GB2395413A - Stabilised fluid composition comprising suspended particulates - Google Patents

Stabilised fluid composition comprising suspended particulates Download PDF

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Publication number
GB2395413A
GB2395413A GB0227244A GB0227244A GB2395413A GB 2395413 A GB2395413 A GB 2395413A GB 0227244 A GB0227244 A GB 0227244A GB 0227244 A GB0227244 A GB 0227244A GB 2395413 A GB2395413 A GB 2395413A
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United Kingdom
Prior art keywords
component
fluid composition
fluid
hydrocolloid
cellulose ether
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.)
Withdrawn
Application number
GB0227244A
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GB0227244D0 (en
Inventor
Craig Davis
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.)
DuPont Nutrition Biosciences ApS
Danisco US Inc
Original Assignee
Danisco AS
Danisco US Inc
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
Application filed by Danisco AS, Danisco US Inc filed Critical Danisco AS
Priority to GB0227244A priority Critical patent/GB2395413A/en
Publication of GB0227244D0 publication Critical patent/GB0227244D0/en
Publication of GB2395413A publication Critical patent/GB2395413A/en
Withdrawn legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C9/00Milk preparations; Milk powder or milk powder preparations
    • A23C9/152Milk preparations; Milk powder or milk powder preparations containing additives
    • A23C9/154Milk preparations; Milk powder or milk powder preparations containing additives containing thickening substances, eggs or cereal preparations; Milk gels
    • A23C9/1544Non-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
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L29/00Foods or foodstuffs containing additives; Preparation or treatment thereof
    • A23L29/20Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents
    • A23L29/206Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of vegetable origin
    • A23L29/262Cellulose; Derivatives thereof, e.g. ethers
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs

Abstract

A fluid composition comprises (a) a fluid medium, (b) a non-ionic cellulose ether, and (c) a hydrocolloid, wherein the hydrocolloid (c) is different to the non-ionic cellulose ether (b). The fluid composition preferably also comprises a particulate component suspended in the fluid, such as cocoa, fruit pulp, starch granules or mineral salts. The fluid medium (a) is preferably milk and/or fruit juice. The non-ionic cellulose ether component may be methyl cellulose, hydroxypropylmethyl cellulose, hydroxylpropylcellulose, ethylmethylcellulose or mixtures thereof. Examples of hydrocolloids used are alginate, carrageenan, guar gum, microcrystalline cellulose, carboxymethylcellulose, pectin, gelatin and starch. An especially preferred embodiment comprises methyl cellulose, carrageenan and cocoa powder. The particulates are held in suspension even when the fluid is subjected to heating, retorting and cooling without agitation.

Description

23954 1 3
COMPOSITION
The present invention relates to a fluid composition. In particular the invention relates to a fluid composition which may contain or which may be contacted with a particulate 5 component and which will suspend the particulate component.
Fluid products are a major category of food products throughout the world. Dairy and soy-based beverages are important in this category. Milks may be plain or flavoured, with varying fat and protein levels, and may also contain insoluble components that require 10 suspension during processing and storage. These insoluble materials are commonly calcium salts, fibres, and cocoa solids. Heat processing of these fluids may range from pasteurization below 100 C to retorting or ultra-heat treatment (UHT) processing at temperatures up to 145 C.
15 Stabiliser systems are commonly used to provide desired mouthfeel, heat stability to proteins and suspension of insolubles. The stabilisers can also be used to control serum separation in dairy products.
The prior art in providing desired mouthfeel and suspension characteristics is the use of
20 hydrocolloids such as carrageenan, alginate, Microcrystalline cellulose (MCC), carboxymethyl cellulose (CMC), guar gum etc in various combinations. The hydrocolloids provide heat stability, viscosity or weak gel structure to give the required suspension characteristics. Normally this functionality is achieved through heat activation of the hydrocolloids, following by cooling below the gelation temperature to provide a weak gel 25 system which can suspend particulates and also provide improved mouthfeel. The hydrocolloids suspend particulates by providing after activation a weak gel structure. The disadvantage of such a system is that often homogenization is required to activate the hydrocolloids (this is particularly the case with microcrystalline cellulose).
30 Carrageenans are often the hydrocolloid of choice because they can interact with milk proteins to make a gelling system at very low concentrations (less than 0.03% by weight of the milk). MCC has been commonly used in recent years as it can provide suspension without excessive viscosity. However, the disadvantage is that high usage levels are required (say more than 0.3% by weight) which becomes expensive for the processor.
For example, the main difficulties with fluid milk stabilization can be summarised as follows: À Requirement to stabilise milks of varying composition which may be subjected to harsh processing regimes.
5 À Filling and storage temperatures may be adverse for the formation of the necessary weak gel system.
À There are some markets that have retorted (sterilised products) which are subject to very harsh processing (retorting without agitation during processing and cooling).
Often suspension of insolubles is required under conditions where conventional 10 stabilization systems are inadequate or prohibitively expensive.
À There may be interactions of the stabilisers with milk components (proteins, cocoa, calcium salts, etc) leading to undesirable visual, textural and sensory characteristics.
It has become clear from research into stabilization of fluid products requiring suspension 15 and mouthfeel functionality, that no one hydrocolloid is likely to perform all the required functions in fluids to give acceptable stabilization and suspension of insolubles during processing and storage.
Conventional hydrocolloids with gelling functionality often require heat activation to move 20 from an insoluble dispersion to a hydrated form. Most hydrocolloids will not have any gel structure when heated, except for the non-ionic cellulose ethers. The temperature at which gelling, if any, occurs will be characteristic for any particular hydrocolloid. On cooling, some of the hydrocolloids will move to the gelled structure with the formation of junction zones typical for the hydrocolloid type. If there is no mixing of a fluid product 25 containing suspended material at high temperature, then in most cases there will be settling occurring before there has been sufficient cooling to provide a weak gel structure. Conventional processing during HTST or UHT treatment and/or agitated retorting 30 products will provide sufficient agitation to keep insolubles in suspension until the weak gelling structure can be generated.
The present invention alleviates the problems of the prior art.
35 In one aspect the present invention provides a fluid composition comprising (a) a fluid
medium, (b) a non-ionic cellulose ether, (c) a hydrocolloid, wherein hydrocolloid (c) is different to non-ionic cellulose ether (b).
The present composition is based on a two stage stabilization system which can give 5 suspension over a much wider temperature range than conventional stabilization systems. In particular, this system can give stabilization in retorted milks where suspension is required without any agitation during processing.
In a further aspect the present invention provides a process for the preparation of a fluid 10 composition, the process comprising contacting (a) a fluid medium with (b) a non-ionic cellulose ether and (c) a hydrocolloid, wherein hydrocolloid (c) is different to non-ionic cellulose ether (b).
In a further aspect the present invention provides a process according as defined herein 15 for the preparation of a fluid composition as defined herein.
In a further aspect the present invention provides a fluid composition obtainable by or obtained by a process defined herein.
20 In a further aspect the present invention provides use of a combination of (b) a non-ionic cellulose ether and (c) a hydrocolloid for the inhibition of the sedimentation of (d) a particulate component in (a) a fluid medium, wherein hydrocolloid (c) is different to non-
ionic cellulose ether (b).
25 For ease of reference, these and further aspects of the present invention are now discussed in further detail. However, the teachings under each section are not necessarily limited to each particular section.
The fluid composition of the present invention may further contain a particulate 30 component. Thus in one preferred aspect the composition further comprises (d) a particulate component. The particulate component is preferably suspended in the fluid medium. In one alternative the fluid composition may not contain a particulate component - the fluid composition may be combined at later stage with a particulate component which is to be suspended therein.
In one preferred aspect the particulate component which may be present in the fluid composition or may added thereto is selected from cocoa, including cocoa powder, fruit, including fruit pieces and fruit pulp, fibrous material, ungelatinised starch granules, mineral salts and combinations thereof.
s The fluid medium of the present fluid composition may be any fluid material. In one aspect the fluid medium is aqueous or aqueous based. Typically the fluid medium may be based on a beverage. In one preferred aspect the fluid medium is or is based on milk, fruit juice, and combination of fat sources (vegetable or dairy), milk solids, non fat 10 components, fruit juice and water.
In one preferred aspect the non-ionic cellulose ether component (b) is selected from methyl cellulose, hydroxy propyl methyl cellulose, hydroxy propyl cellulose, ethyl methyl cellulose and combinations thereof. These compounds may be known by their"E 1 5 numbers" methyl cellulose - E461 hydroxy propyl methyl cellulose - E464 hydroxy propyi cellulose - E463 ethyl methyl cellulose - E465 In one highly preferred aspect the nonionic cellulose ether component (b) is methyl cellulose. One possible methyl cellulose for use in the present invention is Benecel MC or Benecel M 043 available from Aqualon A/S.
25 In one preferred aspect the hydrocolloid component (c) is selected from alginate, carrageenan, guar gum, gellan gum, locust bean gum (LBG), xanthan gum, microcrystalline cellulose (MCC), carboxymethyl cellulose (CIVIC), pectin, gelatin, agar, starch including native and modified starch, both pregelatinated and non-pregelatinated, including starch from maize, potato, tapioca, wheat, and rice; and combinations thereof.
30 In one highly preferred aspect the hydrocolloid component (c) is carrageenan.
In one preferred aspect the non-ionic cellulose ether component (b) is methyl cellulose and the hydrocolloid component (c) is carrageenan.
In one preferred aspect the hydrocolloid component (c) is polysaccharide material. In one preferred aspect the hydrocolloid component (c) may be obtained or obtainable from seaweed sources, endosperm of seed flour, modified and native starch from potato, tapioca, rice, wheat flour and maize, microbially produced extracellular hydrocolloids, S and/or cellulose derivatives. The hydrocolloid component (c) may be gelatin (refined proteinaceous gelling fraction from animal collagen sources.
In one highly preferred aspect the fluid medium is aqueous, the non-ionic cellulose ether component (b) is methyl cellulose, the hydrocolloid component (c) is carrageenan and 10 the particulate component is cocoa powder. In this aspect the present invention provides a fluid composition comprising an aqueous medium, methyl cellulose, carrageenan and cocoa powder, wherein the cocoa powder is suspended in the aqueous medium.
In one preferred aspect the non-ionic cellulose ether component (b) is present in an IS amount of 20 to 95 wt.%, based on the amount of component (b) and (c).
In one preferred aspect the hydrocolloid component (c) is present in an amount of 95 to 20 wt.%, based on the amount of component (b) and (c).
20 In one preferred aspect the non-ionic cellulose ether component (b) and the hydrocolloid component (c) are present in a ratio of from 20:1 to 1:2.
In one preferred aspect the composition has a pH of from 3 to 8, preferably from 4 to 7.
25 As discussed herein in one aspect the present invention provides a process for the preparation of a fluid composition, the process comprising contacting (a) a fluid medium with (b) a non-ionic cellulose ether and (c) a hydrocolloid.
In one preferred aspect the process comprises the step of contacting the fluid medium 30 with a particulate component.
In one preferred aspect the process comprises the subsequent step of heating the fluid composition. 35 In one preferred aspect the process comprises the subsequent step of retorting the fluid
composition. In one preferred aspect the heating or retorting is performed without agitation of the fluid composition. In this aspect the present invention is particularly advantageous. In many 5 heating and retorting processes, there is a desire to perform the process without agitation. An example of this is the retorting of can containing fluid compositions such as beverages. In typical retorting processes, there may be a mechanism to rotate the cans during heating and cooling steps. However, this adds to complexity and cost of the apparatus. There is therefore a desire to provide apparatus which does not agitate the 10 cans. The present invention provides a two component system which provides stabilization of particulate components at the high temperature of retorting and during the cooing phase (down to storage temperature) after retorting.
In one preferred aspect the process comprises the subsequent step of cooling the fluid 15 composition. Preferably retorting and cooling is performed without agitation of the fluid composition. The fluid composition of the present invention can be prepared, heated and/or retorted in a conventional manner. For example a typical process would include: 20 1. Dispersion of dry components into fluid under high agitation at temperatures from about 20 to 50 C.
2. Heating of the fluid (optional addition of fat sources) 3. Heat pasteurization (batch process, HTST) or UHT sterilization 4. Homogenisation 25 5. Retorting and subsequent cooling At high temperature the non-ionic cellulose ether component (b) is active. On cooling the hydrocolloid component (c) becomes active and the non-ionic cellulose ether component (b) loses its gelling properties. The hydrocolloid component (c) maintains suspension at 30 normal ambient storage conditions.
It is to be appreciated that the product obtainable and/or obtained by the process of the present invention is encompassed by the present invention. Accordingly in further aspects the present invention provides 35 À a composition obtainable by the process of the present invention
À a composition obtained by the process of the present invention À a food product comprising or prepared from a composition obtainable by or obtained by the process of the present invention.
5 The present invention may be used in the preparation of any number of products, in particular food products such as acidifed milk products, flavoured milk products, for example cocoa milk, milk juice (a composition comprising milk and fruit juice) and dressings. 10 The invention will now be described, by way of example only, with reference to the following Example.
E)U\MPLE
15 We prepared a recombined chocolate milk by reconstituting skim milk powder and anhydrous milk fat (clarified butter fat) with addition of cocoa powder, sugar and various stabilisers. Formulation Component % by weight Cocoa 1.0 Sugar 9.2 MSNF 6.0
Anhydrous milk fat 2.65 _ Stabiliser As required Water to 100% The milk was processed by dispersion of dry powders at 40 to 50 C, heat processing to 90 C (holding for 30 minutes), homogenization at 70 to 75 C at 200 Bar pressure, cooling to 27 C, filling into clear glass bottles (250 mL), retorting at 119 C/15 minutes, cooling to two different temperatures with and without agitation, storage at ambient 25 temperature (about 20- 25 C).
The table below shows comparative data of the current invention stabiliser system versus conventional carrageenan stabilization. The data clearly show the improved
functionality of the present invention.
Stabilisers used Formulation Composition A (i) 90.9 /0 Benecel M043 methylcellulose (ii) 9.1 % carrageenan blend consisting of 50% Benlacta PT200* and 50% Benlacta S 100* Usage rate: 0.165% _ _ B (i) 90.9% Tylopur MH4000P** methylhydroxyethylcellulose (ii) 9.1 % carrageenan blend consisting of 50% Benlacta PT200* and 50% Benlacta S 100* Usage rate: 0. 165% C (i) 90.9 % Neo-C11 microcrystalline cellulose *** (ii) 9.1 % carrageenan blend consisting of 50% Benlacta PT200* and 50% Benlacta S 100* Usage rate: 0.22 * available from Shemberg 5 ** available from Clariant *** available from Mingtai Results Property Formulation C Usage rate (% 0.165 0.165 0.165 0.165 0.22 0.22 by weight) Cooling regime a b a B a b Viscosity (cP) 13.0 NT 26.5 NT 16 9 NT Cocoa None None None Trace Heavy None sedimentation Coagulation None None None None Slight Slight _ moderate Whey None Slight None Slight None Moderate separation feathering feathering Homogeneity 1 1.5 1.5 1.5 4.5 3.5 when mixed after storage
a Key Cooling regime: a, cooled without agitation to 25 C then stored at room temperature; b, cooled with periodic agitation to 40 C then stored at room temperature.
Viscosity: single point value at a shear rate of 52.8 s' using Brookfield LVT viscometer and
5 small sample adaptor geometry, measured at 25 C.
Cocoa sedimentation: None, no evidence of any settling; trace, the very slightest evidence of settling; heavy, very discrete, thick layer of cocoa visible from the side of the container.
À Coagulation: Evidence of any inhomogeneity in terms of particulated material in the milk.
Whey separation: Evidence of an upper layer of milkiness or wateriness above the chocolate 10 milk. Homogeneity after mixing: Rating of how well sediment disperses or how homogeneous is the milk when mixed after storage - 1, fully homogeneous; 2, almost homogeneous; 3, all sediment off the bottom of the container but not homogeneous; 4, half the sediment off the bottom; 5, none of the sediment off the bottom.
15 NT - not tested We have observed the complete suspension of cocoa solids in retorted chocolate milk using the present dual functionality system under the most adverse heating and cooling sterilization regime of no agitation. These milks also had excellent sensory 20 characteristics. In comparison, the conventional system had a substantially inferior suspension functionality.
All publications mentioned in the above specification are herein incorporated by
25 reference. Various modifications and variations of the described methods and system of the invention will be apparent to those skilled in the art without departing from the scope and spirit of the invention. Although the invention has been described in connection with specific preferred embodiments, it should be understood that the invention as claimed should not be unduly limited to such specific embodiments. Indeed, various 30 modifications of the described modes for carrying out the invention which are obvious to those skilled in chemistry or related fields are intended to be within the scope of the
following claims.

Claims (1)

1. A fluid composition comprising (a) a fluid medium 5 (b) a non-ionic cellulose ether (c) a hydrocolloid wherein hydrocolloid (c) is different to non-ionic cellulose ether (b).
2. A fluid composition according to claim 1 wherein the composition further 10 comprises (d) a particulate component, wherein the particulate component is suspended in the fluid medium.
3. A fluid composition according to claim 2 wherein the particulate component is selected from cocoa, including cocoa powder, fruit, including fruit pieces and fruit pulp, 15 fibrous material, ungelatinised starch granules, mineral salts and combinations thereof.
4. A fluid composition according to claim 1 or 3 wherein the fluid medium is aqueous. 20 5. A fluid composition according to claim 4 wherein the fluid medium is or is based on milk and/or fruit juice.
6. A fluid composition according to any one of claims 1 to 5 wherein the non-ionic cellulose ether component (b) is selected from methyl cellulose, hydroxy propyl methyl 25 cellulose, hydroxy propyl cellulose, ethyl methyl cellulose and combinations thereof.
7. A fluid composition according to claim 6 wherein the non-ionic cellulose ether component (b) is methyl cellulose.
30 8. A fluid composition according to any one of claims 1 to 7 wherein the hydrocolloid component (c) is selected from alginate, carrageenan, guar gum, gellan gum, locust bean gum (LBG), xanthan gum, microcrystalline cellulose (MCC), carboxymethyl cellulose (CMC), pectin, gelatin, agar, starch including native and modified starch, both pregeiatinated and non-pregelatinated, including starch from maize, potato, tapioca, 35 wheat, and rice; and combinations thereof.
9. A fluid composition according to any one of claims 1 to 7 wherein the hydrocolloid component (c) is a polysaccharide or a protein.
5 10. A fluid composition according to claim 8 wherein the hydrocolloid component (c) is carrageenan.
11. A fluid composition according to claim 2 wherein the fluid medium is aqueous, the non-ionic cellulose ether component (b) is methyl cellulose, the hydrocolloid component 10 (c) is carrageenan and the particulate component is cocoa powder.
12. A fluid composition according to any one of claims 1 to 11 wherein the non-ionic cellulose ether component (b) is present in an amount of 20 to 80 wt.% based on the amount of component (b) and (c).
13. A fluid composition according to any one of claims 1 to 12 wherein the hydrocolloid component (c) is present in an amount of 80 to 20wt.% based on the amount of component (b) and (c).
20 14. A fluid composition according to any one of claims 1 to 13 wherein the non-ionic cellulose ether component (b) and the hydrocolloid component (c) are present in a ratio of from 1:0.5 to 1:2.0 15. A fluid composition according to any one of claims 1 to 14 wherein the 25 composition has a pH of from 3 to 8.
16. A process for the preparation of a fluid composition, the process comprising contacting (a) a fluid medium with (b) a non-ionic cellulose ether and (c) a hydrocolloid, wherein hydrocolloid (c) is different to non-ionic cellulose ether (b).
17. A process according to claim 16 comprising the step of contacting the fluid medium with a particulate component.
18. A process according to claim 16 or 17 comprising the subsequent step of heating 35 the fluid composition.
19. A process according to claim 16, 17 or 18 comprising the subsequent step of retorting the fluid composition.
5 20. A process according to claim 18 or 19 wherein the heating or retorting is performed without agitation of the fluid composition.
21. A process according to claim 19 comprising the subsequent step of cooling the fluid composition.
22. A process according to claim 21 wherein the retorting and cooling is performed without agitation of the fluid composition.
23. A process according to any one of claims 16 to 22 for the preparation of a fluid 15 composition as defined in any one of claims 1 to 15.
24. A fluid composition obtainable by or obtained by the process of any one of claims 16 to 23.
20 25. Use of a combination of (b) a non-ionic cellulose ether and (c) a hydrocolloid for the inhibition of the sedimentation of (d) a particulate component in (a) a fluid medium, wherein hydrocolloid (c) is different to non-ionic cellulose ether (b).
26. Use according to claim 25 wherein the non-ionic cellulose ether component (b), 25 the hydrocolloid component (c), the particulate component and/or the fluid medium are as defined in any one of claims 3 to 15.
27. A composition as substantially hereinbefore described with reference to the Example.
28. A process as substantially hereinbefore described with reference to the Example.
29. Use as substantially hereinbefore described with reference to the Example.
GB0227244A 2002-11-21 2002-11-21 Stabilised fluid composition comprising suspended particulates Withdrawn GB2395413A (en)

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WO2007038745A1 (en) * 2005-09-28 2007-04-05 Hercules Incorporated Cream compositions and food foams made therefrom
WO2007134283A2 (en) * 2006-05-15 2007-11-22 Pepsico, Inc. Stabilizer for dairy products
GB2448497A (en) * 2007-04-17 2008-10-22 Perfect Polymers Systems Ltd A dry composition for forming into a meringue or a frozen dessert
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US8697169B2 (en) 2004-09-20 2014-04-15 Carlton And United Beverages Limited Methods and compositions for fining beverages
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US8801847B2 (en) 2002-05-14 2014-08-12 Fmc Corporation Microcrystalline cellulose compositions
US7871468B2 (en) 2002-05-14 2011-01-18 Fmc Corporation Microcrystalline cellulose compositions
US8697169B2 (en) 2004-09-20 2014-04-15 Carlton And United Beverages Limited Methods and compositions for fining beverages
WO2006102051A1 (en) * 2005-03-17 2006-09-28 Hercules Incorporated Process of reducing fouling during heat processing of foods and beverages
WO2007038745A1 (en) * 2005-09-28 2007-04-05 Hercules Incorporated Cream compositions and food foams made therefrom
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WO2007134283A3 (en) * 2006-05-15 2008-01-10 Pepsico Inc Stabilizer for dairy products
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CN101816329A (en) * 2010-05-20 2010-09-01 厦门欧凯科技有限公司 Suspension stabilizer for fruit milk
CN101816329B (en) * 2010-05-20 2013-03-13 厦门欧凯科技有限公司 Suspension stabilizer for fruit milk
US9055757B2 (en) 2011-10-05 2015-06-16 Fmc Corporation Stabilizer composition of co-attrited microcrystalline cellulose and carboxymethylcellulose, method for making, and uses
US9826763B2 (en) 2011-10-05 2017-11-28 Fmc Corporation Stabilizer composition of microcrystalline cellulose and carboxymethylcellulose, method for making, and uses
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