Patent Application
20110052778
This application claims priority from European Patent Application Number EP 09168923, filed Aug. 28, 2009, which is hereby incorporated herein by reference in its entirety.
The present disclosure relates to aerated food products and, in particular, microcellular aerated food products.
Incorporation of gas cells, also known as aeration, impacts textural properties of food products. Generally, their texture is lighter than the texture of non-aerated products and often times, the aerated products also exhibit a more pleasant and a lighter taste. Because of the incorporated gas cells, aerated products also have lower calorific value per volume than non-aerated products. This is an important property, especially for products with high calorific values such as chocolate and fat-containing foods. While a number of aerated products is known, generally speaking they are not satisfactory, especially in view of their texture.
For instance, aerated chocolate has been sold in the market place for a long time. However, the aerated chocolate has a rather unique structure with gas bubbles in the order of a few millimeters. Because of this, aerated chocolate represents an alternative to conventional non-aerated chocolate rather than a lighter version thereof.
While such aerated products may have some market potential, they are not desirable in general. On the contrary, rather than displaying large cells, it would be much more desirable to provide aerated products with gas cells virtually undetectable to the human eye. Such products will be referred to as microcellular in the following and are highly desirable as their texture is very close to that of non-aerated products. However, per unit volume, they contain less calories.
Providing food products such as chocolate with small microscopic and uniform cells is difficult to achieve. Prior art methods aiming at small uniform cells have only partially succeeded, both in terms of the required effort and the results.
U.S. Pat. No. 5,238,698 discloses a method of making aerated sucrose-free chocolate. In this process, the chocolate composition is continuously fed into a hopper under pressure and at temperatures in the range of from about 30° to 45° C. The chocolate composition is maintained under pressure and pumped through a series of static mixer elements after being injected with an inert gas. Following repeated gas injection and further mixer elements, the gas-containing chocolate composition is then pumped into a depositor which is also maintained under pressure in the order of 3 to 5 bars. Still under pressure, the chocolate mass is then put into molds, and pressure is released so as to develop a cellular structure.
This process is disadvantageous as it produces rather large cells and generally speaking, the density reduction is limited. There is, of course, a link between the size of the cells and the achievable density reduction. Materials with large cells tend to suffer from cell collapse to a greater extent than materials with small cells. Accordingly, if the number of large cells is increased, the likeliness of a loss of the cellular structure is also increased.
A further approach to aerated foods is disclosed in International Publication No. WO 2002/013618 A1. The process according to this document is also based on a combination of gas injection and static mixers. The result is again large cells of an average size of 0.7 mm in chocolate. Smaller cells of a size of 0.2 mm are only obtained in small pieces.
This goes to show that producing aerated foods with a microcellular structure is difficult. This is in part also due to the fact that in order to produce very small cells, prior art methods propose more intensive mixing procedures. This, however, also means that a higher amount of energy is introduced which, in turn, can cause changes in the product structure which can be due to the generated heat and/or high shear (WO 2002/013618).
European Patent Application EP 0 730 826 A2 discloses a method for the production of a mixture of solid particles dispersed in a continuous lipid phase. This process comprises a mixing step in which the solid particles in lipids are mixed to form a mixture which is then subjected to a refining step in which the solid particles are ground. Before the grounding step, micronized bubbles are incorporated by way of a microporous diffuser. In the case of EP 0 730 826, however, the micronized bubbles do not remain in the product. They only serve to remove unwanted volatiles in the subsequent milling step.
In view of this prior art, the present disclosure sets out to provide a method for making an aerated food product. The present disclosure thereby does not aim at the manufacture of an aerated product in general but primarily at a microcellular food product, wherein the gas cells or bubbles are small and evenly distributed without impairing the product properties. Accordingly, the present disclosure aims at providing a method where a microcellular structure can be obtained with little mechanical action and thermal stress imposed on the product. Moreover, the present disclosure also aims at providing such products which contain solid particles. The present disclosure is also directed to an apparatus for manufacturing the microcellular food product.
According to one aspect of the disclosed process, gas cells are incorporated into a food process medium by introducing an edible or inert gas through at least one microporous diffuser into the process stream. The thus obtained gas/food mixture is then blended by a static mixer.
With this process, the present disclosure allows to produce aerated food materials, in particular microcellular food products which demonstrate a substantial density reduction versus non-aerated food products with little change in texture or taste. Moreover, the method according to the present disclosure is suited for industrial scale production. The present disclosure thus provides for a highly beneficial process and product.
The process according to the present disclosure is illustrated in
The type of food that can be aerated according to the present process is not particularly limited. The present process works with any food process medium whose physical properties may be rendered capable of retaining gas cells within medium's matrix.
Typically the food according to the present disclosure is a food that can be conveyed inside a pipeline. Various foods such as chocolate, coffee extract, cream cheese, process cheese, other dairy products, ketchup, peanut butter as well as bakery products represent application examples for this disclosure.
The viscosity of the process medium before adding the gas through the microporous diffuser is typically in the range of about 1 to about 200 Pa·s, and preferably within the range of about 1 to about 60 Pa·s.
Preferred products are chocolate and cream cheese.
Chocolate formulas are of the type well known in the art and within the official Standards of Identity for chocolate and chocolate products.
Here below is the generic formula for milk chocolate as used during test runs.
The food according to the present disclosure may comprise solid particles such as nuts, vegetables or the like to blend with the product. Typically nuts, raisins and corn flakes are suitable for use in chocolate and vegetables such as bell peppers or chives are suitable in the case of cream cheese. There is no general limitation in this regard as long as the particulate materials have a size and shape so that they can pass the static mixer without being deteriorated or obstructing the mixer.
The gas according to the present process is an inert gas acceptable for use in food products. In particular, the present process may use air, nitrogen, carbon dioxide as well as inert gases such as argon. Preferred gases are nitrogen and carbon dioxide. When choosing the gas, it should be born in mind that products with a high water activity may have a tendency to dissolve carbon dioxide more readily than nitrogen. The dissolved carbon dioxide may acidify the product. Furthermore, fluid food additives or components such as flavors, etc. may be introduced into a food medium in the form of microscopic droplets through the microporous diffuser for accelerated uniform distribution of flavor.
The gas is introduced by way of a microporous diffuser. Such diffusers are known in the art, e.g., from European Patent Applications EP 0 730 826, EP 1 932 649, EP 1 717 008, International Application WO 2006/021375 A1, and U.S. Pat. No. 6,593,384, etc. Such diffusers are almost exclusively used in the manufacture of micro porous polymers.
The most conventional shape for the microporous gas diffuser is a relatively thin, long, hollow cylinder. This type of diffuser shape facilitates simplified incorporation of the diffuser inside the product pipeline and does not hinder the product flow. However, any other shape that accommodates for uniform distribution of gas cells within product is adequate for the diffuser.
For the use in foods according to the present disclosure, these diffusers do not need specific adaptation. Generally, any diffuser is suitable as long as it is permeable to gas to an extent that allows enough gas to be introduced into the food stream so as to allow for the desired density reduction. Microporous diffusers with pore size in the range about 0.1 to about 20 μm, preferably about 0.2 to about 10 μm and most preferably about 0.3 to about 5 μm are generally preferred. The diffusers may be made from sintered metals and may be coated with a protective finish. However, other sintered and/or porous materials allowed for the use in food industry can also be utilized.
The pressure required for introducing the gas into the food stream depends on the type of gas, the type of product, as well as the diffuser porosity and pore size distribution. It is also impacted by the desired cell size and gas volume fraction in the final product. For most of the applications within the food industry, the pressure ranges from about 0.5 to about 20 bar before the microporous diffuser, and preferably from about 6 to about 10 bar. However, for specific applications, e.g., gas injection into a coffee extract, the required pressure may range from about 50 to about 300 bar, preferably about 80 to about 120 bar.
The gas volume fraction incorporated into the food product depends on the specific application and is typically in the range of about 5 to about 75% vol., preferably about 5 to about 40% vol., and most preferably about 10 to about 30% vol.
Line pressure downstream from the diffuser is adjustable by means known in the industry such as a mechanical valve, pneumatic pinch valve, etc. in order to avoid rapid pressure drops from the diffuser to the point of discharge.
The gas/food mixture is then subjected to blending in a static mixer. Mixers of this kind are known in the art and commercially available. The specific mixer type depends on viscosity and mixing ratio, for most of the applications within food industry the static mixer with intersecting blades represents the preferred option.
The static mixer serves to blend the gas/food mixture and to reduce the overall cell size. The number of mixing elements is in the inverse proportion to the ratio “additive to mainstream medium”, i.e., the smaller the ratio, the higher number of mixing elements is required. The correlation between the number of mixing elements and the mixing ratio is well known to those skilled in the art.
The temperature of the food stream when adding the gas and subjecting it to the static mixer needs not be the same. However, conveniently, both steps are effected at the same temperature. Typically, the temperature is chosen such that a sufficient amount of gas can be absorbed without negatively influencing the product. Thus, for chocolate for instance, it is important to keep the temperature between about 27° C. and about 34° C. so as to maintain the chocolate in a tempered state and avoid later blooming. Products with high protein content will rarely be subjected to temperatures above about 40° C. In general, the temperature range is about 15° C. to about 60° C. for both the gas addition and the static mixing.
The temperature of the product may be adjusted downstream of the static mixer so as to achieve the desired product properties upon deposition, e.g., product viscosity will be largely affected by the deposition temperature
Product deposition at low temperatures is generally preferred, as typically low temperatures such as temperatures of about 30° C. or less, e.g., about 25° C. or less even about 15° C. or less lead to a higher product viscosity, which improves gas cell retention. Various depositors well known in the art can be utilized to facilitate depositing at lower temperatures. In any event, the deposition temperature can be optimized by the skilled person depending on the product and its desired properties.
As mentioned before, the present disclosure aims at products with small gas cells and preferably products with a microcellular structure. Microcellular generally implies gas cells of an average size of about 100 μm or less. In one approach, the average cell size is less than about 50 μm and in other approaches, the average cell size falls within the range of about 5 to about 30 μm. In one example, the average cell size is about 5 to about 10 μm. In one embodiment, at least about 90% of the cells have a size between about 10 and about 50 μm.
The gas cell size can be established with known techniques, e.g., by x-ray micro-tomography. X-Ray micro-tomography provides unique opportunities to visualize and measure the microstructure of food materials in two and even three dimensions. It allows non-destructive measurements without a time consuming preparation method. A micro-focus x-ray force illuminates the object and a planar x-ray detector collects magnified projection images. Based on hundreds of angular views acquired while the object rotates, a radiographic image is generated. The reconstruction takes place using a Feldkamp algorithm. A 3D-object is obtained by addition of sequentially reconstructed slices.
Specifications of exemplary instrument:
Measurement:
Sample Preparation:
No preparation is required. Exceptionally, in order to achieve high resolutions, it may be necessary to reduce the original sample size. Each sample is measured in triplicate.
Analysis of Samples (Software CTan 1.8 was Used)
Different Steps for Analysis:
Reload data set of the reconstructed raw image into the memory of analysis software.
Determination of a region of interest (ROI) or a volume of region (VOI) for evaluation (ROI or VOI should be equal for the whole sample set).
Generation of a binary image: Reconstructed image is converted into a gray scale image on the basis of density differences; Based on the choice of grey scale, different structures in the image can be determined.
Custom processing: The program identifies all objects in the VOI (i.e., air bubbles) and calculates the volume of each object. The analysis of the air bubbles takes place under the assumption that all particles are spherical. On the basis of the volume value for each air bubble, the pore size radius is calculated. For the number distribution the air bubbles are classified in different pore radius groups, in which the number of pores are summarized. The volume distribution shows the proportional share of the total volume which is taking by different size classes.
Approximation: Result represents the mean average value of three analysis results of three different sample scans.
This is a standard procedure that is independent from the x-ray machine and the software. Of course, the skilled person will understand that the sample size and the number of bubbles must be chosen such that they fairly represent the material.
The product of the process according to the present disclosure typically contains about 30% or less by volume of gas. Preferably, the gas volume fraction is less than about 25% and most preferable it is in the range of about 10 to about 25%. By one approach, desired results are obtained when the aforementioned preferred gas volumes and preferred cell sizes are realized in combination.
In the preferred embodiment, further downstream of the process up until the depositor discharge point, the process parameters need to be maintained so as to avoid rapid pressure drops and large temperature changes. Any of these will lead to thermodynamic instabilities within the system, and result in cell sizes deviating from standard.
Further process and formula modifications can be utilized together with this method for adjustment of final results, e.g., employment of pipes with different cross sectional area downstream the apparatus, usage of Venturi tubes, positioning of porous diffuser further upstream, use of emulsifiers and/or ingredients for viscosity alteration, etc.
The present disclosure provides beneficial food products which can be used as such. The products according to the present disclosure can also be used as part of composite food products, e.g., as a filling, as layers or coatings. It is, of course, also possible to combine one or more products obtainable according to the method of the present disclosure.
The Examples that follow are intended to further illustrate, and not limit, embodiments in accordance with the disclosure. All percentages, ratios, parts, and amounts used and described herein are by weight unless indicated otherwise.
The apparatus comprising a microporous diffuser with pore size 1-5 μm and a static mixer with intersecting blades inside a DN25 pipeline was utilized for producing a micro-cellular wafer filling with nitrogen and carbon dioxide. For both gases, the specific weight of the wafer filling was reduced by 25% with gas cells non-detectable by the unaided human eye. Gas cell size distribution analysis demonstrated that the cell size ranged from 20 μm to 400 μm.
The ingredient composition of the wafer filling is summarized in the table below.
An installation comprising only a static mixer with intersecting blades was utilized for aeration of the same formula wafer filling with nitrogen and carbon dioxide. The static mixer was inserted into a product pipe with a corresponding cross-section and a gas injection port with a check valve was situated upstream the static mixer. For both gases, the process settings for specific weight reduction higher than 5% resulted in a jolting and inconsistent rate of product discharge that indicated ineffective gas diffusion in the process medium, i.e., presence of large pockets of gas within the wafer filling.
While the disclosure has been particularly described with specific reference to particular process and product embodiments, it will be appreciated that various alterations, modifications and adaptations may be based on the present disclosure, and are intended to be within the spirit and scope of the present disclosure as defined by the following claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 09168923 | Aug 2009 | EP | regional |
