cereals/starch is be slowed down and slow water penetration (or imbibition) may enhance semolina texture.
Thus, one aspect of the invention relates to a method for producing a food product comprising hydrolysed starch, said method comprising the steps of:
In one embodiment of the present invention, a method for producing a food product comprising hydrolysed starch is provided which, in addition to being endowed with semolina texture, is also characterised by comprising lower amounts of maltose, as compared to the product obtained via conventional hydrolysis process.
In such embodiment, the invention relates to a method for producing a food product comprising hydrolysed starch, said method comprising the steps of:
The method of the invention involves providing a starting material which comprises starch.
In one embodiment, the starting material comprises both starch and at least one amylolytic enzyme.
Some embodiments relate to methods according to the invention wherein the starting material is a plant preparation, such as a preparation of that part of the plant which contains the majority of the plant's starch storage granules. In some embodiments such preparations may also include other parts of the plant, such as stems, leaves etc. In some embodiment, such plant preparations also comprise at least one amylolytic enzyme.
In particular embodiments, the starting material is a dry plant preparation, such as a flour. Thus, the starting material may be selected from a flour of one or more grains, such as a flour selected from wheat flour, rice flour, maize flour, barley flour, rye flour, oat flour, buckwheat flour, millet flour, quinoa flour, sorghum flour; a flour made from one or more tubers, such as potato, cassava; a flour made from legumes such as pea flour; or combinations thereof.
The term dry as used herein means comprising water in the range from 0.01 to 20% w/w such as from 0.01 to 16% w/w, 0.01 to 15% w/w, 0.01 to 12% w/w, 0.01 to 8% w/w, 0.01 to 5% w/w, 0.01 to 3% w/w, w/w such as 0.01 to 0.5% w/w %, or for example being essentially free from water. For example, wheat flour may contain up to 15% moisture (w/w), such as from 12 to 15% w/w, 12 to 14% w/w or 12 to 13% w/w, and is considered a dry plant preparation.
The term flour as used herein refers to the product of milling. The particle size or particle size distribution of the flour is not considered to be critical for the method. Plant preparations in the form of flours which are suitable as starting material for production of hydrolysed starch are known in the art, and selection of such is also within the skill of the person skilled in the art.
In one embodiment of the present invention, the starting material for the method of the invention comprises both starch and at least one amylolytic enzymes. In this embodiment, the at least one amylolytic enzymes present in the starting material may be endogenous amylolytic enzymes. In other words, the starting material may comprise amylolytic enzymes which have not been added by human intervention, but rather have been co-extracted together with the starch (granules) from the plant material, i.e. endogenous amylolytic enzymes. Examples of endogenous amylolytic enzymes include alpha-amylases, and beta-amylases and gamma amylases.
For example, in the specific case of wheat, endogenous amylolytic enzymes, in particular endogenous amylases, are typically inactivated above 60-70 degrees C. Inactivation temperature of endogenous enzymes in other cereals could be determined according to procedure well known to the skilled person, for example by using commercial kits to determine enzyme activity under different conditions.
Examples of commercially available kits which may be used are Betamyl method (K-beta3 10/10) available from Megazyme™ (beta amylase activity), and Phadebas® (alpha amylase activity).
The invention in one embodiment relates to a method according to the invention wherein in step d) is the temperature of the mixture of step c) is adjusted to a temperature which leads to gelatinization of the starch and inactivation of endogenous amylolytic enzymes in said mixture. Such temperature adjustment is simultaneous to subjecting the mixture of step c) to high shear mixing as described in step e).
The method of the invention comprises providing water and mixing with the starting material. Enzymatic hydrolysis of starch requires the presence of water. If the starting material is provided in dry form, such as for example a dry plant preparation, such as for example a plant flour, water may be provided by one or more of steam injection, addition of water, the provision of an aqueous further ingredient, provision of an aqueous solution of at least one (further) amylolytic enzyme or combinations thereof.
If the starting material is not in dry form, but comprises more than 20% water w/w, or for example more than 15% water w/w, the water may be considered to be at least partially provided by the starting material. In some embodiments, further water may also be provided, for example by one or more of steam injection, addition of water, the provision of an aqueous further ingredient, provision of an aqueous solution of at least one (further) amylolytic enzyme or combinations thereof.
In particular embodiments, the provision of water comprises providing water in the form of steam. In particular embodiments, water in the form of steam is provided by way of steam injection, such as direct steam injection. In other embodiments, water in the form of steam is provided by way of steam infusion (where ingredients are sprayed in a steam atmosphere). Direct steam injection has the advantage of rapidly heating the mixture of starting material, the optionally water provided from above-mentioned other sources, the at least one (further) amylolytic enzyme, the fat and any optional further ingredients, at the same time as water is added.
Direct steam injection may be achieved by any suitable means, and the selection of such a means is within the skill of a person of ordinary skill in the art.
In one embodiment, when the provision of water is at least partially in the form of steam, such steam provision may occurr simultaneously to steps d) and e).
Some embodiments relate to the method according to invention, wherein said mixture (step c) has a total solids content in the range of 20 to 70% w/w, such as 30 to 70% w/w, such as 35 to 70% w/w, such as such as 40 to 70% w/w, such as 45 to 70%, such as 50 to 70% w/w, such as 55 to 70%, such as 40 to 65% w/w.
Some embodiments relate to the method according to invention, wherein said mixture (step c) has a total solids content in the range of 20 to 60% w/w, such as 30 to 60% w/w, such as 35 to 60% w/w, such as such as 40 to 60% w/w, such as 45 to 60%, such as 50 to 60% w/w, such as 55 to 60%; or for example from 20 to 55% w/w, 20 to 50% w/w, 20 to 40% w/w; or for example 30 to 50% w/w, or 30 to 40% w/w.
The method of the invention comprises a step wherein at least one amylolytic enzyme is added to the starting material and mixed together with the starting material and fats. Thus, in step b) an amylolytic enzyme is provided and all ingredients mixed in step c).
The at least one amylolytic enzyme provided in step b) may be any suitable amylolytic enzyme, for example an amylase (such as alpha-amylase and/or beta-amylase) and/or pullalanase. In particular embodiments, the at least one further amylolytic enzyme is one or more of an alpha amylase and a beta amylase. The invention in some embodiments relates to a method according to the invention wherein said at least one amylolytic enzyme provided in step b) comprises or consists of amylase not endogenous to the provided starting material.
The selection of the at least one amylolytic enzyme provided in step b) may depend on the gelatinization temperature of the starch present in the starting material. Thus, in particular embodiments, this at least one amylolytic enzyme which is provided in step b) is active at or above the temperature to which the mixture is adjusted in step d) (see further below gelatinization temperature).
In yet further particular embodiments, the at least one amylolytic enzyme provided in step b) has a temperature optimum at or above the temperature to which the temperature is adjusted in step d). The temperature optimum of an enzyme is a certain temperature or range of temperatures where an enzyme's catalytic activity is at its greatest.
As mentioned above, the at least one amylolytic enzyme provided in step b) may be provided as an aqueous solution.
Selecting an at least one amylolytic enzyme provided in step b) which is active, or for example has a temperature optimum, at a temperature in or above the gelatinization temperature range of the starch present in the mixture, ensures that hydrolysis of the starch will take place and will be due to the selected enzymes.
Amylolytic enzymes are commercially available from several distributors, for example from DuPont, Novozymes, DSM, BioCatalysts.
In one embodiment, in step b) an amylolytic enzyme is provided, which is in addition to the amylolytic provided in step a), and all ingredients mixed in step c).
In some embodiments, the at least one further amylolytic enzyme is provided in addition to an endogenous amylolytic enzyme provided in step a).
According to the present invention, fats are provided in step b).
In one embodiment, fat provided in step b) is added in an amount comprised between 1 and 40%, for example between 1 and 30%, for example between 2 and 25%, for example between 7 and 20% w/w, for example between 7 and 18% w/w, for example between 7 and 15% w/w of the solid composition.
In another embodiment, fat provided in step b) is added in an amount comprised between 1 and 40%, for example between 1 and 30%, for example between 2 and 25%, for example between 5 and 20% w/w, for example between 5 and 18% w/w, for example between 5 and 15% w/w of the solid composition.
In one embodiment, fat is an edible solid or liquid fat or mixtures thereof.
In one embodiment, fat is selected in the group consisting of: vegetable oils (for example rapeseed oil, palm oil, corn oil, soy oil, coconut oil and/or sunflower oil), butter and butter oils or mixtures thereof.
In one embodiment, fats such as oils are provided in step b). In a further embodiment, fats such as oils are provided in step b) in an amount comprised between 2 and 25%, for example between 7 and 20% w/w of the solid composition.
As above mentioned, it is believed that the presence of fats at the time of starch gelatinization under high shear mixing is key for obtaining the semolina texture which characterizes the food product according to the method of the invention.
In some embodiments of the invention, one or more other ingredients are included. The one or more further ingredients may be any ingredient suitable for a food. In particular embodiments, the one or more other ingredients added in step b) are not negatively affected by the temperature and high shear mixing of step d) and e). Examples of one or more other ingredients may be protein or amino acid sources, carbohydrate sources such as sugars and/or pre-biotics, fibers, dietary fibers, minerals, vitamins and the like.
In some embodiments of the method, the food product obtained by a method of the invention is itself a finished food product. In such embodiments, at least one other ingredient is provided in step b), such as one or more ingredients such as for example protein or amino acid sources, carbohydrate sources such as sugars and/or pre-biotics, fibers, dietary fibers, minerals, vegetable ingredients, fruit ingredients, milk based ingredients and vitamins.
The method of the invention comprises a step of mixing the starting material of step a) and the ingredients of step b).
It is not believed that this mixing is critical, and thus may be done in any suitable manner. The selection of a method of mixing is within the skill of a person skilled in the art.
In some embodiments of the method according to the invention, the step c) of mixing the starting material of step a) and the ingredients of step b), is performed prior to the step d). This means that the starting material and ingredients are mixed prior to the adjustment of temperature which takes place in step d). This is referred to as “pre-mixing”. In case ingredients are pre-mixed as above described, it is also not believed that the mixing order prior to the performance of step d) is critical.
In one embodiment, mixing of the starting material of step a) and the remaining ingredients of step b) (fat and other optional ingredients) is performed prior to the provision of the amylolytic enzyme of step b), so that mixing of all the ingredients of step a) and b) provided for in step c) doesn't not occur at the same time.
In another embodiment, mixing of the starting material of step a) and of the ingredients of step b) is performed simultaneosuly, so that mixing of all the ingredients of step a) and b) provided for in step c) occurs at the same time.
However, premixing of ingredients is not necessary: dry ingredients and water can be directly fed inside the high shear mixer, such as a Ring Layer Mixer.
In other, particular embodiments, the step c) of mixing takes place simultaneously with step d). For example, the starting material of step a) and the ingredients of step b) may be fed to a container, in which heating is performed and in which, at the same time, mixing takes place.
In one embodiment, steps c), d) and e) are performed in a ring layer mixer, simultaneously.
The method of the invention comprises a step d) where the temperature of the mixture obtained in step c) is adjusted to a temperature which leads to the gelatinization of the starch in said mixture. The temperature is adjusted simultaneously with the high shear mixing of the mixture.
The gelatinizing temperature refers to the temperature (or temperature range) at which a starch gelatinizes in excess water (for example total solid not higher than 20%). Different species of plants yield starches which may have different gelatinization temperatures, and these are well-known in the art. Gelatinization temperature ranges for some starches, are given below in Table 1 by way of example.
Sorghum
Accordingly, depending on the starch type (or types) in the starting material, the temperature is adjusted to the appropriate temperature which will result in gelatinization of the starch. In one embodiment, depending on the starch type (or types) in the starting material, the temperature is adjusted to the appropriate temperature which will result in gelatinization in at least a portion of the starch.
The gelatinizing temperatures of different starches are well known in the art, and the selection of the appropriate gelatinizing temperature is within the skill of a person knowledgeable in the field. For example, gelatinization temperature may be determined by Kofler hot stage microscopy (see also Table 1).
In some embodiments, the extent of gelatinization of the starch is such that at least half of the starch is gelatinized, such as at least 70% w/w, 80% w/w, 90% w/w, or may be essentially complete, that is, essentially all the starch in the mixture is gelatinized.
In some embodiments, the temperature in step d) is adjusted to a temperature above starch gelatinization, for example above 70 degrees C., for example in the range from 70 to 95 degrees C., such as from 70-90 degrees C., or 70-85 degrees, or for example from 75 to 95 degrees, such as from 80 to 95 or 85 to 95 degrees. This temperature range will encompasse the temperature optimum of the at least one amylolytic enzyme added.
In some embodiments, the temperature in step d) is adjusted to a temperature above starch gelatinization and endogenous amylolytic enzyme inactivation, for example above 70 degrees C., for example in the range from 70 to 95 degrees C., such as from 70-90 degrees C., or 70-85 degrees, or for example from 75 to 95 degrees, such as from 80 to 95 or 85 to 95 degrees. This temperature range will ensure the inactivation of most endogenous amylolytic enzymes (e.g. endogenous amylases), while encompassing the temperature optimum of the at least one further amylolytic enzyme. In one embodiment, this temperature range will ensure the inactivation of wheat endogenous amylolytic enzymes (e.g. endogenous amylases), while encompassing the temperature optimum of the at least one further amylolytic enzyme.
In some embodiments, the temperature in step d) is adjusted to a temperature equal or higher than 55 deg C., for example ranging from 55 to 95 deg C., for example ranging from 60 to 95 deg C., for example ranging from 60 to 90 degrees C., such as from 60- to 85 degrees C., or 65 to 85 degrees, or for example ranging from 70 to 95 degrees C., such as from 70- to 90 degrees C., or 70 to 85 degrees, or for example from 75 to 95 degrees, such as from 80 to 95 or 85 to 95 degrees.
In some embodiments of the method according to the invention, a mixture of different starches may be present in the mixture of step c). In such cases, the temperature selected in d) may be the highest gelatinization temperature of the starches present.
In particular embodiments, the step d) (adjusting the temperature of the mixture from step c) to a temperature which leads to gelatinization of the starch in said mixture) is performed by direct steam injection.
The method of the invention comprises a step of subjecting the mixture of step c) to high shear mixing, for example by use of a high shear mixer.
The high shear mixing may be for a time period of 0.5 seconds to 10 minutes, such as 1 second to 10 minutes, such as from 1 second to 5 minutes, such as 1 second to 3 minutes, such as 1 second to 120 seconds, such as 1 second to 90 seconds, such as 1 second to 60 seconds.
The high shear mixing may be such that the mixture is homogenized within a time period of 1 second to 10 minutes, such as from 1 second to 5 minutes, such as 1 second to 3 minutes, such as 1 second to 120 seconds, such as 1 second to 90 seconds, such as 1 second to 60 seconds.
In particular embodiments, the high shear mixing is such that the mixture is homogenized within a time period of 1 second to 50 seconds, such as 1 second to seconds, 1 second to 30 seconds.
In this context, homogenized means where the starch granules are swollen and dispersed into the media.
Said high shear mixing is performed simultaneously with the adjusting of the temperature to a gelatinizing temperature (step c), discussed above).
Shear forces are unaligned forces pushing one part of the body in one direction, and another part of the body in the opposite direction.
In some embodiments, the invention relates to methods of the invention wherein said high shear mixing in step e) may be achieved by using a high shear mixer. High shear mixers disperse an ingredient or ingredient mix into a main continuous phase, for example a solid, semi-liquid or liquid phase. Typically, a mobile rotor or impeller is used together with a stationary component known as a stator together to create high shear. Thus, a high shear mixer may be defined as a mixer comprising a rotor and at least one stator. Examples of high shear mixers are well known in the art, and include for example ring layer mixers. Non-limiting examples of high shear mixers according to the present invention are: ring layer mixer, homogenizer, paddle mixer, pin mixer, pelletizer, granulator and high shear pump.
In one embodiment of the present invention, the high shear mixing in step e) is not an extruder. In one embodiment, the high shear mixer according to the present invention is not an extruder.
The term high shear mixing as used herein may be defined as the mixing which achieves such shear as may be achieved by using a Ring Layer Mixer, for example under the conditions described in Example 2.
Where the temperature adjustment is achieved using direct steam injection, the heat adjustment together with high shear mixing leads to gelatinization occurring within a very short period of time (milliseconds to seconds, such as from 0.5 seconds to 60 seconds), essentially instantaneously.
Any apparatus which can achieve high shear mixing as well as allow for simultaneous temperature adjustment (in particular to relevant gelatinization temperatures) may be used.
Particular embodiments of the invention relate to methods according to the invention wherein the high shear mixing step e) is achieved by use of a high shear mixer, in particular a ring layer mixer.
A ring layer mixer delivers high peripheral speeds. The resulting centrifugal force brings the product outwards into a ring layer on the vessel side wall. The high speed difference between the rotating agitator and the mixing drum, combined with the use of different mixing elements ensures a high shear mixing.
Direct steam injection is simple to implement when using a ring layer mixer, which is a further advantage of using a ring layer mixer.
Some embodiments relate to the method according to the invention, wherein steps c) to e) are performed in a Ring Layer Mixer. Other embodiments relate to method according to the invention where steps c) up to and including at least a part of step f) are performed in a Ring Layer Mixer
Particular embodiments relate to methods of the invention wherein the steps a) to e) are performed in a Ring Layer Mixer. As mentioned below, other embodiments relate to methods of the invention wherein steps a to c) are performed prior to use of the ring layer mixer (i.e., pre-mixing step) and steps d) to e) are performed in the ring layer mixer.
Other particular embodiments relate to the method of the invention where direct steam injection is used to adjust the temperature in step d) and ring layer mixer is used for high shear mixing of step e).
It is believed that the generation of high shear forces during starch gelatinization in the presence of fats is essential to deliver the semolina texture in the food product prepared by the method of the present invention.
As above reported, it was observed that the high shear mixing conditions are necessary to ensure that semolina texture is obtained in the food product. As demonstrated in Example 3, in the absence of an equipment which can deliver high shear mixing during performance of step e) (for example a ring layer mixer), the semolina texture attribute is not obtained in the food product.
The method according to the invention comprises the step f) of incubating the mixture obtained by high shear mixing from step e) such that the desired degree of hydrolysis is achieved.
This incubation step relates to a step when the mixture from step e) is kept at a certain temperature, for a certain period of time. This incubation allows the enzymes, in particular the at least one (further) amylolytic enzyme of step b) to act. In some embodiments, mixing may take place in the incubation period. The mixing avoids sedimentation, and/or facilitates an even and stable temperature profile. In particular embodiments, the mixing in step f) is not high shear mixing.
The temperature may be selected to provide optimal performance of the at least one (further) amylolytic enzyme, such as amylase, from step b). The selection of the conditions for said incubation (temperature, time, mixing speeds) will depend on the desired degree of hydrolysis of the starch in the mixture, and is within the skill of the person with ordinary skill in the field. The desired degree of hydrolysis is determined for example by desired characteristics of the food product. For example, if higher viscosity is desired, then extensive starch hydrolysis may not be necessary.
Some embodiments relate to the method according to the invention, wherein the incubation of step f) is performed at a temperature in a range selected such that the at least one (further) amylolytic enzyme of step b) has an optimal activity.
The temperature at which the at least one (further) amylolytic enzyme of step b) has optimal activity may be determined by routine investigation, but this information is also typically provided by the supplier of the enzyme. See also under the heading “amylolytic enzymes addition in step b)” for further discussion of selection of temperature.
In some embodiments, the incubation of step f) is performed at a temperature in the range of from 70 to 95 degrees C., such as from 70 to 90 degrees C., for example from 70 to 85 degrees C., or for example from 75 to 95 degrees C., such as from 75 to 80 degrees C.; for a period of time in the range from 1 minute to 24 hours, such as 1 minute to 12 hours, such as from 1 minute to 10 hours, such as from 1 minute to 8 hours, such as 1 minute to 7 hours, such as 1 minute to 6 hours, such as 1 minute to 5 hours, such as 1 minute to 4.5 hrs, such as 1 minute to 4 hours, such as 1 minute to 3.5 hours, such as 1 minute to 3 hours, such as 1 minute to 2.5 hours, such as 1 minute to 120 minutes, such as from 2 minutes to 80 minutes, such as from 10 minutes to 80 minutes, 10 to 60 minutes; or for example from 1 minute to 10 minutes, 1 to 8 minutes, or 1 to 5 minutes, or for example from 2 minutes to 10 minutes.
The process comprises a drying step j), for example roller drying, and milling in order to produce a dried product which may be reconstituted before use.
Drying is defined as the application of heat under controlled conditions, to remove the water present in liquid or semi-liquid foods and to yield solid products.
In one embodiment such step j) is a roller drying step. The principle of roller drying process (or drum drying) is that a thin film of material is applied to the smooth surface of a continuously rotating, stema heated metal drum. The film of the drying material is continuously scraped off by a stationary knife located opposite to the point of application of the liquid or semi-liquid material. The dryer consists of a single drum or a pair of drums with or without satellite rollers.
Roller drying is a conventional drying technique in the art. The person skilled in the art will be able to select appropriate roller drying temperature and speed for the preparation of food products according to the method of the invention.
In such embodiment, the product obtained may be a finished infant or all family cereal product to be consumed in the format of a porridge after reconstitution as above described.
Yet further embodiments relate to the method according to the invention, further comprising the step g) additional heat treatment of the mixture which was obtained by high shear mixing according to steps a) to f).
The purpose of the heat treatment in step g) is to reduce microbiological load of the product, as well as to inactivate enzymes, including the at least one (further) amylolytic enzyme from step b). Thus, the temperature and period of time of heat treatment of step g) will be selected in order to fulfil these two requirements and may be performed by any suitable means. It is considered to be within the skill of the person with knowledge in the field to select the means as well as appropriate temperature and time. The heat treatment of step g) may be for example performed by bringing the temperature of the homogenized mixture to a temperature in the range from 90 to 170 degrees Celsius, for a period of time from 2 seconds to 5 minutes.
In particular embodiments, the temperature in step g) is brought to a temperature in the range from 100 to 140 degrees C. for a period of time of 4 seconds to 60 seconds.
In some particular embodiments, the heat treatment of step g) is performed by direct steam injection.
In one embodiment, the heat treatment of step g) may be performed after step e), such as directly after step e). In such embodiment of the invention, steps c) up to and including at least a part of step f) are performed in a Ring Layer Mixer.
The heat treatment of step g) may be performed before step j), such as directly before step j).
The method of the invention may further comprise one or more further steps wherein one or more yet further ingredients are added to mixture. These ingredients may be any ingredient suitable for the food product being manufactured. In particular, ingredients which are desired to be included in the final food product, but which may be negatively affected by for example the heat and-or the high shear mixing of steps c) and d), may be advantageously added at a point after these said steps. Examples of ingredients which may be negatively affected include heat sensitive nutrients such as heat-sensitive vitamins, and-or probiotics. For example, one or more yet further ingredients may be added after step e), for example after step e) and before step f), or for example immediately after step e), or for example immediately after step e) and before step f). In some embodiments the yet further one or more ingredients may be added after step f), such as immediately after step f) and before any further steps. The person skilled in the art will recognize the requirements of conventional ingredients, including heat-sensitive nutrients and can determine at which point these may be added.
In some embodiments, the method of the invention further comprises a step h) of cooling the mixture obtained by previous step. The cooling may be effected by any suitable means, and may be for example to a temperature in the range from −20 degrees C. to 18 degrees C., such as for example 0 to 10 degrees C., such as 0 to 5 degrees C.
The invention relates in a second aspect to a food product obtainable by a method according to the invention. In one embodiment of this aspect, the invention relates to a product obtained by a method according to the invention.
The food product according to the invention may be described as comprising hydrolysed starch and having a semolina texture within the meaning of the present invention.
In particular embodiments, the invention relates to a product according to the invention wherein the semolina attribute as scored according to the method described is equal or higher than 1, in particular equal or higher than 2.
A finished food product means a food product as sold to the consumer. Non limiting examples of final food products include cereals, cereal milk drinks, and the like.
It should be noted that embodiments and features described in the context of one of the aspects of the present invention also apply to the other aspects of the invention.
All patent and non-patent references cited in the present application, are hereby incorporated by reference in their entirety.
The invention will now be described in further details in the following non-limiting examples.
In this example of a conventional in-line hydrolysis process (where the hydrolysis is performed in the line of production of a finished food product), a wheat flour, water, fat and optionally other ingredients (e.g. sucrose, etc.) are mixed in a preparation tank. The slurry is then pumped into tubes. The amylase solution is injected in-line just before the static mixer where steam is injected to reach the optimum temperature for the enzyme activity (for example above 70 degrees C., such as from 70 to 95 degrees C., for example 70 to 90 degrees C., such as from 70 to 85 degrees C., for example from 75-85 degrees C.). The amylase can also be added in the initial liquid batch preparation tank. The slurry is then further processed at this optimum temperature for a residence time (corresponding to the incubation of step f), depending on the extent of hydrolysis required (e.g. 2 to 10 minutes), before final heat treatment for hygienic reasons and enzymes inactivation (step g), for example: above 120° C. for 20 sec). The slurry (comprising around 45% w/w solids) is then subject to a roller drying treatment (corresponding to step j)) according to the process of the invention) to provide the finished food product. Roller drying treatment is performed in a mono-cylinder roller dryer at a temperature comprised between 185 and 190 deg C. and at speed comprised between 4 and 5 rpm. The finished food product may be then milled and packed for commercial use.
The method of the invention may be incorporated as an in-line method of hydrolysis in method for producing a finished food product.
In one example of the method according to the invention, the conventional steps of “enzyme dosing-steam injection-static mixer” as above described in Example 1 are replaced by a Ring Layer Mixer (RLM).
A RLM with 10 litre capacity was used, with speed set to 2000 rpm. The RLM had two inlets, wherein the first inlet was used to introduce ingredients' mixture and enzyme solution. Steam was injected via the second inlet. The steam was superheated, and used to bring the temperature of the flour and enzyme mix in the tank to a temperature of 75 to 80 degrees Celsius, as measured by a probe. The ingredient mixture was thus almost instantaneously both heated and homogenized. The resulting treated mixture was transported out of the ring layer mixer to holding tubes. The treated mixture was incubated at 75 degrees C. for a time longer than 2 minutes to allow the further hydrolysis by the enzymes.
The key characteristic of this high shear mixer is that it allows instantaneous and simultaneous flour gelatinization and mixing under high shear with steam and the other added ingredients, especially the fats.
The slurry is then subject to a roller drying treatment as above described in Example 1. The finished product can then be milled and packed for commercial use.
See a simplified process diagram in
Sensory and Texture attributes were evaluated for porridge obtained by reconstitution of cereal products of the same recipe (see Table 1 below) but prepared under two different manufacturing set ups (with or without ring layer mixer as described above in Example 2) or 1) respectively)
Roller-dried prototypes, reconstituted into a cereal porridge, were assessed by an external trained sensory panel of 12 assessors. Monadic profiles were conducted on product appearance, flavour/aroma and texture without repetition. Results are reported in Table 2 (as well as graphically represented in
Comparison of Sensory and Texture Attributes of a Porridge Based on a Cereal Product not Comprising Fats and Prepared with the Method of the Invention
Texture attributes were evaluated for porridge obtained by reconstitution of cereal products of the same recipe (see Table 3 below) but prepared under two different manufacturing set ups (with or without ring layer mixer as described above in Example 2) or 1) respectively).
Roller-dried prototypes, reconstituted into a cereal porridge, were assessed by an external trained sensory panel of 12 assessors. Monadic profiles were conducted on product appearance, flavour/aroma and texture without repetition. Under the conditions tested in Example 4, no Semolina texture was observed for any of the sample tested demonstrating the unexpected and critical role played by the presence of fats in the composition when the process of the invention is used.
The analysis were performed on a Rapid Visco Analyser equipment (RVA, Newport Scientific):
From each of the RVA curves, maximal viscosity (ViscoMax, mPa·s) and time to reach this maximal viscosity (Tvmax, min) were extracted. The maximal viscosity represents the viscosity of the pap once fully reconstituted. Tvmax represents the time needed for the powder to be fully reconstituted.
The graph in
From the results it can also be observed that at higher values for Tvmax (which is believed to be correlated with the kinetic of reconstitution), the semolina texture becomes more prominent. Accordingly, without wishing to be bound by theory, it is believed that a slower/more difficult imbibition of the particles with liquid may be associated to the presence of the coarse particles providing semolina texture in the product.
| Number | Date | Country | Kind |
|---|---|---|---|
| 16179668.5 | Jul 2016 | EP | regional |
| 16204620.5 | Dec 2016 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2017/067855 | 7/14/2017 | WO | 00 |
