WO2005115164A1 - Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point - Google Patents
Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point Download PDFInfo
- Publication number
- WO2005115164A1 WO2005115164A1 PCT/EP2005/002678 EP2005002678W WO2005115164A1 WO 2005115164 A1 WO2005115164 A1 WO 2005115164A1 EP 2005002678 W EP2005002678 W EP 2005002678W WO 2005115164 A1 WO2005115164 A1 WO 2005115164A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- freezing point
- fat
- frozen confection
- confection
- aerated frozen
- Prior art date
- Legal status (The legal status 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 status listed.)
- Ceased
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
- A23L29/10—Foods or foodstuffs containing additives; Preparation or treatment thereof containing emulsifiers
Definitions
- the present invention relates to the field of aerated frozen confections and in particular to aerated frozen confections with decreased freezing point, i.e. products that keep a soft and easy to scoop texture at serving temperatures of - 18° C and below.
- the depression of the freezing point in a frozen aerated dessert is causing a significant increase of the ice crystal growth over heat shock.
- the increase of temperature is causing the melting of the smallest crystal population while a subsequent decrease of temperature is causing an increase in size of the remaining crystals (recrystallisation).
- the mean ice crystal size after 7 days heat shock can vary in a range from 50 ⁇ m to 150 ⁇ m.
- emulsifiers such as saturated or unsaturated mono-di glycerides, distilled monoglycerides or polyoxyethylene esters of sorbitan can help also the reduce the ice crystal size, but not below this value of 50 ⁇ m.
- Frozen confections are traditionally made using ingredients such as: fat, milk solids-not-fat, sweeteners, stabilizers, emulsif ⁇ ers and water. The various ingredients are mixed together, the mixture is then homogenized, pasteurized, cooled, optionally aged at about 2 to 6°C and deep-frozen with stirring with injection of air in a freezer to provide a degree of overrun of the order of 30 to
- Various gums and/or emulsifiers have been used as additives with the aim of improving the stability, the smoothness and the resistance of frozen confections to heat shocks.
- These may include guar gum, carob or guar seed flour, alginate, carboxymethyl cellulose, xanthan, carrageenan, synthetic or natural emulsifiers.
- the milk proteins contained in the milk dry extract participate in this stabilization due to their water-binding property.
- gums has the disadvantage of conferring on the product a texture which is sometimes too firm or gummy.
- EP-A-1 321 043 relates to a frozen aerated ice cream which has a soft structure at - 18° C, contains high amounts of freezing point depressing sugars and contains less than 0.5 % by weight glycerol. Since it is for use with soft serve ice dispensing devices which comprise extrusion of cartridges containing the soft ice cream on the place of consumption, stability after heat shock is not an issue since the consumer would not notice it.
- the problem which the invention proposes to solve consists to control the ice crystal growth in aerated frozen products where the freezing point has been reduced by the addition of sugars with low molecular weight and/or addition of freezing point depressing agents such as polyols or alcohols.
- the present invention consists in a method for regulating the formation and growth of ice crystals in an aerated frozen confection with low freezing point when the confection experiences heat shock, which comprises adding polyol esters of fatty acids (PEFA) alone or in combination with other food grade emulsifiers as primary emulsifier in an amount of at least 0.2 % by weight in the preparation of an aerated frozen confection with improved texture and stability.
- PEFA polyol esters of fatty acids
- a frozen confection preferably may comprise up to 12 % fat, 10 to 25%> of sweeteners, 8 to 10 % of milk solids-not-fat, 0.1 to 0.5 % of stabilizers, at least 0.2 % of propylene glycol monoester of fatty acid as primary emulsifier and water as balance.
- the milk solids-not-fat used for making a frozen confection may be powdered or concentrated defatted sweet whey, for example. They may include powdered or concentrated skim milk, for example. Milk solids-not-fat may also be derived from a commercial mixture of milk powder and whey proteins whose functionality has been modified by specific denaturation treatments.
- the product of the invention comprises sweetener ingredients which are capable of decreasing its freezing point, selected from the group consisiting of sucrose, dextrose, glucose syrup, fructose, polydextrose, inulin and a mixture of these agents, preferably a combination of sucrose, dextrose and glucose syrup, that provide a desired level of sweetness and texture and decrease the freezing point of the mixture.
- a suitable polyol or alcohol can be selected from the group consisting of sorbitol, mannitol, lactilol, xylitol, maltitol, glycerol, ethanol and their mixtures, glycerol and ethanol being preferred.
- the role of polyol is to further soften the frozen confection by making it sufficiently soft to be scoopable at home freezer temperature of - 18° C or less. It is used to increase softness because it reduces ice content with less sweetening effect than sucrose.
- glycerol may be used at a level of 1 to 5 % by weight.
- the fat may be of milk or vegetable origin and its level may be within a broad range. If less fat is used in combination with a freezing point depressing agent, it is then possible to manufacture a cheaper ice cream or an ice cream which is more dietetic with the same softness as a regular high fat ice cream.
- propylene glycol monoester of fatty acid is used as a primary emulsifier in an amount of 0.2 to 0.5 % and most preferably in an amount of at least 0.26 %.
- propylene glycol monostearate/palmitate is used.
- the frozen confections may optionally comprise one additional emulsifier, for example, unsaturated monoglyceride or saturated mono-di glyceride in an amount of at least 5 % of the total emulsifiers, preferably in an amount of 0.04 to 0.16 % by weight as partial replacement of propylene glycol monoester of fatty acid.
- one additional emulsifier for example, unsaturated monoglyceride or saturated mono-di glyceride in an amount of at least 5 % of the total emulsifiers, preferably in an amount of 0.04 to 0.16 % by weight as partial replacement of propylene glycol monoester of fatty acid.
- the frozen confections may comprise stabilizing agents; these may include carob flour, guar flour, alginates, carboxymethyl cellulose, xanthan, carrageenan, gelatin, starches used alone or in the form of a mixture at a dose of 0.1 to 0.5 % by weight, preferably about 0.25 %.
- the formulation of the product in the invention may in addition comprise colourings such as beta-carotene, for example, and/or any type of flavourings or perfumes customarily used to flavour frozen confections, such as vanilla, strawberry or chocolate for example.
- colourings such as beta-carotene, for example, and/or any type of flavourings or perfumes customarily used to flavour frozen confections, such as vanilla, strawberry or chocolate for example.
- compositions used in the invention may optionally comprise additions such as fruit or fruit pieces, for example, or nuts, or hazelnuts, whole or in pieces, for example.
- the organoleptic qualities of the frozen compositions are not reduced compared with the traditional products.
- the characteristics of smoothness and creaminess are increased and in particular, better preserved during the period of storage.
- it is the use of propylene glycol monoester of fatty acid, as emulsifier which makes it possible in addition to reduce remarkably the growth of water crystals in the products subjected to heat shock and thus it confers greater stability to heat shocks on the product.
- the ingredients entering into the composition of a frozen confection may be dispersed at around approximately 60 to 70° C for approximately 15 to 30 min., for example.
- the whole may be heated and homogenized at around 70 to 75° C, for example, at a pressure of the order of 140 to 220 bar, for example.
- the mixture may then be pasteurized according to methods known to persons skilled in the art, for example at around 80 to 90° C for 10 to 30 s.
- the homogenisation-heating step may be carried out at a pasteurization temperature which brings about, on its own, pasteurization of the mixture.
- the mixture may then be cooled to around 2 to 8° C by known means.
- This mixture may then be aged or otherwise for 4 to 24 h at around 2 to 6° C, for example, with or without stirring.
- the mixture may be frozen at around -3 to -8° C, and preferably at about -4.5 to -7.5° C with stirring with injection of gas so as to produce a degree of overrun of the order of 30 to 150 %, for example.
- the mixture obtained may then be hardened by freezing at around -20 to -40° C, for example.
- the frozen compositions may, for example, be extruded in the form of bars having a greater or lesser degree of overrun, with the aid of an ice- cream industry refrigerated scraped surface heat exchanger or freezer with injection of gas.
- the aerated semi-frozen composition coming out of the freezer may also be filled into containers or moulds under pressure using a bottom-up filler, for example.
- Standard heat shock the samples initially stored at -30° C are subjected, for 7 days, to temperature cycles of -8° C/12h followed by -20° C/12h. After 7 days of stabilisation at -30° C, the melting parameters are evaluated for these samples which were subjected to a heat shock. Size of the ice crystals in an ice confection
- An aliquot of ice confection is mixed with an equivalent quantity of glycerol and observed under a microscope at a temperature of -10° C.
- the measurement may be carried out in a chamber at -10° C equipped with microscope and a camera. It is thus possible to measure the mean diameter of the crystals (D o.o) in ⁇ m) in the finished products and in the products which have been subjected to a heat shock (microscope magnification 129).
- the frozen confections exhibit improved stability and organoleptic characteristics compared to traditional products. These products exhibit remarkable reduced ice crystal growth compared with traditional products when submitted to heat shock treatment. This property confers to the product smooth texture, which is considerably preserved after unfavourable storage conditions. Such functionalities make it possible to envisage production, storage and distribution of the products according to the invention extending over time.
- reduced crystal growth is understood to mean an increase in the mean diameter of the ice crystals of less than 50 % after heat shock .
- Example 1 comparative example 1 : use of PEFA in the presence of freezing point depressing sugars
- the objective of these examples is to produce soft aerated frozen confections with freezing point depressing sugars showing texture and sensory attributes which are comparable to a conventional product made with conventional ingredients currently used in the aerated frozen dessert preparation.
- PEFA polyol esters of fatty acids
- PGMS propylene glycol monostearate
- other food-grade emulsifiers such as unsaturated monoglyceride
- the various ingredients are dispersed at 65° C and then undergo a hydration step at 60° C for 20 minutes.
- the mixture is then homogenized at 180 bar with the aid of homogenizer and then pasteurized at 86° C for 32 s.
- After cooling to 4° C the mixture is aged for 24 hours at 4° C, without stirring.
- the mixture is frozen at about -7.5° C draw temperature (example 1) and at about -5.7° C draw temperature (comparative example 1) with a degree of overrun of about 100 %>.
- the ice confection obtained is hardened at -30° C by conventional means.
- Vegetable lauric fat blend Blend of palm and palm kernel oil
- Sweet whey powder whey proteins, non demineralised from Euroserum, 10 to 12
- PGMS Propylene glycol monostearate PGMS SPV® from Danisco;
- UMG Unsaturated monoglyceride DIMODAN UP/B® from Danisco;
- SMDG Saturated Mono-diglycerides: CREMODAN 60 Veg® from Danisco;
- Glucose syrup Glucose MD 40 from Roquette.
- the freezing point achieved in this examples is an average value, to keep a very soft product at a serving temperature below -18° C it can be necessary to decrease the freezing point down to -4.5° C. e.g. by addition of 2.5 % of ethanol (at 98 volume) or 4 % glycerol, based on the total composition of the recipe.
- Table 2 below describes the measured mean ice crystal size of bothe recipes, example 1 and comparative example 1 after heat shock.
- Sample of example 1 which contains a blend of PGMS and UMG has smaller ice crystals and the crystals are significantly more resistant to growth following heat shock treatment compared to the other sample of comparative example 1.
- the heat shock samples were also evaluated for the texture attribute smoothness by a trained testing panel.
- the texture of the product of example 1 was showing a very high smoothness and the aspect was good.
- PEFA polyol esters of fatty acids
- PGMS polyol esters of fatty acids
- other food grade emulsifiers such as unsaturated mono glyceride
Landscapes
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Confectionery (AREA)
Abstract
Description
Claims
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2005247066A AU2005247066A1 (en) | 2004-05-25 | 2005-03-14 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point |
| EP05716024A EP1753300A1 (en) | 2004-05-25 | 2005-03-14 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point |
| BRPI0511493-4A BRPI0511493A (en) | 2004-05-25 | 2005-03-14 | use of polyol fatty acid esters in low freeze-plated frozen preparation |
| JP2007513703A JP2008500031A (en) | 2004-05-25 | 2005-03-14 | Use of fatty acid polyol esters in aerated ice confections with a low freezing point |
| MXPA06013518A MXPA06013518A (en) | 2004-05-25 | 2005-03-14 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point. |
| CA002564157A CA2564157A1 (en) | 2004-05-25 | 2005-03-14 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point |
| IL178630A IL178630A0 (en) | 2004-05-25 | 2006-10-15 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point |
| US11/590,346 US20070042100A1 (en) | 2004-05-25 | 2006-10-30 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP04015026A EP1602283A1 (en) | 2004-05-25 | 2004-05-25 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point |
| EP04015026.0 | 2004-05-25 |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US11/590,346 Continuation US20070042100A1 (en) | 2004-05-25 | 2006-10-30 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2005115164A1 true WO2005115164A1 (en) | 2005-12-08 |
Family
ID=34925493
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2005/002678 Ceased WO2005115164A1 (en) | 2004-05-25 | 2005-03-14 | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US20070042100A1 (en) |
| EP (2) | EP1602283A1 (en) |
| JP (1) | JP2008500031A (en) |
| CN (1) | CN1956661A (en) |
| AU (1) | AU2005247066A1 (en) |
| BR (1) | BRPI0511493A (en) |
| CA (1) | CA2564157A1 (en) |
| IL (1) | IL178630A0 (en) |
| MX (1) | MXPA06013518A (en) |
| RU (1) | RU2006145877A (en) |
| WO (1) | WO2005115164A1 (en) |
| ZA (1) | ZA200610766B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7488504B2 (en) | 2003-12-19 | 2009-02-10 | Danisco A/S | Process for production of a frozen food product |
| US8003151B2 (en) | 2005-07-14 | 2011-08-23 | Conopco, Inc. | Low fat frozen confectionery product |
| US11576397B2 (en) | 2016-02-05 | 2023-02-14 | Conopco, Inc. | Frozen confection |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ATE502527T1 (en) | 2006-11-27 | 2011-04-15 | Palsgaard As | FROZEN FOODS, EMULSIFIER SYSTEMS AND RELATED METHODS |
| BR112013006965A8 (en) | 2010-09-24 | 2018-04-03 | Cargill Inc | COMBINATION OF FAT SUBSTITUTES FOR THE WHOLE OR PARTIAL REPLACEMENT OF FAT IN FOOD PRODUCTS, AND A FOOD PRODUCT COMPRISING THE SAME |
| WO2012093709A1 (en) * | 2011-01-06 | 2012-07-12 | キユーピー 株式会社 | Foam-containing processed food, method for producing same and food using foam-containing processed food |
| US20140079848A1 (en) * | 2011-05-11 | 2014-03-20 | Danone S.A. | Freezable dairy product |
| CN102550793B (en) * | 2011-12-30 | 2014-06-11 | 内蒙古伊利实业集团股份有限公司 | Hard frozen drink as well as production method and extrusion molding method thereof |
| CN102960425B (en) * | 2012-12-11 | 2014-07-16 | 浙江海洋学院 | Method for treating and fresh-keeping sciaenops ocellatus by using acidic electrolyzed water |
| CA2893884C (en) * | 2012-12-20 | 2020-10-20 | Unilever Plc | Frozen aerated confectionary and its manufacturing process |
| JP5536273B1 (en) | 2013-12-27 | 2014-07-02 | 赤城乳業株式会社 | Molded container |
| EP3139763B1 (en) * | 2014-05-08 | 2020-08-12 | Unilever Plc. | Method for manufacturing a frozen confection |
| EP3236771B1 (en) * | 2014-12-22 | 2018-09-26 | Unilever N.V. | Frozen confection |
| JP6243492B1 (en) * | 2016-08-19 | 2017-12-06 | 森永製菓株式会社 | Combined frozen food |
| JP2017013904A (en) * | 2016-10-14 | 2017-01-19 | 赤城乳業株式会社 | Container for frozen confectionery material, frozen confectionery material, eating and drinking method of frozen confectionery material, eating and drinking method |
| CN108157706B (en) * | 2016-12-07 | 2021-04-23 | 内蒙古蒙牛乳业(集团)股份有限公司 | Frozen beverage and preparation method thereof |
| JP6352465B1 (en) * | 2017-02-24 | 2018-07-04 | 森永製菓株式会社 | Frozen food |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3647477A (en) * | 1970-02-10 | 1972-03-07 | Atlas Chem Ind | Surfactant composition for frozen confections |
| US3702768A (en) * | 1969-11-17 | 1972-11-14 | Gen Foods Corp | Low calorie frozen desserts |
| US3968266A (en) * | 1975-10-24 | 1976-07-06 | The Procter & Gamble Company | Low density frozen dessert |
| GB1484167A (en) * | 1975-11-13 | 1977-09-01 | Kraftco Corp | Milk product |
| US4244977A (en) * | 1977-01-28 | 1981-01-13 | Rich Products Corporation | Intermediate-moisture frozen foods |
| EP1321043A1 (en) * | 2001-12-21 | 2003-06-25 | Unilever Plc | Frozen aerated confection |
| US20030134025A1 (en) * | 1999-07-21 | 2003-07-17 | Nestec Sa | Aerated frozen products |
Family Cites Families (43)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US134024A (en) * | 1872-12-17 | Improvement in apparatus for extinguishing fires | ||
| US134025A (en) * | 1872-12-17 | Improvement in pumps | ||
| US2048364A (en) * | 1935-02-20 | 1936-07-21 | Henry J Willems | Combination frozen confection |
| US2587369A (en) * | 1949-05-11 | 1952-02-26 | Lanco Products Corp | Method of adding emulsifying agents to prepared ice cream mixes |
| US2604406A (en) * | 1949-08-02 | 1952-07-22 | Borden Co | Process for stabilizing foodstuff and stabilizing composition |
| US3821442A (en) * | 1970-11-20 | 1974-06-28 | Ashland Oil Inc | Emulsifier for frozen confections |
| US3355300A (en) * | 1963-05-20 | 1967-11-28 | Araxia B Avedikian | Dry ice cream mix composition and a method for producing same |
| US3582357A (en) * | 1969-03-24 | 1971-06-01 | Pillsbury Co | Edible mix composition for producing an aerated product |
| US3673106A (en) * | 1969-06-18 | 1972-06-27 | Kraftco Corp | Emulsifier system |
| US3677443A (en) * | 1969-07-14 | 1972-07-18 | Dca Food Ind | Apparatus for dispensing frozen comestibles |
| US3991224A (en) * | 1973-03-12 | 1976-11-09 | Kraftco Corp | Whipped food product and method for making same |
| US3928648A (en) * | 1974-06-12 | 1975-12-23 | Gen Foods Corp | Method and composition for low ph whipped toppings |
| US3924018A (en) * | 1974-06-14 | 1975-12-02 | Gen Foods Corp | Whipped toppings |
| GB1495750A (en) * | 1974-11-20 | 1977-12-21 | Kraftco Corp | Aerated dessert |
| US3996389A (en) * | 1976-02-25 | 1976-12-07 | General Mills Chemicals, Inc. | Stabilizer blend |
| US4452824A (en) * | 1981-11-10 | 1984-06-05 | Cole Bruce A | Soft, frozen dessert formulation |
| US4431682A (en) * | 1982-06-15 | 1984-02-14 | General Foods Corporation | Frozen aerated creamy frosting and method therefore |
| US4505943A (en) * | 1982-12-02 | 1985-03-19 | General Foods Corporation | Process for making a freeze-thaw stable edible foam containing milk fat |
| US4451492A (en) * | 1982-12-02 | 1984-05-29 | General Foods Corporation | Real cream frozen whipped topping composition |
| US4450182A (en) * | 1982-12-30 | 1984-05-22 | General Foods Corporation | Process for modifying a dairy media for use as a foaming agent |
| US4500553A (en) * | 1983-08-01 | 1985-02-19 | General Foods Corporation | Method of producing a frozen dual-textured confection |
| US4542035A (en) * | 1984-03-16 | 1985-09-17 | The Pillsbury Company | Stable aerated frozen dessert with multivalent cation electrolyte |
| US4828866A (en) * | 1984-12-13 | 1989-05-09 | Olympus Industries, Inc. | Fruit shake and method of making the same |
| US4724153A (en) * | 1985-09-26 | 1988-02-09 | General Foods Corporation | Soft-frozen water-ice formulation |
| US4795650A (en) * | 1986-08-04 | 1989-01-03 | Food Trends, Inc. | Method of making extruded frozen cheesecake product |
| US4988529A (en) * | 1989-03-24 | 1991-01-29 | Nissei Kabushiki Kaisha | Milk shake and manufacturing method thereof |
| US5194281A (en) * | 1989-10-16 | 1993-03-16 | The Procter & Gamble Company | Polyol fatty acid polyesters with reduced trans double bond levels and process for making |
| US5084295A (en) * | 1990-02-02 | 1992-01-28 | The Procter & Gamble Company | Process for making low calorie fat-containing frozen dessert products having smooth, creamy, nongritty mouthfeel |
| US5171602A (en) * | 1990-06-13 | 1992-12-15 | Kraft General Foods, Inc. | Non-fat frozen dairy product |
| US5077076A (en) * | 1990-06-15 | 1991-12-31 | Kraft General Foods, Inc. | Low-fat frozen whipped topping and process therefore |
| US5758571A (en) * | 1990-08-06 | 1998-06-02 | Kateman Family Limited Partnership | Method and apparatus for producing and dispensing aerated or blended fluid products |
| EP0542886B1 (en) * | 1990-08-06 | 1997-10-08 | KATEMAN, Paul | Method and apparatus for producing and dispensing aerated products |
| US5112626A (en) * | 1990-12-31 | 1992-05-12 | The Pillsbury Company | Aerated frozen dessert compositions and products |
| US5175013A (en) * | 1990-12-31 | 1992-12-29 | The Pillsbury Company | Frozen dessert compositions and products |
| EP0506987B1 (en) * | 1991-03-30 | 1995-01-11 | Frisco-Findus Ag | Process and apparatus for producing a frozen confection |
| CA2087648C (en) * | 1992-01-22 | 1998-07-28 | Mamoru Tomita | Ice cream, process for producing the ice cream and apparatus |
| CA2134125A1 (en) * | 1992-04-24 | 1993-11-11 | Christopher Brunsden Holt | Frozen confection |
| CN1042190C (en) * | 1992-12-02 | 1999-02-24 | 尤尼利弗公司 | Frozen confections |
| US5384145A (en) * | 1993-08-19 | 1995-01-24 | Kraft General Foods, Inc. | Low-fat, frozen whipped topping |
| ZA95746B (en) * | 1994-02-04 | 1996-07-31 | Unilever Plc | Ice confections |
| US5486372A (en) * | 1994-03-08 | 1996-01-23 | Kraft Foods, Inc. | Frozen dairy product containing polyol polyesters |
| DE69636931T2 (en) * | 1995-10-31 | 2007-11-15 | Société des Produits Nestlé S.A. | SHAPED CHOCOLATE PARTICLES FOR DISPERSION IN OR DISTRIBUTION ON CONFIGURATED GOODS |
| ATE265149T1 (en) * | 1999-09-18 | 2004-05-15 | Nestle Sa | METHOD FOR PRODUCING ICE CREAM CONFECTS |
-
2004
- 2004-05-25 EP EP04015026A patent/EP1602283A1/en not_active Withdrawn
-
2005
- 2005-03-14 RU RU2006145877/13A patent/RU2006145877A/en not_active Application Discontinuation
- 2005-03-14 EP EP05716024A patent/EP1753300A1/en not_active Withdrawn
- 2005-03-14 CN CNA2005800168336A patent/CN1956661A/en active Pending
- 2005-03-14 MX MXPA06013518A patent/MXPA06013518A/en unknown
- 2005-03-14 CA CA002564157A patent/CA2564157A1/en not_active Abandoned
- 2005-03-14 JP JP2007513703A patent/JP2008500031A/en not_active Withdrawn
- 2005-03-14 BR BRPI0511493-4A patent/BRPI0511493A/en not_active IP Right Cessation
- 2005-03-14 WO PCT/EP2005/002678 patent/WO2005115164A1/en not_active Ceased
- 2005-03-14 AU AU2005247066A patent/AU2005247066A1/en not_active Abandoned
-
2006
- 2006-10-15 IL IL178630A patent/IL178630A0/en unknown
- 2006-10-30 US US11/590,346 patent/US20070042100A1/en not_active Abandoned
- 2006-12-20 ZA ZA200610766A patent/ZA200610766B/en unknown
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3702768A (en) * | 1969-11-17 | 1972-11-14 | Gen Foods Corp | Low calorie frozen desserts |
| US3647477A (en) * | 1970-02-10 | 1972-03-07 | Atlas Chem Ind | Surfactant composition for frozen confections |
| US3968266A (en) * | 1975-10-24 | 1976-07-06 | The Procter & Gamble Company | Low density frozen dessert |
| GB1484167A (en) * | 1975-11-13 | 1977-09-01 | Kraftco Corp | Milk product |
| US4244977A (en) * | 1977-01-28 | 1981-01-13 | Rich Products Corporation | Intermediate-moisture frozen foods |
| US20030134025A1 (en) * | 1999-07-21 | 2003-07-17 | Nestec Sa | Aerated frozen products |
| EP1321043A1 (en) * | 2001-12-21 | 2003-06-25 | Unilever Plc | Frozen aerated confection |
Non-Patent Citations (2)
| Title |
|---|
| DATABASE FSTA [online] INTERNATIONAL FOOD INFORMATION SERVICE (IFIS), FRANkFURT-MAIN, DE; 1977, WIELINGA W C: "Some aspects of stabilization of edible ices.", XP002331392, Database accession no. 78-1-08-p1106 * |
| MARSHALL R. T.; ARBUCKLE W. S.: "Ice Cream", 2000, ASPEN PUBLISHERS, INC., GAITHERSBURG, USA, XP002299661 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7488504B2 (en) | 2003-12-19 | 2009-02-10 | Danisco A/S | Process for production of a frozen food product |
| US8003151B2 (en) | 2005-07-14 | 2011-08-23 | Conopco, Inc. | Low fat frozen confectionery product |
| US11576397B2 (en) | 2016-02-05 | 2023-02-14 | Conopco, Inc. | Frozen confection |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2008500031A (en) | 2008-01-10 |
| ZA200610766B (en) | 2008-09-25 |
| CA2564157A1 (en) | 2005-12-08 |
| US20070042100A1 (en) | 2007-02-22 |
| EP1602283A1 (en) | 2005-12-07 |
| CN1956661A (en) | 2007-05-02 |
| BRPI0511493A (en) | 2008-01-08 |
| RU2006145877A (en) | 2008-06-27 |
| EP1753300A1 (en) | 2007-02-21 |
| MXPA06013518A (en) | 2007-03-01 |
| IL178630A0 (en) | 2007-02-11 |
| AU2005247066A1 (en) | 2005-12-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8425967B2 (en) | Aerated frozen products | |
| US20080050495A1 (en) | Process for manufacturing aerated frozen confections | |
| WO2005115164A1 (en) | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point | |
| EP1597976B1 (en) | Use of polyol esters of fatty acids in aerated frozen confection with improved nutritional attributes | |
| EP1584241B2 (en) | Aerated frozen confections | |
| HK1079660A (en) | Use of polyol esters of fatty acids in aerated frozen confection with decreased freezing point | |
| EP1597975A1 (en) | Use of polyol esters of fatty acids in aerated frozen confection with improved nutritional attributes | |
| HK1079405B (en) | Use of polyol esters of fatty acids in aerated frozen confection with improved nutritional attributes | |
| HK1077710B (en) | Aerated frozen confections | |
| HK1091689A (en) | Process for manufacturing aerated frozen confections |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
| AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
| WWE | Wipo information: entry into national phase |
Ref document number: 2005716024 Country of ref document: EP Ref document number: 2005247066 Country of ref document: AU |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 12006502019 Country of ref document: PH |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 178630 Country of ref document: IL |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 2564157 Country of ref document: CA |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 2007513703 Country of ref document: JP |
|
| ENP | Entry into the national phase |
Ref document number: 2005247066 Country of ref document: AU Date of ref document: 20050314 Kind code of ref document: A |
|
| WWP | Wipo information: published in national office |
Ref document number: 2005247066 Country of ref document: AU |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 11590346 Country of ref document: US |
|
| WWE | Wipo information: entry into national phase |
Ref document number: PA/a/2006/013518 Country of ref document: MX |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 200580016833.6 Country of ref document: CN |
|
| NENP | Non-entry into the national phase |
Ref country code: DE |
|
| WWW | Wipo information: withdrawn in national office |
Ref document number: DE |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 200610766 Country of ref document: ZA |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 2006146440 Country of ref document: RU Ref document number: 2006145877 Country of ref document: RU |
|
| WWP | Wipo information: published in national office |
Ref document number: 2005716024 Country of ref document: EP |
|
| WWP | Wipo information: published in national office |
Ref document number: 11590346 Country of ref document: US |
|
| ENP | Entry into the national phase |
Ref document number: PI0511493 Country of ref document: BR |

