Patent Application
20210084926
The invention relates to a manufacturing process for the production of a fat-fiber powder. In particularly the invention relates to a process for the production of a fat-fiber powder having up to 93% of a fat (by weight of total fat-fiber powder) and at least 7% of a vegetable fiber (by weight of total fat-fiber powder), wherein the fiber is characterized by having a rate of hydration between 15 to 500 cP/min and wherein the fat has a solid fat content (SFC) at 20° C. at least of 12.1 wt % (by weight of total fat).
Fats are often added in foods to provide nutrition, taste/aroma, texture, specific processing role, and/or to drive consumers liking. Fat powders are available and have been widely used in food products as confectionary products or culinary products as soups, bouillon powders or bouillon tablets/cubes. By nature, fat powders are temperature-sensitive and therefore exposure to a mild elevation of temperatures (e.g. 25° C. to 40° C.) can be detrimental causing powders to lump which subsequently impairs mixing and/or tableting process. Solutions relate to stringent delivery and storage condition of fat powders (always kept in temperature controlled condition). Major cost impact is one drawback. Ensuring strict supply chain conditions is another issues that often cannot be easily solved. Another limitation to produce a fat powder is related that a minimum crystallinity characteristic of fat is required. Solid fat content (SFC) at 30° C. of at least 45 wt % (by weight of total fat) is usually advised. This limits the selection of fats to powderise. High SFC fats are usually having low amounts of unsaturated fatty acids. Unsaturated fatty acids are usually positively perceived by consumers. Therefore there is a need to increase the load of unsaturated fatty acid in the fat powders for its application.
Hence, it was the object of the present invention to provide the art with a manufacturing process for the production of a solid fat-fiber powder. This solid fat-fiber powder is suitable to use for the preparation of a food product.
The object of the present invention is to improve the state of the art or at least provide an alternative for a fat-fiber powder (powdered fat) having a solid fat content (SFC) at 20° C. of at least 12.1 wt % (by weight of total fat):
The object of the present invention is achieved by the subject matter of the independent claims. The dependent claims further develop the idea of the present invention.
Accordingly, the present invention provides in a first aspect a process for the production of a fat-fiber powder comprising up to 93 wt % of a fat (by weight of total fat-fiber powder) and at least 7 wt % of a fiber (by weight of total fat-fiber powder), the process comprising the steps of:
In a second aspect of the invention, there is provided a product obtainable by process for the production of a fat-fiber powder having up to 93 wt % of a fat (by weight of total fat-fiber powder) and at least 7% of a fiber (by weight of total fat-fiber powder) comprising the steps of:
A third aspect of the invention relates to a food product prepared by making use of the fat-fiber powder of the invention. Such food product can be a confectionary product or a culinary food product e.g. a dough, a soup, bouillon powder or hard bouillon tablet/cube.
It has been surprisingly found by the inventors that by the process of the invention a fat-fiber powder comprising up to 93% of a fat (by weight of total fat-fiber powder) and at least 7% of fiber (by weight of total fat-fiber powder), wherein the fiber is characterized by having a rate of hydration between 15 to 500 cP/min, can be obtained which can now solve the requirement to achieve the necessary attributes:
The present invention pertains to a process for the production of a fat-fiber powder comprising up to 93 wt % of a fat (by weight of total fat-fiber powder) and at least 7 wt % of a fiber (by weight of total fat-fiber powder), the process comprising the steps of:
In an embodiment the invention pertains to a process for the production of a fat-fiber powder comprising between 40 to 93 wt % of fat (by weight of total fat-fiber powder) and 7 to 60 wt % of a fiber (by weight of total fat-fiber powder), the process comprising the steps of:
In a preferred embodiment the present invention pertains to a process for the production of a fat-fiber powder comprising between 75 to 93 wt % of fat (by weight of total fat-fiber powder) and 7 to 25 wt % of a fiber (by weight of total fat-fiber powder), wherein the fiber is characterized by having a rate of hydration between 15 to 500 cP/min and wherein the fat has a solid fat content (SFC) at 20° C. of at least 12.1 wt % (by weight of total fat).
“Fat-fiber powder” according to this invention has particle size distribution with a median diameter Dv50 in the range of 15 to 5000 μm, preferably in the range of 20 to 5000 μm, preferably in the range of 30 to 3000 μm, preferably in the range of 30 to 1500 μm, preferably in the range of 40 to 1500 μm, preferably in the range of 40 to 1000 μm, preferably in the range of 50 to 1000 μm, preferably in the range of 80 to 1000 μm, preferably in the range of 80 to 700 μm, preferably in the range of 100 to 700 μm, preferably in the range of 150 to 700 μm, preferably in the range of 150 to 500 μm. In a further embodiment “fat-fiber powder” according to this invention has a water activity below 0.50, preferably below 0.40, preferably below 0.35, more preferably below 0.30, more preferably below 0.25, more preferably below 0.20, more preferably between 0.01 and 0.40.
The particle size Dv50 is used in the conventional sense as the median of the particle size distribution. Median values are defined as the value where half of the population reside above this point, and half resides below this point. The Dv50 is the size in micrometer that splits the volume distribution with half above and half below this diameter. The particle size distribution may be measured by laser light scattering, microscopy or microscopy combined with image analysis. For example, the particle size distribution may be measured by laser light scattering. Since the primary result from laser diffraction is a volume distribution, the Dv50 cited is the volume median.
“Fat” of the present invention has a solid fat content (SFC) at 20° C. of at least 12.1 wt % (by weight of total fat), preferably has a solid fat content (SFC) at 20° C. between 12.1 to 90 wt %, preferably has a solid fat content (SFC) at 20° C. between 15 to 85 wt %, preferably has a solid fat content (SFC) at 20° C. between 20 to 85 wt %, preferably has a solid fat content (SFC) at 20° C. between 20 to 80 wt %, preferably has a solid fat content (SFC) at 20° C. between 20 to 75 wt %, preferably has a solid fat content (SFC) at 20° C. between 25 to 75 wt %, preferably has a solid fat content (SFC) at 20° C. between 30 to 75 wt %, preferably has a solid fat content (SFC) at 20° C. between 40 to 75 wt %. Fat is solid at a temperature of 20° C., preferably at a temperature of 25° C. Sunflower oil has a solid fat content (SFC) at 20° C. of 0. Olive oil has a solid fat content (SFC) at 20° C. of 0. Chicken fat has a solid fat content (SFC) at 20° C. of 3.7. The solid fat content shows that according to the invention oils are excluded as they are liquid at a temperature of 25° C., preferably at room temperature of 20° C.
In a preferred embodiment the fat is selected from the group consisting of palm oil, palm stearin, hydrogenated palm oil, interesterified palm oil, coconut oil, cocoa butter, shea butter, fractionated shea butter, sal fat, illipe butter, mango (kernel) oil, kokum butter, beef fat (tallow), fractionated beef fat, pork fat (lard), butter, milk fat, single and double fractionated chicken fat or combination thereof. The present invention does not include palm olein.
In a further embodiment, the fat-fiber powder comprises fat in an amount in the range of 40 to 93% (by weight of the fat-fiber powder), preferably between 45 to 93%, preferably between 50 to 93%, preferably 55 to 93%, preferably 60 to 93%, preferably 70 to 93%, preferably 75 to 93%, preferably 80 to 93%, preferably 85 to 93%, preferably 70 to 90%, preferably 75 to 90%, preferably 75 to 85% (by weight of the fat-fiber powder). The fat is melted before mixing the fiber at temperatures between 50 and 100° C.; preferably between 50 and 90° C.; preferably between 60 and 90° C.; more preferably between 60 and 85° C.
“Fiber” according to this invention is characterized by having a rate of hydration between 15 to 500 cP/min, preferably 25 to 400 cP/min, preferably 50 to 350 cP/min. The cP/min can be recalculated to cP/sec and 1 cP=10−3 Pa·s. In a preferred embodiment fiber having a rate of hydration between 0.250 to 8.333 cP/sec, preferably 0.417 to 6.666 cP/sec, preferably 0.833 to 5.833 cP/sec.
“Rate of hydration” according to this invention is defined as the time required for the fiber to interact with water and swell resulting an increase in viscosity.
In a preferred embodiment fiber is a water insoluble dietary fiber, preferably a water insoluble vegetable dietary fiber. It is selected from at least one of carrot, beetroot, pumpkin or combinations thereof.
Fiber has particle size with median diameter Dv50 in the range of 5 to 400 μm, preferably in the range of 10 to 400 μm, preferably in the range of 15 to 400 μm, preferably in the range of 20 to 400 μm, preferably 25 to 375 μm, preferably 30 to 350 μm; preferably 35 to 300 μm.
In a further embodiment, the fat-fiber powder comprises fiber in an amount in the range of 7 to 60% (by weight of the fat-fiber powder), preferably between 7 to 55%, preferably between 7 to 50%, preferably 7 to 45%, preferably 7 to 40%, preferably 7 to 30%, preferably 7 to 25%, preferably 7 to 20%, preferably 7 to 15%, preferably 10 to 30%; preferably 10 to 25%, preferably 15 to 25% (by weight of the fat-fiber powder).
In an embodiment water is added at a weight ratio of fiber to water between 1:2.5 and 1:35, preferably between 1:3 and 1:30, preferably between 1:3.5 and 1:30, preferably between 1:3.5 and 1:25, preferably between 1:3.5 and 1:20. In an embodiment the added water has a temperature between 40 and 100° C., preferably between 50 and 100° C., preferably between 50 and 90° C., more preferably between 60 and 90° C.
“Dietary fiber” consists of the remnants of the edible plant cell, polysaccharides, lignin, and associated substances resistant to digestion (hydrolysis) by human alimentary enzymes.
In a preferred embodiment, the fat-fiber powder of the present invention does not include any emulsifier, added proteins or combinations thereof. The term “emulsifier” is selected from the group consisting of egg yolk, lecithin, mustard, soy lecithin, sodium phospates, sodium stearoyl lactylate, diacetyl tartaric ester of monoglyceride (DATEM), polyglycerol-polyricinoleate (PGPR), monoglyceride and mono-diglyceride or a combination thereof. The term “protein” is selected from the group consisting of milk and/or whey proteins, soy proteins, pea proteins, caseinate, egg albumen, lyzozyme, gluten, rice protein, corn protein, potato protein, pea protein, skimmed milk proteins or any kind of globular and random coil proteins as well as combinations thereof.
The drying step can be carried out by any commonly known drying technique such as air drying, oven drying, ventilation, spray drying, vacuum drying, bed drying, microwave-vacuum drying, infrared radiation drying or combinations thereof. The drying temperature is between 50 to 120° C., preferably between 50 to 110° C., preferably between 60 to 100° C., preferably between 60 to 90° C.
Milling according to this invention is a process that breaks solid materials into smaller pieces by grinding, crushing, or cutting. Milling can be carried out by any commonly known milling techniques such as roll mill, hammer mill, chopper mill, ball mill, SAG mil, rod mil or combinations thereof.
Independently of the mixing sequence of the fiber, fat, and water a powdered fat-fiber can be obtained after drying. In case fiber and water is mixed first the viscosity of this mixture is higher due to the swelling of the fiber. Therefore adding melted fat to the fiber-water-suspension needs a longer mixing time or a higher mixing shear rate to obtain a homogenous fiber-fat-water mixture. In a preferred embodiment the fiber and melted fat is mixed first and water is added afterwards and further mixed. This process sequence has the advantage that the resulting fat-fiber-water-suspension ensures a better homogenous mixture in less time or lower mixing shear rate.
“Flow-ability” means flow properties on how easily a powder flows. Flow-ability (f fc) is quantified as the ratio of consolidation stress σ1 to unconfined yield strength ci, according to “Schulze, D. (2006). Flow properties of powders and bulk solids. Braunschweig/Wolfenbuttel, Germany: University of Applied Sciences.” In an embodiment flow-ability (f fc) of the fat-fiber powder is at least 1.8 at 23° C., preferably between the range of 1.8 to 12 at 23° C., preferably between the range of 2 to 10 at 23° C., preferably between the range of 2 to 8 at 23° C., preferably between the range of 2.2 to 7 at 23° C.
The invention is further described with reference to the following examples. It is to be appreciated that the examples do not in any way limit the invention.
The general procedure for preparing fat powder of the invention is as follows:
Fiber was mixed with melted fat in a Thermomix TM5 (Vorwerk &Co. KG). Mixing speed was set to speed 3. Mixing was performed for 5 minute, until a homogenous slurry was obtained. Subsequently, water at a temperature of 75° C. was gradually added to the mixture while mixing parameters were maintained. Mixing was maintained for another 3 minute. The slurry was then spread onto a baking pan; slurry thickness was maintained between 5 and 10 mm, then dried in Rational Self Cooking Centre Electric Combination Oven SCC202E (Rational AG, Germany). Drying was carried out for 12 h at 70° C. with 30% fan speed.
In order to evaluate and understand rate of hydration of fiber, experiments were performed in the laboratory under controlled conditions using a Rapid Viscosity Analyser (Newport Scientific, Australia). The method has been slightly modified as described within the reference “Instant Emulsions, Tim Foster et al, pages 413-422 in Dickinson, E. and M. E. Leser (2007). Food Colloids: Self-assembly and Material Science, Royal Society of Chemistry.” Rate of hydration of fibers were measured by following the change in viscosity with time. 2.5 g of fiber or non-fiber material was weighed and added to 22.5 g of water. Measurement was carried out at 25° C. under continuously steering at 160 rpm. The value for rate of hydration is determined by subtracting the final viscosity value from the initial viscosity value and then divided by the time, i.e. 10 min. When maximum (peak) viscosity value is observed earlier than 10 min (e.g. for the case of citrus fiber), the rate of hydration is determined by subtracting the maximum viscosity from the initial viscosity values and then divided by the time to reach this maximum viscosity value.
In case the fat is mixed with fiber alone (no added water), the presence of fiber does not improve flow-ability of fat powder (Comp. Ex. 3), shown by comparable flow-ability index to that of in pure fat powder (Comp. Ex. 2).
Different kind of fibers have been tested according the process of example 1. Examples 7 to 10 show that the rate of hydration of fiber should be between 15 to 500 cP/min to obtain a flow-able powder.
Three different carrot fibers regarding the particle size have been tested. It is concluded that the tested particle size does not have an influence on the preparation of a fat powder.
When standard palm fat powder (SFC at 20° C. of 45-75 wt %) is exposed to temperatures of 130° C. in frying pan, the fat melts and smears over the pan. When fat-fiber powder with 90 wt % fat and 10 wt % carrot fiber (example 4) is exposed to a temperature of 130° C. in frying pan, it retains the powder structure and the fat does not smear out. See
When the fat-fiber powder (e.g. example 4) is suspended in water at 60° C., the fat is released and so called fat eyes are visible on top.
| Number | Date | Country | Kind |
|---|---|---|---|
| 18152898.5 | Jan 2018 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2019/051316 | 1/21/2019 | WO | 00 |
