US20120128829A1 - Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof - Google Patents
Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof Download PDFInfo
- Publication number
- US20120128829A1 US20120128829A1 US13/357,357 US201213357357A US2012128829A1 US 20120128829 A1 US20120128829 A1 US 20120128829A1 US 201213357357 A US201213357357 A US 201213357357A US 2012128829 A1 US2012128829 A1 US 2012128829A1
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- composition
- dairy
- freeze
- yogurt
- mono
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Links
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Classifications
-
- 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; MAKING OR TREATMENT THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/12—Fermented milk preparations; Treatment using microorganisms or enzymes
- A23C9/123—Fermented milk preparations; Treatment using microorganisms or enzymes using only microorganisms of the genus lactobacteriaceae; Yoghurt
- A23C9/1232—Fermented milk preparations; Treatment using microorganisms or enzymes using only microorganisms of the genus lactobacteriaceae; Yoghurt in powdered, granulated or dried solid form
-
- 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; MAKING OR TREATMENT THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/12—Fermented milk preparations; Treatment using microorganisms or enzymes
- A23C9/13—Fermented milk preparations; Treatment using microorganisms or enzymes using additives
- A23C9/1307—Milk products or derivatives; Fruit or vegetable juices; Sugars, sugar alcohols, sweeteners; Oligosaccharides; Organic acids or salts thereof or acidifying agents; Flavours, dyes or pigments; Inert or aerosol gases; Carbonation methods
-
- 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; MAKING OR TREATMENT THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/12—Fermented milk preparations; Treatment using microorganisms or enzymes
- A23C9/13—Fermented milk preparations; Treatment using microorganisms or enzymes using additives
- A23C9/137—Thickening substances
-
- 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; MAKING OR TREATMENT THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/152—Milk preparations; Milk powder or milk powder preparations containing additives
- A23C9/1524—Inert gases, noble gases, oxygen, aerosol gases; Processes for foaming
-
- 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; MAKING OR TREATMENT THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/152—Milk preparations; Milk powder or milk powder preparations containing additives
- A23C9/154—Milk preparations; Milk powder or milk powder preparations containing additives containing thickening substances, eggs or cereal preparations; Milk gels
- A23C9/1544—Non-acidified gels, e.g. custards, creams, desserts, puddings, shakes or foams, containing eggs or thickening or gelling agents other than sugar; Milk products containing natural or microbial polysaccharides, e.g. cellulose or cellulose derivatives; Milk products containing nutrient fibres
- A23C9/1546—Non-acidified gels, e.g. custards, creams, desserts, puddings, shakes or foams, containing eggs or thickening or gelling agents other than sugar; Milk products containing natural or microbial polysaccharides, e.g. cellulose or cellulose derivatives; Milk products containing nutrient fibres in powdered, granulated or dried solid form
-
- 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; MAKING OR TREATMENT THEREOF
- A23C2240/00—Use or particular additives or ingredients
- A23C2240/20—Inert gas treatment, using, e.g. noble gases or CO2, including CO2 liberated by chemical reaction; Carbonation of milk products
Definitions
- Aerated milk compositions such as aerated yogurt products are known in the art. Aeration can provide desirable characteristics such as light, fluffy textures. It is also known in the art that aerated products are subject to physical and chemical instability and therefore can destabilize over time.
- One solution to such instability issues in aerated milk-based products includes the addition of a hydrated emulsifier to already cultured dairy products before aeration (See e.g. U.S. Pat. No. 7,005,157, hereinafter “the '157 patent”). Specifically, the, 157 patent teaches against adding ingredients directly to the milk blend prior to fermentation because such ingredients can adversely affect processing considerations such as fermentation times.
- the '157 patent teaches that the addition of a hydrated emulsifier post-fermentation avoids adversely lengthening fermentation times while contributing to stability. Freeze-drying is a process well known in the food industry. It is critical in further drying aerated products that the resulting product retain sensory attributes that are important to consumers. Using the invention taught in the '157 patent, hydration of the aerated product before freeze-drying can detrimentally affect physical stability. For example, a hydrated, aerated product when freeze dried may result in increased fragility during shipping and handling of the product.
- dissolvability is an important issue in a freeze-dried product.
- the aerated product which has been dried and treated with air, nitrogen or other gases, must still remain readily dissolvable upon consumption at such a rate as to transfer flavor to the consumer's taste buds.
- the product should be readily dissolvable to reduce the risk of choking hazards for consumers with restricted or under-developed oral motor skills or digestive functions.
- increasing the aeration can improve dissolvability.
- increased aeration has the negative effect of reducing the hardness of the end product. When the hardness is reduced beyond a certain level, the physical stability of product can be compromised.
- the present invention comprises a freeze-dried, aerated dairy or dairy-substitute composition comprising a dairy or dairy-substitute ingredient, an emulsifier, wherein said dairy or dairy-substitute composition is pasteurized, and methods of making thereof.
- ranges are used as a shorthand for describing each and every value that is within the range. Any value within the range can be selected as the terminus of the range.
- the phrase “at least one of” refers to the selection of anyone member individually or any combination of the members.
- the conjunction “and” or “or” can be used in the list of members, but the “at least one of” phrase is the controlling language.
- at least one of A, B, and C is shorthand for A alone, B alone, C alone, A and B, B and C, A and C, or A and Band C.
- Freeze-dry is a dehydration process that works by freezing the material and then reducing the surrounding pressure to allow the frozen water in the material to sublimate directly from the solid phase to gas.
- “Aeration” is the process of introducing air to increase gas concentration in liquids. Aeration may be performed by bubbling a gas through the liquid, spraying the liquid into the gas or agitation of the liquid to increase surface absorption.
- Dissolvability is defined as the change in hardness of a product in going from a dry to a wet state.
- Hardness is defined as the peak stress prior to fracturing a material. Universal Tester model 4465 with 100 N static load cell, manufactured by Instron in Canton, Mass., is used. The probe used for testing is a compression anvil #2830-011. Initial settings for speed of probe were 1 mm/second to approximately 90% compression. Speed based upon journal article in J. Texture Studies, 36 (2005), pp 157-173, “Effects of Sample Thickness of Bite Force for Raw Carrots and Fish Gels.” Testing is repeated on 10-15 replicate samples for each variable.
- Viscosity is defined as a measure of the resistance of a substance to flow. Viscosity is measured using a Brookfield viscometer with a Helipath® stand with an F-T bar before the composition is aerated. Viscosity aids in holding the shape of a substance through aeration and deposit.
- the present invention comprises a dairy or dairy substitute composition useful in the preparation of a freeze-dried, aerated product.
- the first component of the composition comprises a dairy or dairy substitute ingredient.
- the dairy or dairy substitute ingredient is selected from any dairy or dairy substitute ingredient ordinarily known in the art. Specifically, the dairy ingredient is selected from the group including but not limited to milk, milk powder, yogurt, skim milk and milk proteins and combinations thereof.
- the dairy substitute ingredient is selected from but not limited to soy proteins and rice proteins and combinations thereof.
- the dairy or dairy substitute ingredient is present in amount of from 50% to 98%, preferably from 60% to 90% and most preferably from 70% to 85% of the composition.
- the second component of the present composition comprises an emulsifier. While not wishing to be bound by any theories, it is believed that the emulsifier reduces the surface tension at the air-liquid interface, therefore allowing for stable dispersion of air bubbles within the viscous liquid matrix.
- the emulsifier is preferably a lactylated mono and diglyceride.
- the lactylated mono and diglyceride is selected from the group consisting of but not limited to lactic and citrate acid esters of mono- and diglycerides, distilled mono glycerides, and combinations thereof.
- the lactic acid moiety of the whipping agent resides in the aqueous phase at the interface of the aqueous phase and the hydrophobic phase while the mono and diglycerides reside in hydrophobic phase of the whipped dairy foam.
- the lactylated mono and diglycerides are present in an amount of from 0.001 to 1%, preferably from 0.01 to 0.5%, and most preferably from 0.1 to 0.4% of the composition. It is believed that the lactylated mono and diglyceride component of the present invention promotes stabilization of the final aerated composition.
- the combination of the first component and the second component are then pasteurized through procedures commonly used in the industry. Pasteurization can take between 1 to 10 minutes between 170 F to 210 F, preferably between 180 F to 205 F.
- composition of the present invention can further comprise optional ingredients such as starch, including but not limited to com starch, rice starch (native, physically or chemically modified) and tapioca starch; sugar/sweetners, stabilizers, flavors, colors, fruit purees, prebiotics, probiotics, vegetable purees, fibers, fortificants such as DHA, minerals and vitamins, and gelatins such as porcine, fish and bovine.
- starch including but not limited to com starch, rice starch (native, physically or chemically modified) and tapioca starch
- Viscosity is defined as a measure of the resistance of a substance to flow. Viscosity is measured using a Brookfield viscometer with a Helipath® stand with an F-T bar before the composition is aerated. It is believed that while the viscosity aids in holding the shape of a substance through aeration and deposit, the hardness aids in physical stability.
- the dissolvability also a hardness measurement, is the change in hardness of a product in going from a dry to a wet state.
- compositions and methods of the present invention have unexpectedly discovered the optimum balance between viscosity, hardness and dissovability to provide a physically stable and consumer acceptable product.
- the composition of the present invention has a hardness value of from 0.5 to 8 pounds force, preferably from 1.5 to 5.5 peak load. Peak load force can be measured using an Instron Universal Testing Machine fitted with a 100N load cell anda #2830-011 compression anvil. The traveling is at a speed of 1 mm/sec until initial piece fraction occurs.
- composition of the present invention has a dissolvability in the range of from 0.1 to 8 peak load, preferably from 0.1 to 30 pounds force.
- the composition of the present invention has a viscosity of from 1,000 to 150,000 cp, dependent upon the temperature and speed of the viscometer used to measure the viscosity.
- the viscosity of the wet composition ranges from 30,000 to 60,000 cp at a 10 RPM speed of the spindle 6 in a Brookfield Viscometer. The most preferred range is from 35,000 to 50,000 cp.
- the present invention has a viscosity of from 1,000 to 700,000 cp, dependent upon the temperature and speed of the viscometer used to measure the viscosity.
- the viscosity of the wet composition ranges from 100,000 to 400,000 cp at a 5 RPM speed of the spindle 6 in a Brookfield Viscometer.
- the most preferred range for the alternate embodiment is from 200,000 to 350,000 cp. It should be noted that the viscosity can be adjusted based on the RPM and is dependent upon dissolvability and the stabilizer.
- a method of preparing a freeze-dried, aerated, milk product comprising the steps of (a) providing a dairy or dairy substitute blend, (b) adding an emulsifier, (c) thermally processing the dairy or dairy substitute blend, (d) fermenting the blend, (e) admixing a gas with the blend; (f) simultaneously aerating the gas and the dairy or dairy substitute blend to form an aerated product, and (f) cooling the product; and (g) freeze-drying the product.
- Pasteurized lowfat milk is transferred from a tanker truck to large hold tank.
- the mixture is transferred to the HTST plate heat exchanger for thermal processing.
- the thermal process conditions used require that all achieve and maintain a minimum temperature of 191 deg F at the end of a 4 5 minutes hold time. This temperature and hold time can vary depending upon the mechanics of the process, for example it is possible to go slightly higher in temperature and have a 7 or 8 minute hold time.
- homogenizing of the mixture can occur.
- the typical homogenization pressures are 2000 to 2500 psi at a first stage and 200-600 psi at a second stage.
- the mix is cooled to 100-112 deg F., and transferred to the culturing vat.
- the yogurt culture is added (for example, a freeze-dried culture, ABY-2C, supplied by Danisco Ingredients, or other vendors).
- the culture is blended with the pasteurized mix for 30-60 minutes, the mixing is stopped and the vat is maintained at 104-107 deg F. for 4-6 hours.
- Yogurt is allowed to acidify to pH 4.5 to 4.6, and is then agitated (broken) and cooled to 60 deg F. in the culture tank. Final pH will range from is 4.1-4.4.
- Yogurt is transferred to 250 gal. blending tanks by pumping through a cooling press, which lowers temp to 37-45 deg F. Pasteurized fruit puree, flavors and any desired color will be added. Mixture will be blended with gentle agitation and recirculation for 10-15 minutes. Blended fruit yogurt is transferred to 275 gallon totes.
- Yogurt will be conveyed/pumped from 275 gallon totes (previously stored at 34-40 deg F.) to the aerator (in this case, a Mondomix aerator, although other brands exist).
- Nitrogen gas is admixed to the yogurt via the Mondo mixer (connected to plant ice water circulation system, to maintain mixing head temperature at 35-45 deg F.).
- Product overrun can range from 20% to 80%. However, preferably, the overrun target will be between 30% and 50% and most preferably between 35% and 45%. This process happens continuously.
- Aerated yogurt is pumped, maintained at 38-50 deg F., under pressure, to a depositor manifold, where it is distributed to multiple nozzles which, via a metering pump, create the appropriately shaped deposit form (in this case, a large chocolate chip shape, although other shapes/forms are possible).
- the current target shape has a diameter of 13-22 mm (ideal is 15-20 mm), a height of 7-12 mm (ideal is 8-10), and a weight of 0.8-1.3 grams (ideal is 1.0-1.1 g).
- Freezer tunnel air temperature is approximately ⁇ 20 to ⁇ 30 deg F., with high velocity air circulation. Dwell time in the tunnel can range from 3-5 minutes. Frozen pieces exit the tunnel with an internal temperature of 24-28 deg F.
- composition of the present invention can be prepared. The percentages listed are based on the total weight of the composition.
- composition described above is made using the methods described herein.
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Microbiology (AREA)
- Dispersion Chemistry (AREA)
- Dairy Products (AREA)
- Fodder In General (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
Abstract
The present invention comprises a freeze-dried, aerated dairy or dairy-substitute composition comprising a dairy or dairy-substitute ingredient and an emulsifier and methods of making thereof.
Description
- This application is a continuation of U.S. application Ser. No. 12/599,321, filed Jan. 28, 2010, which is the U.S. national stage designation of International Application No. PCT/US08/063312, filed on May 9, 2008, which claims priority to U.S. application Ser. No. 60/916,949, filed on May 9, 2007, the entire contents of which are incorporated herein by reference.
- Aerated milk compositions, such as aerated yogurt products are known in the art. Aeration can provide desirable characteristics such as light, fluffy textures. It is also known in the art that aerated products are subject to physical and chemical instability and therefore can destabilize over time. One solution to such instability issues in aerated milk-based products includes the addition of a hydrated emulsifier to already cultured dairy products before aeration (See e.g. U.S. Pat. No. 7,005,157, hereinafter “the '157 patent”). Specifically, the, 157 patent teaches against adding ingredients directly to the milk blend prior to fermentation because such ingredients can adversely affect processing considerations such as fermentation times. The '157 patent teaches that the addition of a hydrated emulsifier post-fermentation avoids adversely lengthening fermentation times while contributing to stability. Freeze-drying is a process well known in the food industry. It is critical in further drying aerated products that the resulting product retain sensory attributes that are important to consumers. Using the invention taught in the '157 patent, hydration of the aerated product before freeze-drying can detrimentally affect physical stability. For example, a hydrated, aerated product when freeze dried may result in increased fragility during shipping and handling of the product.
- As a further example, dissolvability is an important issue in a freeze-dried product. Specifically, the aerated product, which has been dried and treated with air, nitrogen or other gases, must still remain readily dissolvable upon consumption at such a rate as to transfer flavor to the consumer's taste buds. Moreover, the product should be readily dissolvable to reduce the risk of choking hazards for consumers with restricted or under-developed oral motor skills or digestive functions. As a known solution, increasing the aeration can improve dissolvability. However, increased aeration has the negative effect of reducing the hardness of the end product. When the hardness is reduced beyond a certain level, the physical stability of product can be compromised.
- Therefore, there is a need for a product that is freeze-dried and aerated that has improved physical stability and improved dissolvability.
- The present invention comprises a freeze-dried, aerated dairy or dairy-substitute composition comprising a dairy or dairy-substitute ingredient, an emulsifier, wherein said dairy or dairy-substitute composition is pasteurized, and methods of making thereof.
- As used throughout, ranges are used as a shorthand for describing each and every value that is within the range. Any value within the range can be selected as the terminus of the range. When used, the phrase “at least one of” refers to the selection of anyone member individually or any combination of the members. The conjunction “and” or “or” can be used in the list of members, but the “at least one of” phrase is the controlling language. For example, at least one of A, B, and C is shorthand for A alone, B alone, C alone, A and B, B and C, A and C, or A and Band C.
- “Freeze-dry” is a dehydration process that works by freezing the material and then reducing the surrounding pressure to allow the frozen water in the material to sublimate directly from the solid phase to gas.
- “Aeration” is the process of introducing air to increase gas concentration in liquids. Aeration may be performed by bubbling a gas through the liquid, spraying the liquid into the gas or agitation of the liquid to increase surface absorption.
- “Dissolvability” is defined as the change in hardness of a product in going from a dry to a wet state.
- “Hardness” is defined as the peak stress prior to fracturing a material. Universal Tester model 4465 with 100 N static load cell, manufactured by Instron in Canton, Mass., is used. The probe used for testing is a compression anvil #2830-011. Initial settings for speed of probe were 1 mm/second to approximately 90% compression. Speed based upon journal article in J. Texture Studies, 36 (2005), pp 157-173, “Effects of Sample Thickness of Bite Force for Raw Carrots and Fish Gels.” Testing is repeated on 10-15 replicate samples for each variable.
- “Viscosity” is defined as a measure of the resistance of a substance to flow. Viscosity is measured using a Brookfield viscometer with a Helipath® stand with an F-T bar before the composition is aerated. Viscosity aids in holding the shape of a substance through aeration and deposit.
- The present invention comprises a dairy or dairy substitute composition useful in the preparation of a freeze-dried, aerated product. The first component of the composition comprises a dairy or dairy substitute ingredient. The dairy or dairy substitute ingredient is selected from any dairy or dairy substitute ingredient ordinarily known in the art. Specifically, the dairy ingredient is selected from the group including but not limited to milk, milk powder, yogurt, skim milk and milk proteins and combinations thereof. The dairy substitute ingredient is selected from but not limited to soy proteins and rice proteins and combinations thereof. The dairy or dairy substitute ingredient is present in amount of from 50% to 98%, preferably from 60% to 90% and most preferably from 70% to 85% of the composition.
- The second component of the present composition comprises an emulsifier. While not wishing to be bound by any theories, it is believed that the emulsifier reduces the surface tension at the air-liquid interface, therefore allowing for stable dispersion of air bubbles within the viscous liquid matrix. The emulsifier is preferably a lactylated mono and diglyceride. The lactylated mono and diglyceride is selected from the group consisting of but not limited to lactic and citrate acid esters of mono- and diglycerides, distilled mono glycerides, and combinations thereof. While not wishing to be bound by any theories, it is believed that the lactic acid moiety of the whipping agent resides in the aqueous phase at the interface of the aqueous phase and the hydrophobic phase while the mono and diglycerides reside in hydrophobic phase of the whipped dairy foam. The lactylated mono and diglycerides are present in an amount of from 0.001 to 1%, preferably from 0.01 to 0.5%, and most preferably from 0.1 to 0.4% of the composition. It is believed that the lactylated mono and diglyceride component of the present invention promotes stabilization of the final aerated composition.
- The combination of the first component and the second component are then pasteurized through procedures commonly used in the industry. Pasteurization can take between 1 to 10 minutes between 170 F to 210 F, preferably between 180 F to 205 F.
- The composition of the present invention can further comprise optional ingredients such as starch, including but not limited to com starch, rice starch (native, physically or chemically modified) and tapioca starch; sugar/sweetners, stabilizers, flavors, colors, fruit purees, prebiotics, probiotics, vegetable purees, fibers, fortificants such as DHA, minerals and vitamins, and gelatins such as porcine, fish and bovine.
- Hardness, Dissolvability and Viscosity
- The consumer preference for the final product of the present invention is believed to be based on physical characteristics such as hardness, viscosity and dissolvability. While each characteristic is important, the correct balance between the three components is desired to optimize the end product of the present invention. Viscosity is defined as a measure of the resistance of a substance to flow. Viscosity is measured using a Brookfield viscometer with a Helipath® stand with an F-T bar before the composition is aerated. It is believed that while the viscosity aids in holding the shape of a substance through aeration and deposit, the hardness aids in physical stability. The dissolvability, also a hardness measurement, is the change in hardness of a product in going from a dry to a wet state. With increased aeration, which aids in dissolvability, the hardness can be negatively affected. The compositions and methods of the present invention have unexpectedly discovered the optimum balance between viscosity, hardness and dissovability to provide a physically stable and consumer acceptable product.
- The composition of the present invention has a hardness value of from 0.5 to 8 pounds force, preferably from 1.5 to 5.5 peak load. Peak load force can be measured using an Instron Universal Testing Machine fitted with a 100N load cell anda #2830-011 compression anvil. The traveling is at a speed of 1 mm/sec until initial piece fraction occurs.
- The composition of the present invention has a dissolvability in the range of from 0.1 to 8 peak load, preferably from 0.1 to 30 pounds force.
- The composition of the present invention has a viscosity of from 1,000 to 150,000 cp, dependent upon the temperature and speed of the viscometer used to measure the viscosity. In the preferred embodiment, the viscosity of the wet composition ranges from 30,000 to 60,000 cp at a 10 RPM speed of the spindle 6 in a Brookfield Viscometer. The most preferred range is from 35,000 to 50,000 cp. In an alternate embodiment, the present invention has a viscosity of from 1,000 to 700,000 cp, dependent upon the temperature and speed of the viscometer used to measure the viscosity. In the preferred embodiment for the alternate embodiment, the viscosity of the wet composition ranges from 100,000 to 400,000 cp at a 5 RPM speed of the spindle 6 in a Brookfield Viscometer. The most preferred range for the alternate embodiment is from 200,000 to 350,000 cp. It should be noted that the viscosity can be adjusted based on the RPM and is dependent upon dissolvability and the stabilizer.
- Method of Making
- A method of preparing a freeze-dried, aerated, milk product comprising the steps of (a) providing a dairy or dairy substitute blend, (b) adding an emulsifier, (c) thermally processing the dairy or dairy substitute blend, (d) fermenting the blend, (e) admixing a gas with the blend; (f) simultaneously aerating the gas and the dairy or dairy substitute blend to form an aerated product, and (f) cooling the product; and (g) freeze-drying the product.
- Yogurt production:
- 1. Pasteurized lowfat milk is transferred from a tanker truck to large hold tank.
- 2. All dry ingredients (sugar, gelatin, starch, nonfat dry milk, emulsifier, as well as functional ingredients such as prebiotics) are incorporated into milk via addition to a high shear blender (such as Bredo Liqwifier) to achieve homogenous dispersion and initial hydration.
- 3. Once all dry ingredients have been incorporated, the mixture is agitated for 30 minutes at 35-38 deg F.
- 4. Following agitation, the mixture is transferred to the HTST plate heat exchanger for thermal processing. The thermal process conditions used require that all achieve and maintain a minimum temperature of 191 deg F at the end of a 4 5 minutes hold time. This temperature and hold time can vary depending upon the mechanics of the process, for example it is possible to go slightly higher in temperature and have a 7 or 8 minute hold time.
- 5. As an optional step for optimizing the formula and the consistency of aeration, homogenizing of the mixture can occur. The typical homogenization pressures are 2000 to 2500 psi at a first stage and 200-600 psi at a second stage.
- 6. After the hold time at 191 deg F., the mix is cooled to 100-112 deg F., and transferred to the culturing vat. At this point, the yogurt culture is added (for example, a freeze-dried culture, ABY-2C, supplied by Danisco Ingredients, or other vendors). The culture is blended with the pasteurized mix for 30-60 minutes, the mixing is stopped and the vat is maintained at 104-107 deg F. for 4-6 hours. Yogurt is allowed to acidify to pH 4.5 to 4.6, and is then agitated (broken) and cooled to 60 deg F. in the culture tank. Final pH will range from is 4.1-4.4.
- 7. Yogurt is transferred to 250 gal. blending tanks by pumping through a cooling press, which lowers temp to 37-45 deg F. Pasteurized fruit puree, flavors and any desired color will be added. Mixture will be blended with gentle agitation and recirculation for 10-15 minutes. Blended fruit yogurt is transferred to 275 gallon totes.
- Production Frozen Yogurt Drops
- 1. Yogurt will be conveyed/pumped from 275 gallon totes (previously stored at 34-40 deg F.) to the aerator (in this case, a Mondomix aerator, although other brands exist).
- 2. Nitrogen gas is admixed to the yogurt via the Mondo mixer (connected to plant ice water circulation system, to maintain mixing head temperature at 35-45 deg F.). Product overrun can range from 20% to 80%. However, preferably, the overrun target will be between 30% and 50% and most preferably between 35% and 45%. This process happens continuously.
- 3. Aerated yogurt is pumped, maintained at 38-50 deg F., under pressure, to a depositor manifold, where it is distributed to multiple nozzles which, via a metering pump, create the appropriately shaped deposit form (in this case, a large chocolate chip shape, although other shapes/forms are possible). The current target shape has a diameter of 13-22 mm (ideal is 15-20 mm), a height of 7-12 mm (ideal is 8-10), and a weight of 0.8-1.3 grams (ideal is 1.0-1.1 g).
- 4. Drops are deposited onto a solid, stainless steel freezer belt (in this case, the maker of the belt and freezer is Sandvik).
- 5. Freezer tunnel air temperature is approximately −20 to −30 deg F., with high velocity air circulation. Dwell time in the tunnel can range from 3-5 minutes. Frozen pieces exit the tunnel with an internal temperature of 24-28 deg F.
- 6. Products are removed from the freezer belt and conveyed to a bulk case packer, where they are filled into 20-30 lb, plastic bag lined cases. Cases are closed, taped and stored at −20 deg F. until shipment to OFD.
- The following composition of the present invention can be prepared. The percentages listed are based on the total weight of the composition.
- Unflavored yogurt:
-
Percentage Ingredient by weight Low fat milk 82.89 Non-fat dry milk (NFDM) 4 Sugar 9 Starch/Gelatin Stabilizer Blend 3.7 Yogurt Culture + Skim Milk 0.01 Lactem Emulsifier (Lactic Acid Esters of Monoglycerides) 0.4 -
-
Ingredient % of formula Lowfat Milk 78.442148 NFDM Low Heat 3.68628 Sugar, White Satin 8.5068 Starch/Gelatin Stabilizer Blend (0.38% Lactem, 3.87532 1.1% Tapioca Starch, 2.3% gelatin Peach Puree, Single Strength, Frozen, Organic 5 Natural Peach Flavor 0.3 Natural Annatto Extract 0.18 Yogurt Culture 0.009452 TOTAL 100 -
-
Ingredient % of formula Lowfat Milk (1.65% fat) 78.442148 NFDM Low Heat 3.68628 Sugar, White Satin 8.5068 Starch/Gelatin Stabilizer Blend #1795 3.87532 Peach Puree, Single Strength, Frozen, Organic 5 Natural Peach Flavor WONF C13206 0.3 Natural Annatto Extract 1211663 0.18 Yogurt Culture ABY-2C 0.009452 TOTAL 100 - The composition described above is made using the methods described herein.
- It should be appreciated that the present invention is not limited to the specific embodiments described above, but includes variations, modifications and equivalent embodiments defined by the following claims.
Claims (26)
1. A freeze-dried, aerated dairy or dairy substitute composition comprising:
a dairy or dairy substitute ingredient;
an emulsifier; and
a viscosity enhancer,
wherein the dairy composition is pasteurized, has a hardness value from about 0.5 to about 8 pounds of force, and has a dissolvability in a range from about 0.1 to about 8 pounds force peak load.
2. The freeze-dried composition of claim 1 , wherein the emulsifier is selected from the group consisting of lactylated mono and diglycerides, polysorbates, caseinate, whey proteins, egg white protein, and combinations thereof.
3. The freeze-dried composition of claim 1 , wherein the emulsifier is a lactylated mono and diglyceride.
4. The freeze-dried composition of claim 3 , wherein the lactylated mono and di-glycerides are present in an amount of from about 0.001% to about 1% of the composition.
5. The freeze-dried composition of claim 3 , wherein the lactylated mono and diglyceride is selected from the group consisting of lactic acid esters of mono- and di-glycerides, citrate acid esters of mono and diglycerides and distilled monoglycerides.
6. The freeze-dried composition of claim 5 , wherein the lactylated mono and diglyceride is a lactic acid ester of mono glycerides or a blend of mono and diglycerides.
7. The freeze-dried composition of claim 1 further comprising a gelling agent, wherein the gelling agent is gelatin.
8. The freeze-dried composition of claim 1 , wherein the dairy or dairy substitute ingredient is present in an amount of from about 60% to about 98% of the composition.
9. The freeze-dried composition of claim 1 , wherein the viscosity enhancer is selected from the group consisting of starch, hydrocolloids such as carageenan, guar gum, locust bean gum, pectin, and combinations thereof.
10. The freeze-dried composition of claim 1 , wherein the dairy or dairy substitute ingredient is selected from the group consisting of milk, milk powder, yogurt, skim milk, milk proteins, hydrolyzed milk proteins, soy proteins, whey proteins, rice proteins, and combinations thereof.
11. The freeze-dried composition of claim 1 further comprising at least one sugar.
12. The freeze-dried composition of claim 1 , wherein the viscosity of the freeze-dried composition is from about 1000 to about 500,000 cp.
13. The freeze-dried composition of claim 1 further comprising at least one probiotic.
14. A freeze-dried, aerated yogurt composition comprising:
a dairy or dairy substitute ingredient;
an emulsifier; and
a viscosity enhancer,
wherein the yogurt composition has a hardness value from about 0.5 to about 8 pounds of force, and has a dissolvability in a range from about 0.1 to about 8 pounds force peak load.
15. The yogurt composition of claim 14 , wherein the emulsifier is selected from the group consisting of lactylated mono and diglycerides, polysorbates, caseinate, whey proteins, egg white protein, and combinations thereof.
16. The yogurt composition of claim 14 , wherein the emulsifier is a lactylated mono and diglyceride.
17. The yogurt composition of claim 16 , wherein the lactylated mono and di-glycerides are present in an amount of from about 0.001% to about 1% of the composition.
18. The yogurt composition of claim 16 , wherein the lactylated mono and diglyceride is selected from the group consisting of lactic acid esters of mono- and di-glycerides, citrate acid esters of mono and diglycerides and distilled monoglycerides.
19. The yogurt composition of claim 16 , wherein the lactylated mono and diglyceride is a lactic acid ester of mono glycerides or a blend of mono and diglycerides.
20. The yogurt composition of claim 14 further comprising a gelling agent, wherein the gelling agent is gelatin.
21. The yogurt composition of claim 14 , wherein the dairy or dairy substitute ingredient is present in amount of from about 60% to about 98% of the composition.
22. The yogurt composition of claim 14 , wherein the viscosity enhancer is selected from the group consisting of starch, hydrocolloids such as carageenan, guar gum, locust bean gum, pectin, and combinations thereof.
23. The yogurt composition of claim 14 , wherein the dairy or dairy substitute ingredient is selected from the group consisting of milk, milk powder, yogurt, skim milk, milk proteins, hydrolyzed milk proteins, soy proteins, whey proteins, rice proteins, and combinations thereof.
24. The yogurt composition of claim 14 further comprising at least one sugar.
25. The yogurt composition of claim 14 , wherein the viscosity of the yogurt composition is from about 1000 to about 500,000 cp.
26. The yogurt composition of claim 14 further comprising at least one probiotic.
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Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2892269B1 (en) * | 2005-10-26 | 2007-12-21 | Gervais Danone Sa | MICROFOISONNE FRESH DAIRY PACKAGE AND PROCESS FOR PREPARING THE SAME |
CN101707868A (en) * | 2007-05-09 | 2010-05-12 | 雀巢产品技术援助有限公司 | Freeze-dried, aerated dairy products or newborn substitute compositions and preparation method thereof |
US20110300255A9 (en) * | 2007-05-09 | 2011-12-08 | Nestec S.A. | Freeze-dried, dairy or dairy-substitute compositions and methods of using same |
AR066526A1 (en) | 2007-05-09 | 2009-08-26 | Nestec Sa | COMPOSITIONS OF FRUIT OR VEGETABLE AIR AND LIOPHILIZED AND METHODS TO PREPARE |
MX340648B (en) * | 2009-12-17 | 2016-07-08 | Rich Products Corp | Yogurt topping. |
MX344981B (en) * | 2010-07-19 | 2017-01-12 | Nestec Sa | Textured, freeze-dried products and methods for making same. |
CN103260426A (en) | 2010-12-09 | 2013-08-21 | 雀巢产品技术援助有限公司 | Freeze-dried snack product comprising hydrolyzed whole grain |
CN103125597B (en) * | 2011-11-29 | 2014-06-25 | 光明乳业股份有限公司 | Oxygen-enrichment animal milk and preparation method thereof |
AU2013329419B2 (en) * | 2012-10-08 | 2017-03-09 | General Mills, Inc. | Cultured dairy products having excellent freeze/thaw properties |
FI128499B (en) * | 2013-10-17 | 2020-06-30 | Valio Oy | Method for preparing an aerated dairy product |
CN104585329B (en) * | 2013-10-31 | 2017-07-18 | 内蒙古蒙牛乳业(集团)股份有限公司 | A kind of normal temperature solid dairy products and preparation method thereof |
CN104585312B (en) * | 2013-10-31 | 2017-11-03 | 内蒙古蒙牛乳业(集团)股份有限公司 | A kind of normal temperature solid dairy products and preparation method thereof |
MX2017001291A (en) * | 2014-07-28 | 2017-10-02 | Gervais Danone Sa | Pressurized spray device containing a low fat fermented dairy product. |
CN107455481A (en) * | 2017-09-14 | 2017-12-12 | 吉林市广泽乳品有限公司 | One kind freeze-drying molten beans of whey cheese and preparation method thereof |
US11191289B2 (en) | 2018-04-30 | 2021-12-07 | Kraft Foods Group Brands Llc | Spoonable smoothie and methods of production thereof |
US10921058B2 (en) * | 2019-01-27 | 2021-02-16 | Vinamit Usa Llc | Fully automatic convection current vacuum freeze drying method |
US10676797B1 (en) * | 2019-01-27 | 2020-06-09 | Vinamit Usa Llc | Concentrated sugarcane juice powder and method for preparing the same using the convection current freeze drying apparatus |
US10966439B2 (en) * | 2019-01-27 | 2021-04-06 | Vinamit Usa Llc | Concentrated fruit juice powder and method for preparing the same using a non-linear screw press juicer and convection current freeze drying apparatus |
CN110179042A (en) * | 2019-05-28 | 2019-08-30 | 稳健医疗用品股份有限公司 | The method of the frozen dried food product of preparation simulation biscuit and made frozen dried food product |
US20240074469A1 (en) | 2021-01-26 | 2024-03-07 | Societe Des Produits Nestle S.A. | Aerated freeze-dried baby-snack |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5147668A (en) * | 1987-08-21 | 1992-09-15 | Munk Werner Georg | Process of producing a reconstitutable solid lactic acid dried product |
US6361813B1 (en) * | 1998-03-20 | 2002-03-26 | Meiji Seika Kaisha, Ltd. | Freeze-dried foods and process for producing the same |
US7033634B2 (en) * | 2001-09-28 | 2006-04-25 | General Mills, Inc. | Whipped yogurt products and method of preparation |
Family Cites Families (108)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1190044A (en) | 1957-11-04 | 1959-10-08 | Expl Des Ferments Et Produits | Vegetable or fruit powder |
US2955943A (en) * | 1958-12-16 | 1960-10-11 | Jr Arthur I Morgan | Dehydration of fruit and vegetable juices |
DE1149975B (en) | 1959-12-04 | 1963-06-06 | Ledoga Spa | Process for the production of fruit and vegetable juices in powder form |
FI40675B (en) | 1964-11-13 | 1968-12-31 | American Potato Co | |
GB1070060A (en) | 1965-07-29 | 1967-05-24 | Kellog Co | Process for preparing dried fruit products |
US3313032A (en) * | 1966-07-28 | 1967-04-11 | George J Malecki | Freeze-drying process and apparatus |
US3492126A (en) * | 1966-11-09 | 1970-01-27 | Maryland Cup Corp | Soft-frozen whipped aqueous extract concentrate of coffee or tea |
JPS4811568B1 (en) | 1968-10-03 | 1973-04-14 | ||
US3806610A (en) * | 1969-09-11 | 1974-04-23 | Us Army | Method for making a compressed, freeze-vacuum-dehydrated blueberry product of increased density |
FR2079766A6 (en) | 1970-02-12 | 1971-11-12 | Courtaulds Ltd | Knitting on hosiery machines - esp sleeved garments eg pullovers |
FR2079776A5 (en) | 1970-02-12 | 1971-11-12 | Etna | Fruit preservation - with addition of a lyophilisation agent before freeze-drying |
FR2080271A5 (en) | 1970-02-27 | 1971-11-12 | Irab | |
CA994158A (en) * | 1972-02-09 | 1976-08-03 | Rex J. Sims | Protein-free oil in water emulsions |
US4080477A (en) * | 1972-10-23 | 1978-03-21 | Fuji Oil Co., Ltd. | Processed cheese-like product containing soy cheese |
GB1484167A (en) | 1975-11-13 | 1977-09-01 | Kraftco Corp | Milk product |
US4055675A (en) * | 1976-12-13 | 1977-10-25 | The United States Of America As Represented By The Secretary Of Agriculture | Preparation of puffed fruit |
SU800538A1 (en) * | 1978-12-19 | 1981-01-30 | Московский Технологический Ин-Ститут Мясной И Молочной Промыш-Ленности | Method and apparatus for sublimation drying |
JPS55159752A (en) * | 1979-05-31 | 1980-12-12 | Morinaga & Co Ltd | Preparation of solid fermentation milk |
US4244981A (en) * | 1979-05-31 | 1981-01-13 | General Mills, Inc. | Non-dairy, aerated frozen dessert containing citrus juice vesicles |
US4289789A (en) | 1979-06-25 | 1981-09-15 | M P Food Technology, Inc. | Instant yogurt drink composition |
US4427701A (en) | 1980-11-26 | 1984-01-24 | Landwide Foods, Inc. | Frozen yogurt product |
US4386211A (en) * | 1981-08-25 | 1983-05-31 | G. D. Searle & Co. | Anti-ulcer urea compounds |
US4368211A (en) * | 1981-11-23 | 1983-01-11 | General Mills, Inc. | Composition for aerated frozen desserts containing uncooked fruit puree and method of preparation |
CH650647A5 (en) * | 1982-12-10 | 1985-08-15 | Knorr Naehrmittel Ag | STORAGE PRODUCT WHICH CAN BE OPENED TO A DESSERT MOUSSE AND METHOD FOR THE PRODUCTION THEREOF. |
US4624853A (en) * | 1983-02-07 | 1986-11-25 | S. C. Johnson & Son, Inc. | Instant yogurt food product |
CA1209845A (en) | 1983-02-07 | 1986-08-19 | Richard E. Rudin | Instant yogurt food product |
US4515822A (en) * | 1983-08-29 | 1985-05-07 | General Mills, Inc. | Hollow, puffed fruit products and methods of preparation |
US4542035A (en) * | 1984-03-16 | 1985-09-17 | The Pillsbury Company | Stable aerated frozen dessert with multivalent cation electrolyte |
EP0166600A2 (en) | 1984-06-26 | 1986-01-02 | General Foods Corporation | Method for producing freeze-dried strawberry slices |
US4631196A (en) * | 1985-04-15 | 1986-12-23 | Zeller Clifford L | Low calorie dairy product |
JPS6283842A (en) | 1985-10-08 | 1987-04-17 | Sennosuke Tokumaru | Freeze-dried yogurt and production thereof |
US4702923A (en) | 1985-10-08 | 1987-10-27 | Sennosuke Tokumaru | Lyophilized kefir yoghurt health food |
HU195094B (en) | 1985-11-26 | 1988-04-28 | Ferenc Berki | Process for preparing dried fruit with intensive flavour, porous structure particularly from apple fruits |
DE3690664T (en) * | 1985-12-27 | 1988-01-28 | ||
JPH0789854B2 (en) | 1986-07-07 | 1995-10-04 | ハウス食品株式会社 | Manufacturing method of dried cut vegetables |
NL193652C (en) * | 1986-08-19 | 2000-06-06 | Ferrero Ohg | Sweet delicacy and method for its preparation. |
US5000974A (en) * | 1986-11-12 | 1991-03-19 | International Flavors & Fragrances, Inc. | Process of the preparation of fruit, vegetable or spicy aerated foods |
ES2001820A6 (en) | 1986-12-31 | 1988-06-16 | Fruits Secs Puigdellivol S A | Dehydrating and packing of dried fruit |
FR2620904A1 (en) | 1987-09-24 | 1989-03-31 | Deshylaon Cooperative Agricole | Process for drying food products, in particular plant products |
US4851239A (en) * | 1987-09-29 | 1989-07-25 | Kathleen M. Dalziel | Shelf-stable aerosol dispensable yogurt products |
US4948609A (en) | 1988-02-12 | 1990-08-14 | Nabisco Brands, Inc. | Fruit and vegetable dried food product |
US4889730A (en) * | 1988-02-18 | 1989-12-26 | The Procter & Gamble Company | Crisp fruit or vegetable snack product and process |
IT1219663B (en) | 1988-06-20 | 1990-05-24 | Agrofil Coop Sarl | PROCEDURE FOR THE PREPARATION OF A FOOD PRODUCT IN SOLID FORM, BASED ON YOGURT AND / OR MILK AND / OR FRUITS, FREEZE-DRIED, AND RELATED PRODUCT SO OBTAINED |
US5176928A (en) * | 1988-08-04 | 1993-01-05 | The Nutrasweet Company | Reduced calorie diary mix |
US4946697A (en) * | 1988-11-25 | 1990-08-07 | University Of Kentucky Research Foundation | Puffing biological material |
US4956185A (en) * | 1989-04-26 | 1990-09-11 | Milpak Inc. | Instant yogurt composition and process |
NL9001325A (en) | 1990-06-12 | 1992-01-02 | Preservenbedrijf Bv | METHOD FOR PUGGING VEGETABLES, TUBULAR VEGETABLES AND VEGETABLE VEGETABLES AND VEGETABLE VEGETABLES AND PULSES. |
US5093137A (en) * | 1990-10-17 | 1992-03-03 | Shazer Jr William H | Reduced calorie frozen dairy desserts and processes for producing them |
US5518740A (en) * | 1990-12-13 | 1996-05-21 | Innovative Freeze-Drying Products (Ifdp) N.V. | Process for the preparation of yogurt based freeze-dried foodstuffs having a solid shape, and products obtained by said process |
US5143096A (en) * | 1991-02-04 | 1992-09-01 | The Boc Group, Inc. | Method and apparatus for expanding cellular materials |
NZ243986A (en) * | 1992-08-17 | 1997-07-27 | Nekta International Ltd Substi | Dairy substitute whose viscosity increases under shear force, made by filtering and deodourising kiwifruit pulp |
US5342635A (en) * | 1993-05-12 | 1994-08-30 | General Mills, Inc. | Puffed edible foams and high intensity microwave method of preparation |
US5445844A (en) | 1993-08-19 | 1995-08-29 | Electric Power Research Institute | Formulated food containing a freeze concentrated liquid dairy product |
JP3153899B2 (en) * | 1993-09-14 | 2001-04-09 | 森永乳業株式会社 | Whipped yogurt and method for producing the same |
DE69324490T2 (en) * | 1993-10-25 | 1999-12-23 | Skw Biosystems | Stabilizing composition for the production of a viscous, air-containing milk dessert |
US5486372A (en) | 1994-03-08 | 1996-01-23 | Kraft Foods, Inc. | Frozen dairy product containing polyol polyesters |
US5759653A (en) * | 1994-12-14 | 1998-06-02 | Continental Pet Technologies, Inc. | Oxygen scavenging composition for multilayer preform and container |
EP0805629B1 (en) | 1995-01-12 | 1999-04-21 | HAMA Foodservice GesmbH | Food product |
JP3240917B2 (en) | 1995-05-10 | 2001-12-25 | 不二製油株式会社 | Manufacturing method of yogurt and processed yogurt |
US5959128A (en) * | 1996-03-13 | 1999-09-28 | Cargill Incorporated | Method for preparation of purified glycerides and products |
US6030650A (en) | 1996-11-22 | 2000-02-29 | Princeton Nutrition, L.L.C. | Complete nutritional milk compositions and products |
US5820903A (en) | 1997-06-30 | 1998-10-13 | General Mills, Inc. | Calcium fortified yogurt and methods of preparation |
JP4075307B2 (en) | 1998-05-07 | 2008-04-16 | 味の素株式会社 | Manufacturing method of dried instant soups and sauces |
JP3884875B2 (en) | 1999-01-22 | 2007-02-21 | 株式会社 フード インスティテュート インターナショナル | Dried vegetables and method for producing the same |
PT1085816E (en) | 1999-04-13 | 2004-02-27 | Sigma Tau Healthscience Spa | DIETETIC SUPPLEMENT DERIVED FROM FERMENTED MILK FOR THE PREVENTION OF OSTEOPOROSIS |
DE69925807T2 (en) | 1999-04-28 | 2006-05-11 | Société des Produits Nestlé S.A. | A dry and compacted milk product |
US6183803B1 (en) * | 1999-06-11 | 2001-02-06 | Biosante Pharmaceuticals, Inc. | Method for processing milk |
US6596333B1 (en) * | 1999-07-21 | 2003-07-22 | Nestec S.A. | Process for producing aerated frozen products |
JP3650711B2 (en) | 1999-08-03 | 2005-05-25 | 株式会社ヤクルト本社 | Method for producing low fat yogurt and low fat yogurt obtained by the method |
GB9919487D0 (en) * | 1999-08-17 | 1999-10-20 | Nestle Sa | Moulded onfectionery product comprising vegetables |
US6368645B2 (en) | 1999-09-16 | 2002-04-09 | The Pillsbury Company | Reheating tolerant icing composition |
DE19962427A1 (en) * | 1999-12-22 | 2001-07-12 | Nutrinova Gmbh | Encapsulated multifunctional, biologically active food component, process for their production and their application |
WO2001062099A1 (en) | 2000-02-25 | 2001-08-30 | Arthur D. Little, Inc. | Edible product with live and active probiotics |
JP2002034462A (en) | 2000-07-18 | 2002-02-05 | Taiyo Corp | Method for producing frozen yogurt |
US6599555B2 (en) * | 2001-03-08 | 2003-07-29 | Bocabear Foods, Inc. | Process for making a reduced-calorie fruit and/or vegetable spread |
EP1367907B1 (en) * | 2001-03-13 | 2007-02-28 | Kellogg Company | Aerated food component |
US20020192435A1 (en) | 2001-06-14 | 2002-12-19 | Poe William D. | Towel with segregated body part areas |
US6998146B2 (en) * | 2001-09-11 | 2006-02-14 | General Mills, Inc. | Food products and their method of preparation |
JP3747190B2 (en) * | 2001-10-30 | 2006-02-22 | 天野実業株式会社 | Freeze-dried frozen dessert |
DE10154063B4 (en) * | 2001-11-02 | 2013-11-28 | Airbus Operations Gmbh | Double-walled core composite, preferably fiber composite |
US20030194468A1 (en) | 2002-04-12 | 2003-10-16 | Amy Konkoly | Dairy beverage and method of preparation thereof |
US20030211218A1 (en) | 2002-05-13 | 2003-11-13 | Cote Antoine J. | Yogurt production process and products |
EP1369041A1 (en) * | 2002-06-07 | 2003-12-10 | Campina B.V. | Gelatine free dairy dessert |
US7264835B2 (en) * | 2002-08-01 | 2007-09-04 | General Mills, Inc. | Food product and method of preparation |
US20040110442A1 (en) * | 2002-08-30 | 2004-06-10 | Hannong Rhim | Stretchable nonwoven materials with controlled retraction force and methods of making same |
JP4106487B2 (en) | 2002-10-24 | 2008-06-25 | 株式会社日立グローバルストレージテクノロジーズ | Positioning control device |
AU2003285130A1 (en) * | 2002-10-31 | 2004-05-25 | Kellogg Company | Aerated confection containing high levels of fruit solids and method of making same |
US20040086615A1 (en) | 2002-11-04 | 2004-05-06 | Cargill, Inc. & Cerestar Holding Bv | Reduced calorie confectionery compositions |
ITMI20022439A1 (en) | 2002-11-18 | 2004-05-19 | Rimarchio 14 S R L Ora Yogurtal S P A | ICE CREAM YOGURT. |
JP4497446B2 (en) * | 2003-01-27 | 2010-07-07 | 三栄源エフ・エフ・アイ株式会社 | Yogurt and method for producing the same |
JP4217080B2 (en) | 2003-02-07 | 2009-01-28 | 群栄化学工業株式会社 | Process for producing processed fruit, processed fruit and sugar |
GB0312147D0 (en) | 2003-05-27 | 2003-07-02 | Danisco | A composition of lactic acid esters of mono- and diglycerides of fatty acids, an emulsifier containing the same and its use |
JP2005050499A (en) | 2003-07-16 | 2005-02-24 | Sanyo Electric Co Ltd | Optical disk and its disposal method |
JP4183125B2 (en) | 2003-08-01 | 2008-11-19 | 株式会社ブリヂストン | Vulcanizing apparatus having tire take-out device |
US7118772B2 (en) * | 2003-09-18 | 2006-10-10 | General Mills, Inc. | Inulin infused fruit and method of preparation |
WO2005060763A1 (en) | 2003-12-19 | 2005-07-07 | Danisco A/S | Process for the production of a frozen food product |
PL1584241T5 (en) | 2004-04-08 | 2016-02-29 | Nestec Sa | Aerated frozen confections |
WO2006017363A1 (en) | 2004-07-13 | 2006-02-16 | Kellogg Company | Vacuum puffed and expanded fruit |
WO2006099553A2 (en) | 2005-03-15 | 2006-09-21 | Innovative Foods Inc. | Methods for preparing freeze dried foods |
US7569244B2 (en) * | 2005-04-08 | 2009-08-04 | J. Kirk Jordan | Ready-to-eat dry fruit products and process |
US20060286209A1 (en) * | 2005-06-17 | 2006-12-21 | Kraft Foods Holdings, Inc. | Cultured dairy products and methods of manufacture |
ATE422827T1 (en) * | 2005-09-23 | 2009-03-15 | Unilever Nv | PROCESS FOR PRODUCTION OF A FROZEN AND AERATED COMPOSITION |
CN101707868A (en) * | 2007-05-09 | 2010-05-12 | 雀巢产品技术援助有限公司 | Freeze-dried, aerated dairy products or newborn substitute compositions and preparation method thereof |
AR066526A1 (en) | 2007-05-09 | 2009-08-26 | Nestec Sa | COMPOSITIONS OF FRUIT OR VEGETABLE AIR AND LIOPHILIZED AND METHODS TO PREPARE |
JP5386157B2 (en) | 2007-11-30 | 2014-01-15 | 日本エフディ株式会社 | Manufacturing method of freeze-dried molded products |
EP2153730B1 (en) * | 2008-07-30 | 2012-02-01 | Nestec S.A. | Frozen confectionery having high protein and low fat content |
JP5301384B2 (en) | 2009-07-30 | 2013-09-25 | シロキ工業株式会社 | Control device for vehicle opening / closing body |
JP6314658B2 (en) | 2014-05-27 | 2018-04-25 | 株式会社豊田自動織機 | Power storage device |
-
2008
- 2008-05-09 CN CN200880015156A patent/CN101707868A/en active Pending
- 2008-05-09 RU RU2009145539/10A patent/RU2491823C2/en active
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- 2008-05-09 TW TW097117362A patent/TWI486127B/en not_active IP Right Cessation
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- 2008-05-09 US US12/599,321 patent/US20100233317A1/en not_active Abandoned
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- 2009-06-10 US US12/482,252 patent/US10206409B2/en active Active
- 2009-12-08 ZA ZA2009/08722A patent/ZA200908722B/en unknown
-
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- 2012-01-24 US US13/357,357 patent/US20120128829A1/en not_active Abandoned
- 2012-01-24 US US13/357,364 patent/US20120121762A1/en not_active Abandoned
-
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- 2016-03-11 US US15/067,446 patent/US10159261B2/en active Active
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Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5147668A (en) * | 1987-08-21 | 1992-09-15 | Munk Werner Georg | Process of producing a reconstitutable solid lactic acid dried product |
US6361813B1 (en) * | 1998-03-20 | 2002-03-26 | Meiji Seika Kaisha, Ltd. | Freeze-dried foods and process for producing the same |
US7033634B2 (en) * | 2001-09-28 | 2006-04-25 | General Mills, Inc. | Whipped yogurt products and method of preparation |
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BRPI0811302A8 (en) | 2017-02-21 |
CL2008001383A1 (en) | 2009-09-25 |
WO2008141233A1 (en) | 2008-11-20 |
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MX2009012011A (en) | 2010-01-14 |
TW200926988A (en) | 2009-07-01 |
TWI486127B (en) | 2015-06-01 |
EP2154982B1 (en) | 2014-06-04 |
ZA200908722B (en) | 2011-02-23 |
JP2010526538A (en) | 2010-08-05 |
ES2482091T3 (en) | 2014-08-01 |
US10206409B2 (en) | 2019-02-19 |
CA2686582A1 (en) | 2008-11-20 |
US20160316775A1 (en) | 2016-11-03 |
MY148286A (en) | 2013-03-29 |
EP2154982A1 (en) | 2010-02-24 |
RU2009145539A (en) | 2011-06-20 |
PL2154982T3 (en) | 2014-12-31 |
AR066525A1 (en) | 2009-08-26 |
US20090324773A1 (en) | 2009-12-31 |
PT2154982E (en) | 2014-07-24 |
US10143211B2 (en) | 2018-12-04 |
US20100233317A1 (en) | 2010-09-16 |
RU2491823C2 (en) | 2013-09-10 |
CA2686582C (en) | 2014-09-02 |
US20120121762A1 (en) | 2012-05-17 |
AU2008251339B2 (en) | 2011-03-24 |
US10159261B2 (en) | 2018-12-25 |
CN101707868A (en) | 2010-05-12 |
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