US20100233317A1 - 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 PDF

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Publication number
US20100233317A1
US20100233317A1 US12/599,321 US59932108A US2010233317A1 US 20100233317 A1 US20100233317 A1 US 20100233317A1 US 59932108 A US59932108 A US 59932108A US 2010233317 A1 US2010233317 A1 US 2010233317A1
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United States
Prior art keywords
dairy
freeze
composition
mono
milk
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Abandoned
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US12/599,321
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English (en)
Inventor
Scott Peterson
Frank Welch
Thomas Burkholder
Norman Jager
Giovanna Aleman
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nestec SA
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Nestec SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
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Priority to US12/599,321 priority Critical patent/US20100233317A1/en
Assigned to NESTEC S.A. reassignment NESTEC S.A. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ALEMAN, GIOVANNA, BURKHOLDER, TOM, JAGER, NORM, PETERSON, SCOTT, WELCH, FRANK
Assigned to NESTEC S.A. reassignment NESTEC S.A. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BURKHOLDER, THOMAS, PETERSON, SCOTT, WELCH, FRANK, ALEMAN, GIOVANNA, JAGER, NORMAN
Publication of US20100233317A1 publication Critical patent/US20100233317A1/en
Abandoned legal-status Critical Current

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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 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 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 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 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 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 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 any one 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 B and 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 monoglycerides, 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 corn 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 corn 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
  • gelatins such as porcine, fish and bovine.
  • 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 and a #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.
  • All dry ingredients sucgar, gelatin, starch, nonfat dry milk, emulsifier, as well as functional ingredients such as prebiotics
  • a high shear blender such as Bredo Liqwifier
  • the mixture is agitated for 30 minutes at 35-38 deg F.
  • 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.
  • 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. 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.
  • 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. 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.
  • 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)
US12/599,321 2007-05-09 2008-05-09 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof Abandoned US20100233317A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US12/599,321 US20100233317A1 (en) 2007-05-09 2008-05-09 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US91694907P 2007-05-09 2007-05-09
PCT/US2008/063312 WO2008141233A1 (en) 2007-05-09 2008-05-09 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof
US12/599,321 US20100233317A1 (en) 2007-05-09 2008-05-09 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof

Related Parent Applications (1)

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PCT/US2008/063312 A-371-Of-International WO2008141233A1 (en) 2007-05-09 2008-05-09 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof

Related Child Applications (1)

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US15/067,446 Continuation US10159261B2 (en) 2007-05-09 2016-03-11 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof

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ID=39540532

Family Applications (6)

Application Number Title Priority Date Filing Date
US12/599,321 Abandoned US20100233317A1 (en) 2007-05-09 2008-05-09 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof
US12/482,252 Active 2033-02-11 US10206409B2 (en) 2007-05-09 2009-06-10 Freeze-dried, dairy or dairy-substitute compositions and methods of making and using
US13/357,364 Abandoned US20120121762A1 (en) 2007-05-09 2012-01-24 Freeze-dried, dairy or dairy-substitute compositions and methods of making and using
US13/357,357 Abandoned US20120128829A1 (en) 2007-05-09 2012-01-24 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof
US15/067,446 Active 2029-09-08 US10159261B2 (en) 2007-05-09 2016-03-11 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof
US15/207,926 Active 2028-06-03 US10143211B2 (en) 2007-05-09 2016-07-12 Freeze-dried, dairy or dairy-substitute compositions and methods of making and using

Family Applications After (5)

Application Number Title Priority Date Filing Date
US12/482,252 Active 2033-02-11 US10206409B2 (en) 2007-05-09 2009-06-10 Freeze-dried, dairy or dairy-substitute compositions and methods of making and using
US13/357,364 Abandoned US20120121762A1 (en) 2007-05-09 2012-01-24 Freeze-dried, dairy or dairy-substitute compositions and methods of making and using
US13/357,357 Abandoned US20120128829A1 (en) 2007-05-09 2012-01-24 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof
US15/067,446 Active 2029-09-08 US10159261B2 (en) 2007-05-09 2016-03-11 Freeze-dried, aerated dairy or dairy-substitute compositions and methods of making thereof
US15/207,926 Active 2028-06-03 US10143211B2 (en) 2007-05-09 2016-07-12 Freeze-dried, dairy or dairy-substitute compositions and methods of making and using

Country Status (18)

Country Link
US (6) US20100233317A1 (de)
EP (1) EP2154982B1 (de)
JP (1) JP2010526538A (de)
CN (1) CN101707868A (de)
AR (1) AR066525A1 (de)
AU (1) AU2008251339B2 (de)
BR (1) BRPI0811302A8 (de)
CA (1) CA2686582C (de)
CL (1) CL2008001383A1 (de)
ES (1) ES2482091T3 (de)
MX (1) MX2009012011A (de)
MY (1) MY148286A (de)
PL (1) PL2154982T3 (de)
PT (1) PT2154982E (de)
RU (1) RU2491823C2 (de)
TW (1) TWI486127B (de)
WO (1) WO2008141233A1 (de)
ZA (1) ZA200908722B (de)

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US20090220644A1 (en) * 2005-10-26 2009-09-03 Sophie Vaslin Nee Reimann Microfoamed fresh dairy product and method for making same
US20170215448A1 (en) * 2014-07-28 2017-08-03 Compagnie Gervais Danone Pressurized spray device containing a low fat fermented dairy product

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ES2727417T3 (es) 2007-05-09 2019-10-16 Nestle Sa El uso de una composición de fruta o de verdura en un procedimiento para la preparación de un producto liofilizado, aireado, de fruta o de verdura
US20110300255A9 (en) * 2007-05-09 2011-12-08 Nestec S.A. Freeze-dried, dairy or dairy-substitute compositions and methods of using same
EP2154982B1 (de) * 2007-05-09 2014-06-04 Nestec S.A. Gefriergetrocknete, lufthaltige milch- oder milchersatzzusammensetzungen und herstellungsverfahren derselben
CN102791138B (zh) 2009-12-17 2016-06-15 里奇产品有限公司 酸奶顶料
ES2619589T3 (es) * 2010-07-19 2017-06-26 Nestec S.A. Productos liofilizados texturizados y métodos para su obtención
MX352901B (es) 2010-12-09 2017-12-13 Nestec Sa Productos de bocadillo liofilizados que comprenden grano entero hidrolizado.
CN103125597B (zh) * 2011-11-29 2014-06-25 光明乳业股份有限公司 富氧动物乳及其制造方法
WO2014058873A2 (en) * 2012-10-08 2014-04-17 General Mills, Inc. Cultured dairy products having excellent freeze/thaw properties
FI128499B (en) * 2013-10-17 2020-06-30 Valio Oy Method for making a foamed dairy product
CN104585329B (zh) * 2013-10-31 2017-07-18 内蒙古蒙牛乳业（集团）股份有限公司 一种常温固体乳制品及其制备方法
CN104585312B (zh) * 2013-10-31 2017-11-03 内蒙古蒙牛乳业（集团）股份有限公司 一种常温固体乳制品及其制备方法
CN107455481A (zh) * 2017-09-14 2017-12-12 吉林市广泽乳品有限公司 一种冷冻干燥乳清奶酪溶豆及其制备方法
US11191289B2 (en) 2018-04-30 2021-12-07 Kraft Foods Group Brands Llc Spoonable smoothie and methods of production thereof
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
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
CN110179042A (zh) * 2019-05-28 2019-08-30 稳健医疗用品股份有限公司 制备模拟饼干的冻干食品制品的方法及所制冻干食品制品
US20240074469A1 (en) 2021-01-26 2024-03-07 Societe Des Produits Nestle S.A. Aerated freeze-dried baby-snack

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