FROZEN AERATED CONFECTIONERY PRODUCT AND A METHOD FOR PREPARING SUCH A PRODUCT

Abstract

The present invention relates to a method for preparing an aerated frozen confectionery product, preferably ice cream. A further aspect of the present invention further relates to an aerated frozen confectionery product obtainable by said method and to the use of an ingredient mix for preparing an aerated frozen confectionery product.

Claims

1.-19. (canceled)

20. A method for preparing an aerated frozen confectionery product, comprising: (a) providing an ingredient mix, comprising: (i) 1 to 15% by weight fat; (ii) 5 to 40% by weight carbohydrates; (iii) 0.1 to 5% by weight of a stabilizer and/or emulsifier; (iv) 0.1 to 1.5% by weight protein, whereof at least 30% by weight is caseinate; (b) pasteurizing and homogenizing the ingredient mix; (c) ripening the ingredient mix of step (b) for at least one hour at a temperature between 0 and 100 C.; (d) freezing while aerating the ingredient mix of step (c) up to an overrun of 75 to 150%; and (e) hardening the frozen aerated ingredient mix.

21. The method according to claim 20, wherein the ripening is for 3 to 24 hours at a temperature between 0 and 100 C.

22. The method according to claim 20, wherein the hardening by freezing to a temperature of 180 C. or lower.

23. The method according to claim 20, wherein on a weight basis the ratio fat to protein in the ingredient mix of step (a) is 5 or higher.

24. The method according to claim 23, wherein on a weight basis the ratio fat to protein in the ingredient mix of step (a) is 10 or higher.

25. The method according to claim 20, wherein the ingredient mix of step (a) comprises 0.25 to 1.25% by weight protein.

26. The method according to claim 20, wherein the ingredient mix of step (a) at least 95% by weight of the total amount of protein is caseinate.

27. The method according to claim 20, wherein the protein in the ingredient mix of step (a) further comprises skim milk powder, nonfat dry milk solids and/or whey protein.

28. The method according to claim 20, wherein the ingredient mix of step (a) comprises 3 to 12% by weight fat.

29. The method according to claim 20, wherein the fat comprises vegetable fat, animal fat or a combination thereof.

30. The method according to claim 20, wherein the stabilizer comprises locust bean gum, guar gum, carrageenan, microcrystalline cellulose, carboxymethylcellulose, pectin, gelatin, gum Arabic, gellan gum, xanthan gum, modified starch, alginate, gum ghatti, gum karaya, gum konjac, agar-agar, oat or a combination thereof.

31. The method according to claim 20, wherein the emulsifier comprises mono- and diglycerides of fatty acids, lactic acid esters of mono- or diglycerides (LACTEM), acetic acid esters of mono- or diglycerides (ACETEM), diacetyltartaric acid esters of mono- and diglycerides (DATEM), sucrose esters of fatty acids, polyglycerol esters of fatty acids, polyoxyethylene sorbitan fatty acid mono-esters, sodium stearoyl lactylate, calcium stearoyl lactylate, propylene glycol monostearate, lecithin, lysolecithin, phospholipoproteins, egg yolk or mixtures thereof.

32. An aerated frozen confectionery product obtainable by the method according to claim 20.

33. An aerated frozen confectionery product having an overrun of 75 to 150%, comprising: (i) 1 to 15% by weight fat; (ii) 5 to 40% by weight carbohydrates; (iii) 0.1 to 5% by weight stabilizer and/or emulsifier; (iv) 0.1 to 1.5% by weight protein, wherein at least 30% by weight of the total amount of protein is caseinate.

34. The aerated product according to claim 33, wherein on a weight basis the ratio fat to protein is 5 or higher.

35. The aerated product according to claim 34, wherein on a weight basis the ratio fat to protein is 10 or higher.

36. The aerated product according to claim 33, comprising 0.25 to 1.25% by weight protein.

37. The aerated product according to claim 33, wherein the product comprises 3 to 12% by weight fat and 0.25 to 1.25% by weight protein of which at least 90% by weight is caseinate, and has total solids content between 35 and 40% by weight and a ratio fat to protein is 5 or higher.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0043] A first aspect of the present invention relates to a method for preparing an aerated frozen confectionery product, comprising the steps of: [0044] a) providing an ingredient mix, which mix comprises: [0045] 1 to 15% by weight fat; [0046] 5 to 40% by weight carbohydrates; [0047] 0.1 to 5% by weight of a stabilizer and/or emulsifier; [0048] 0.1 to 1.5% by weight protein, whereof at least 30% by weight is caseinate; [0049] b) pasteurizing and homogenizing the ingredient mix; [0050] c) ripening the ingredient mix of step b) for at least one hour at a temperature between 0 and 10 C.; [0051] d) freezing while aerating the ingredient mix of step c) up to an overrun of 75 to 150%; [0052] e) hardening the frozen aerated ingredient mix.

[0053] With respect to the above mentioned method it is noted that in step b), pasteurizing and homogenizing may be carried out in any order.

[0054] In the art, an amount of about 3% protein (normally added as skim milk powder and/or whey proteins) is regarded as a typical protein amount in these types of products. Hence, it has never been contemplated to significantly further reduce the protein content as it was believed it would lead to inferior products or cumbersome processing of the ingredient mix during preparation.

[0055] However, with the method according to the present invention it has now become possible to prepare an aerated frozen confectionery product which has very good sensorial properties, excellent melting properties and a good heat shock stability, but which comprises an exceptionally low amount of protein compared to frozen aerated confectionery products known in the art. One of the advantages of the method of the present invention is thus that the costs for preparing such products can be reduced significantly.

[0056] It has remarkably been found that the total amount of protein in the ingredient mix of step a) may range between 0.1 to 1.5% by weight. Preferably, the total amount of protein in the ingredient mix used in the method of the present invention ranges between 0.25 to 1.25%, more preferably between 0.4 to 1.2% by weight, most preferably 0.5 to 1.0% by weight.

[0057] Despite the very low amount of protein which is used in the ingredient mix of the method of the present invention, the physical and sensorial properties of the products prepared therewith are not compromised. In this regard it is noted that the present inventors have found that it is possible to use relatively low amounts of protein in the ingredient mix of step a), if a considerable part of the proteins present in said mix are caseinate proteins. According to the present invention, at least 30% by weight of the total amount of protein present in said ingredient mix are caseinate proteins, however a larger proportion of caseinate proteins may also be used.

[0058] Hence, preferably at least 50%, more preferably at least 80%, and even more preferably 95% by weight of the total amount of proteins in said ingredient mix may be caseinate proteins. The other proteins present in said ingredient mix may originate from skim milk powder, non-fat dry milk solids and/or may be whey proteins.

[0059] It is further noted that it is particularly preferred to use caseinate salts, such as sodium caseinate or calcium caseinate in the ingredient mix of step a) of the method according to the present invention. Sodium caseinate is particularly preferred.

[0060] Caseinate salts are commonly available to the person skilled in the art. They are prepared by dissolving acid-precipitated casein in alkali (e.g., NaOH, KOH, NH4OH, Ca(OH).sub.2, and Mg(OH).sub.2), and spray drying or roller drying the resulting solution. Sodium caseinate is the most common product, although potassium caseinate and calcium caseinate are also commonly used. A range of caseinates is available from FrieslandCampina DMV, The Netherlands.

[0061] As a source for caseinate, so called converted casein may also be used. The term converted casein is known in the art and relates to casein generally in dry form and in addition to casein it also contains an alkali metal salt; when converted casein is dissolved in an aqueous medium, the casein is converted into the corresponding caseinate by the alkali metal salt.

[0062] For preparing a frozen aerated confectionery product with a good quality but with a relatively low protein content, the ratio fat to protein in the ingredient mix of step a) from which the frozen aerated product has been prepared, is also of importance. The inventors of the present invention have found that a very good frozen aerated confectionery product can be prepared if on a weight basis the ratio fat to protein in the ingredient mix of step a) is preferably 5 or higher. In products wherein the total amount of protein is relatively low, such as 1% by weight or lower, the ratio fat to protein on a weight basis is preferably 5 or higher and more preferably 10 or higher.

[0063] Without wishing to be bound by any theory, it is assumed that if protein comprising caseinate is dosed at regular, conventional concentrations, emulsion droplets stabilized with caseinate are too well stabilized to allow a sufficient level of churning of the fat droplets during the combined freezing and aeration of the ingredient mix. However, at a lower dosage of protein comprising caseinate (higher fat-protein ratio) a sufficient level of churning is allowed, resulting in a frozen aerated product, such as ice cream, with the required sensory properties.

[0064] In step c) of the method of the present invention, the ingredient mix obtained in step b) is preferably ripened for 3 to 24 hours at a temperature between 0 and 10 C. During such ripening the ingredient mix (emulsion) is sensitized to churning by partial desorption of protein from the fat droplets. This has an important effect on the stability of the aerated product formed in the subsequent steps. The hardening of the frozen aerated ingredient obtained in step d) is carried out in order to rapidly adjust the temperature of the product to retain its shape and to give it sufficient shelf life with respect to chemical and enzymatic reactions, as well as to the physical structure. Hardening is preferably carried out at a temperature below 18 C., more preferably below 30 C., even more preferably below 35 C. It is particularly preferred to pass the product prepared, such as packaged ice cream, through a so called hardening-tunnel, in which very cold air (e.g. 35 C.) is blown over the product.

[0065] The temperature of the frozen aerated product prepared with the method according to the present invention before consumption is lower than 5 C., preferably lower than 10 C.

[0066] Furthermore, the ingredient mix of step a) of the method of the present invention typically comprises between 50 and 70% by weight water. Hence, a considerable part of the water present in the product according to the present invention will be in frozen state.

[0067] The method according to the present invention is particularly suitable for making mainstream types of aerated frozen confectionery products, such as ice cream. In these types of products the amount of protein is already fairly low and further reducing the amount of protein has been considered impossible. The overrun of these products preferably range between 75 and 120%, although the overrun may be as high as 150%.

[0068] The fat used in the preparation of the frozen aerated products of the present invention, such as ice cream, may come from vegetable or animal origin. Alternatively, use is made of a combination of animal fat and vegetable fat. The animal fat may be butter, butter oil and/or cream. The vegetable fat may be palm kernel oil, palm oil fractions, coconut oil, soy oil or rapeseed oil, or mixtures thereof. The oils may be natural (unhardened), fully or partially hardened.

[0069] Preferably, in the ingredient mix of step a) of the method according to the present invention the fat content ranges between 3 to 12% by weight, preferably between 3 to 11% by weight, even more preferably between 5 to 10% by weight, most preferably between 5 to 8% by weight.

[0070] Carbohydrates used in the preparation of the frozen aerated products according to the present invention comprise monosaccharides (e.g. dextrose, fructose, galactose), disaccharides (e.g. sucrose, lactose), starch hydrolysates (e.g. glucose syrup 90 to 20 DE (combination of mono, di and oligosaccharides)), maltodextrins (DE<20), soluble fibre (e.g. inulin, fructo-oligosaccharide, polydextrose), sugar alcohols (e.g. erythritol, xylitol, sorbitol, mannitol, lactitol, maltitol), glycerol. Different combinations of these materials may be used as sweeteners, freezing point depressants and bulk fillers depending upon the required final product properties like sweetness, calorie content and/or texture. The ingredient mix of step a) of the method according to the present invention preferably comprises between 10 and 30% by weight carbohydrates.

[0071] Said ingredient mix may also comprise high intensity sweeteners (e.g. aspartame, neotame, cyclamate, saccharine, acesulfame-K, sucralose), or sweeteners from vegetable original like Stevia. Preferred amounts used are up to 0.5% by weight of said ingredient mix.

[0072] Besides fat and protein, the ingredient mix of step a) preferably comprises one or more stabilizers. The stabilizers used are preferably chosen from the group of locust bean gum, guar gum, carrageenan, microcrystalline cellulose, carboxy-methylcellulose, pectin, gelatin, gum Arabic, gellan gum, xanthan gum, modified starch, alginate, gum ghatti, gum karaya, gum konjac, agar-agar, oat or a combination thereof. More preferably, the stabilizers are selected from the group of locust bean gum, guar gum, carrageenan or combination thereof. Amounts thereof used in the ingredient mix of step a) of the method of the invention are preferably 0.2 to 3% by weight, preferably 0.2 to 1% by weight.

[0073] The ingredient mix of step a) of the method according to the present invention, preferably comprises an emulsifier. Preferably the emulsifier comprises mono- and diglycerides of fatty acids, lactic acid esters of mono- or diglycerides (LACTEM), acetic acid esters of mono- or diglycerides (ACETEM), diacetyltartaric acid esters of mono- and diglycerides (DATEM), sucrose esters of fatty acids, polyglycerol esters of fatty acids, polyoxyethylene sorbitan fatty acid mono-esters, sodium stearoyl lactylate, calcium stearoyl lactylate, propylene glycol monostearate, lecithin, lysolecithin, phospholipoproteins, egg yolk or mixtures thereof.

[0074] In a preferred embodiment emulsifier comprises mono- and/or diglycerides of fatty acids (i.e. mono and/or di-esters of glycerol and fatty acids). These fatty acids can be saturated or unsaturated and/or may comprise C16 and/or C18 carbon chains.

[0075] In an alternative embodiment, the emulsifier comprises derivatives of mono and diglycerides, such as esters of lactic acid (LACTEM), acetic acid (ACETEM) and/or diacetyltartaric acid (DATEM) of mono- and/or diglycerides.

[0076] In yet another embodiment, the emulsifier comprises sucrose esters of fatty acids, polyglycerol esters of fatty acids, polyoxyethylene sorbitan fatty acid mono-esters, sodium stearoyl lactylate, calcium stearoyl lactylate, propylene glycol monostearate, lecithin, lysolecithin, phospholipoproteins, egg yolk or mixtures thereof. Combinations of 2 or more emulsifiers from the group above may be preferably used in the ingredient mix of step a) of the method of the present invention. Wherein the polyglycerol ester of fatty acids is preferably polyglycerol polyricinoleate. Wherein the polyoxyethylene sorbitan fatty acid mono-esters preferably are selected from polyoxyethylene sorbitan mono-oleate, polyoxyethylene sorbitan monolaurate, polyoxyethylene sorbitan monostearate and combinations thereof.

[0077] In a more preferred embodiment the emulsifier comprises a polyoxyethylene sorbitan fatty acid mono-ester, even more preferably the emulsifier comprises polyoxyethylene sorbitan mono-oleate.

[0078] Preferred amounts of these emulsifiers in the ingredient mix of step a) range between 0.2 to 3% by weight, preferably between 0.2 to 1% by weight.

[0079] The total amount of stabilizers and/or emulsifiers in the ingredient mix of step a) of the method of the present invention preferably ranges between 0.1 and 1% by weight.

[0080] The total solids content of said ingredient mix preferably ranges up to 40% by weight. Preferably the total solids content ranges between 35 and 40% by weight of said ingredient mix.

[0081] Said ingredient mix may further contain flavours and/or colorants customary in the art.

[0082] To further enhance the milky notes of the aerated frozen product of the invention, if deemed necessary, non-protein or non casein containing milk solids, such as lactose or UF permeate from milk or whey, may be incorporated into the ingredient mix of step a).

[0083] A second aspect of the present invention relates to an aerated frozen confectionery product obtainable by the method as has been described above. The frozen aerated confectionery product according to the present invention is preferably ice cream.

[0084] A third aspect of the present invention relates to a frozen aerated confectionery product having an overrun of 75 to 150%, comprising: [0085] 1 to 15% by weight fat; [0086] 5 to 40% by weight carbohydrates; [0087] 0.1 to 5% by weight stabilizer and/or emulsifier; [0088] 0.1 to 1.5% by weight protein, whereof at least 30% by weight of the total amount of protein is caseinate.

[0089] In the frozen aerated confectionery product according to the present invention, on a weight basis the ratio fat to protein is preferably equal or higher than 5, preferably equal or higher than 10.

[0090] The total amount of protein in the frozen aerated product according to the present invention preferably ranges between 0.25 to 1.25% by weight, more preferably between 0.4 to 1.2% by weight, most preferably between 0.5 to 1.0% by weight.

[0091] At least 30% by weight of the total amount of protein is caseinate protein. However, significantly more caseinate may be used. Hence, in a preferred embodiment of the present invention, at least 50%, more preferably at least 80% and even more preferably at least 95% by weight of the total amount of protein is caseinate.

[0092] Preferably, caseinate salts are used, such as sodium caseinate or calcium caseinate. Sodium caseinate is particularly preferred.

[0093] The fat used in the frozen aerated product according to the present invention may come from vegetable or animal origin. Alternatively, a combination of animal fat and vegetable fat is used. The animal fat may be butter, butter oil and/or cream. The vegetable fat may be palm kernel oil, palm oil fractions, coconut oil, soy oil, rapeseed oil or mixtures thereof. The oils may be natural (unhardened), fully or partially hardened.

[0094] Preferably, the fat content in the frozen aerated product according to the present invention ranges between 3 to 12% by weight, preferably between 3 to 11% by weight, even more preferably between 5 to 10% by weight and most preferably between 5 to 8% by weight.

[0095] The carbohydrates and their amounts used in the frozen aerated product according to the present invention, may be as has been described above in relation to the method of the present invention. Furthermore, also the stabilizers and/or emulsifiers and their amounts may be chosen from those described above in relation to the method of the present invention.

[0096] In a preferred embodiment of the present invention, the frozen aerated product has an overrun of 75 to 150%, comprises 1 to 10% by weight fat, 0.25 to 1.0% by weight protein of which at least 50% by weight is caseinate, preferably sodium caseinate, a total solids content between 35 and 40% by weight and wherein the ratio fat to protein is on a weight basis 5 or higher, preferably 10 or higher.

[0097] In a further preferred embodiment of the present invention, the frozen aerated product has an overrun of 75 to 150% comprises 1 to 10% by weight fat, 0.25 to 1.0% by weight protein of which at least 80% by weight is sodium caseinate, a total solids content between 35 and 40% by weight and wherein the ratio fat to protein is on a weight basis 5 or higher, preferably 10 or higher.

[0098] The frozen aerated product according to the present invention is preferably ice cream, most preferably hardened ice cream.

[0099] With respect to the frozen aerated product according to the present invention, it is noted that it may be prepared according to the method of the present invention.

[0100] A further aspect of the present invention relates to an ingredient mix as has been used in relation to step a) of the method of the present invention.

[0101] A last aspect of the present invention relates to the use of such an ingredient mix for preparing a frozen aerated confectionery product as has been described above.

[0102] The present invention will be illustrated further by means of the following non-limiting examples.

EXAMPLES

Sensory Analysis

[0103] The sensory properties of the ice cream samples were evaluated before and after heat shock by an internal expert panel. Ice cream variants were evaluated on the following attributes: body and texture, appearance and melting quality. A + in the sensory test was rated as good and a as unacceptable.

Melting Behaviour:

[0104] Melting tests were carried out on the different frozen ice cream variants. Ice cream variants were kept for 90 minutes on a sieve (stainless steel, mesh size 2.52.5 mm) in a temperature-controlled cabinet having a constant temperature of 20 C. Prior to melting, the ice-cream variants had the following dimensions 679751 cm (wlh). The melted ice cream which dripped through the sieve was weighed in line. In general, good quality ice cream is defined as having a melt-down % of less than 20%, preferably less than 15% after 90 minutes at 20 C.

[0105] The percentage of melted ice cream was calculated according to the following formula:

M2/M1*100%=% melted ice cream

Where,

[0106] M1=mass of the frozen confectionary product in gram
M2=mass of the melted ice cream (liquid) in gram

[0107] In the tables below the results of the melting tests are shown as the melting percentage after 90 minutes of storage at 20 C.

Freeze-Thaw Stability (Resistance to Heat Shock):

[0108] Freeze-thaw stability was simulated by subjecting frozen ice cream variants to temperature cycling of 20 C. to 10 C. Temperature was kept at 20 C. for 12 h and changed within 30 minutes to 10 C. and kept for 11.5 h at this temperature. After 11.5 h, the temperature was again changed within 30 minutes to 20 C. and kept for 11.5 h, this cycle was repeated for a period of 5 days (heat shock).

Particle Size Distribution:

[0109] The fat particle size distribution (PSD) was obtained using a Malvern mastersizer 2000 laser diffraction particle size analyzer. Ice cream mixtures were diluted in about 1:10 in water and/or 1:10 diluted in 10 mM SDS/EDTA solution.

[0110] The fat PSD was measured both directly after the emulsification process and after the ageing process. Differences between the two measuring points are indicative for partial destabilisation of the emulsion upon cooling and storage. Dilution in SDS/EDTA solution enables to distinguish whether larger particle fractions are related to either aggregation/flocculation of emulsion droplets or to poor emulsification and/or partial coalescence.

Example 1: Ice Cream Comprising 5 wt % Vegetable Fat and 0.25 to 3 w/w % Protein from Na-Caseinate and Reference 3% Protein from Skimmed Milk Powder

[0111] Ice cream mixes were prepared according to the formulations shown in Table 1.

TABLE-US-00001 TABLE 1 Example % w/w 1 2 3 4** 5 6 7 Coconut fat: 5.0 5.0 5.0 5.0 5.0 5.0 5.0 Hardened coconutfat K93 Fujioil Europe Skimmed milk 8.6 powder (SMP) medium heat (Promex) Sodium Caseinate 0.28 0.55 0.55 1.1 2.2 3.3 (Excellion EM7, FrieslandCampina DMV) Dextrose 2.0 4.0 4.0 4.0 4.0 4.7 5.9 Sucrose 12.7 12.5 12.5 12.5 12.5 12.0 9.0 Glucodry 355 7.0 12.8 12.5 12.5 12.2 11.0 11.7 (Sedamyl) Cremodan 0.6 0.6 0.6 0.6 0.6 0.6 0.6 709 VEG (Danisco)*** Water 64.1 64.8 64.9 64.9 64.6 64.5 64.5 Total 100.0 100.0 100.0 100.0 100.0 100.0 100.0 Protein content 3 0.25 0.5 0.5 1 2 3 % w/w Casein(ate) 2.4 0.25 0.5 0.5 1 2 3 protein level* Fat: protein ratio 1.8 21.3 10.8 10.8 5.4 2.7 1.8 *SMP: calculated with 80% casein protein and Na caseinate calculated with 90.7% protein of which is 100% caseinate protein. **130% overrun ***Cremodan 709 VEG is a standard commercially available emulsifier/stabilizer cocktail for ice-cream preparation where the emulsifier is of the type mono- and diglycerides, partly unsaturated and the stabilizers are locust bean gum, guar gum and carrageenan.

[0112] Water, protein powder and carbohydrate ingredients were combined in a mix tank and subjected to high shear at a temperature of 60 C. The emulsifier/stabilizer blend was added to the melted fat (70 C.) and this cocktail was added to the water phase while stirring. The resulting mix was pasteurized at 82 C. for 120 seconds, and subsequently homogenized at 175/20 bar and 75 C.-82 C., and followed by a rapid in line cooling step to 4 C. using a plate heat exchanger. The mix was held overnight at 2-7 C. prior to freezing. The ice cream mixes were frozen using an APV MF 50 ice cream freezer (scraped surface heat exchanger) at a mix flow rate of about 18 L/h, an extrusion temperature of 5.5 C. to 6.2 C. and an overrun at the freeze outlet of about 100% (130% for example 1.4). After filling, the ice cream was directly frozen overnight in a hardening freezer at <25 C. and then stored at 18/20 C. A part of the samples was subjected to a heat shock test.

[0113] From Table 2 below it is clear that good quality ice cream was prepared using less than 2% protein from caseinate. Increasing protein content from 0.25% to 1% results in improved body, texture and creaminess, comparable to ice cream with 3% protein from skim milk powder. However, at higher levels of caseinate the ice cream quality decreased to an unacceptable quality in contrast to the application of SMP as a protein source. The table shows that ice cream prepared with a lower concentration sodium caseinate, a higher fat/protein ratio, results in clearly better physical and sensorial properties than ice cream prepared with higher sodium caseinate content.

TABLE-US-00002 TABLE 2 Example 1 2 3 4 5 6 7 Melting % 3 8 7 5 7 14* 40 w/w Melting % 5 9 8 6 10 20 56 w/w after heat shock Sensory + + + + + +/ *visual poor performance

Example 2: Ice Cream Comprising 10 wt % Vegetable Fat and 0.25 to 1.0 w/w % Protein from Na-Caseinate

[0114] Ice cream mixes were prepared according to the formulations shown in Table 3.

TABLE-US-00003 TABLE 3 Example % w/w 1 2 3 Coconut fat: Hardened 10.0 10.0 10.0 coconut fat K93 Fujioil Europe Sodium Caseinate (Excellion 0.28 0.55 1.10 EM7, FrieslandCampina DMV) Dextrose 3.6 3.7 3.8 Sucrose 10.8 10.8 10.6 Glucodry 355 (Sedamyl) 10.0 10.0 10.0 Cremodan 709 VEG 0.5 0.5 0.5 (Danisco)** Water 64.8 64.5 64.0 Total 100.0 100.0 100.0 Protein content % w/w 0.25 0.5 1.0 Caseinate protein level* 0.25 0.5 1.0 Fat:protein ratio 41.4 20.7 10.4 *SMP: calculated with 80% casein protein and Na caseinate calculated with 90.7% protein of which is 100% caseinate protein. **Cremodan 709 VEG is a standard commercially available emulsifier/stabilizer cocktail for ice-cream preparation where the emulsifier is of the type mono- and diglycerides, partly unsaturated and the stabilizers are locust bean gum, guar gum and carrageenan.

[0115] Water, protein powder and carbohydrate ingredients were combined using a mix tank and subsequently subjected to high shear at a temperature of 60 C. The emulsifier/stabilizer blend was added to the melted fat (70 C.) and this cocktail was added to the water phase while stirring. The resulting mix was pasteurized at 82 C. for 120 seconds, homogenized (140/35 bar and 75 C.-82 C.), and followed by a rapid in line cooling step to 4 C. using a plate heat exchanger. The mix was held overnight at 2-7 C. prior to freezing. Ice cream mixes were frozen using an APV MF 50 ice cream freezer (scraped surface heat exchanger) at a mix flow rate of 18 L/h, an extrusion temperature of 5.5 C. to 6.2 C. and an overrun at the freeze outlet of about 100%. After filling, the ice cream was directly, frozen overnight in a hardening freezer at <25 C. and then stored in freezer of 18/20 C. A part of the samples was subjected to a heat shock test.

TABLE-US-00004 TABLE 4 Example 1 2 3 Melting % w/w 7 11 11 Melting % w/w 8 11 10 after heat shock Sensory* + + + Sensory after heat shock + + + Fat particle size distribution PSD fresh** 1.0/1.6 0.9/1.8 0.7/1.6 d(0.5)/d(0.9) water (m) PSD fresh** 1.0/1.5 0.8/1.7 0.7/1.6 d(0.5)/d(0.9) SDS/EDTA (m) PSD after ripening 1.1/2.0 0.9/1.8 0.7/1.6 d(0.5)/d(0.9) Water (m) *increasing protein content from 0.25% protein to 1% improves body, texture and creaminess of the ice cream **samples were diluted in water or SDS/EDTA after cooling down.

[0116] Table 4 shows again that at low concentration of sodium caseinate, at high fat/protein ratio, ice creams having good physical and sensorial properties were obtained. In line with these observations the fat particle size distribution figures show that at all protein levels good emulsions good be prepared, where at the higher protein content the d (0.5) was a bit smaller.

Example 3: Ice Cream Comprising 10% Vegetable Fat and Different Emulsifier/Stabilizer Systems

[0117] Ice cream mixes were prepared according to the formulations shown in Table 5 below.

TABLE-US-00005 TABLE 5 Example % w/w 1 2 3 4 Coconut fat: Hardened 10.0 10.0 10.0 10.0 coconut fat K93 Fujioil Europe Sodium Caseinate 1.1 1.1 (Excellion EM7, FrieslandCampina DMV) Sodium Caseinate 1.1 (Excellion Sodium Caseinate Spray, FrieslandCampina DMV) Excellion EM7 High 1.1 Viscosity***** Dextrose 4.1 4.1 3.8 3.8 Sucrose 11.0 11 10.6 10.6 Glucodry 355 9.7 9.7 10.0 10.0 (Sedamyl) Cremodan 1001 IcePro 0.6 0.6 (Danisco)** Cremodan 709 VEG 0.5 (Danisco)*** Cremodan 315 0.5 (Danisco)**** Water 63.5 63.5 64.0 64.0 Total 100.0 100.0 100.0 100.0 Protein content % 1.0 1.0 1.0 1.0 w/w* Caseinate level* 1.0 1.0 1.0 1.0 Fat:protein ratio 10.5 10.5 10.5 10.4 *Na caseinate and Excellion EM 7 HV calculated with 90.7% protein of which is 100% caseinate protein. **Cremodan 1001 IcePro is a commercially available emulsifier/stabilizer cocktail for ice-cream preparation where the emulsifier is propane-1,2-diol esters of fatty acids and of the type mono- and diglycerides, partly unsaturated and the stabilizers are locust bean gum, and guar gum. ***Cremodan 709 VEG is a commercially available emulsifier/stabilizer cocktail for ice-cream preparation where the emulsifier is of the type mono- and diglycerides, partly unsaturated and the stabilizers are locust bean gum, guar gum and carrageenan. ****Cremodan 315 is a commercial available emulsifier/stabilizer cocktail for ice-cream preparation where the emulsifier is of the type mono- and diglycerides and the stabilizers are locust bean gum and guar gum. *****Excellion EM7 High Viscosity (EM 7 HV) is transglutaminase treated sodium caseinate.

[0118] Water, protein powder and carbohydrate ingredients were combined using a mix tank and subsequently subjected to high shear at a temperature of 60 C. The emulsifier/stabilizer blend was added to the melted fat (70 C.) and this cocktail was added to the water phase while stirring. The resulting mix was pasteurized at 82 C. for 120 seconds, homogenized (140/35 bar and 75 C.-82 C.), and followed by a rapid in line cooling step to 4 C. using a plate heat exchanger. The mix was held overnight at 2-7 C. prior to freezing. Ice cream mixes were frozen using an APV MF 50 ice cream freezer (scraped surface heat exchanger) at a mix flow rate of 18 L/h, an extrusion temperature of 5.5 C. to 6.2 C. and an overrun at the freeze outlet of about 100%. After filling, the ice cream was directly, frozen overnight in a hardening freezer at <25 C. and then stored in freezer of 18/20 C. A part of the samples was subjected to a heat shock test.

TABLE-US-00006 TABLE 6 Example 1 2 3 4 Processability* + + + + Melting % w/w 13 9 11 12 Melting % w/w after 14 12 10 14 Heat shock Sensory + + + + *+ = Good processability during ice cream preparation: ability to incorporate the air, visual good appearance, homogeneous, smooth

[0119] Table 6 shows results from an experiment with different commercially available emulsifier/stabiliser cocktails, the emulsifier being of a) the type emulsifier propane-1,2-diol esters of fatty acids together with the type mono and diglycerides, partly unsaturated or b) the type mono- and diglycerides, partly unsaturated or c) the type mono- and diglycerides, saturated. It shows that good quality ice cream can be prepared with 1% protein from caseinate, and a protein to fat ratio of 10 using different emulsifier/stabilizer systems.

[0120] Next to this, apparently cross linking sodium caseinate with transglutaminase did not significantly change the functional properties of the caseinate in ice cream.

Example 4: Ice Cream Comprising 10 wt % Vegetable Fat and 1 to 2 w/w % Protein from Na-Caseinate

[0121] Ice cream mixes were prepared according to the formulations shown in Table 7 below.

TABLE-US-00007 TABLE 7 Example % w/w 1 2 Coconut fat: Hardened 10.0 10.0 coconut fat K93 Fujioil Europe Sodium Caseinate 1.1 2.2 (Excellion EM7, FrieslandCampina DMV) Dextrose 3.8 4.5 Sucrose 10.6 11.0 Glucodry 355 10.0 8.2 (Sedamyl) Cremodan 315** 0.6 0.6 (Danisco) Water 64.0 63.6 Total 100.0 100.0 Protein content % w/w 1.0 2.0 Casein(ate) level* 1.0 2.0 Fat:protein ratio 10.5 5.3 *Na caseinate calculated with 90.7% protein of which is 100% caseinate protein. **Cremodan 315 is a commercially available emulsifier/stabilizer cocktail for ice-cream preparation where the emulsifier is of the type mono- and diglycerides and the stabilizers are locust bean gum and guar gum.

[0122] Water, protein powder and carbohydrate ingredients were combined using a mix tank and subsequently subjected to high shear at a temperature of 60 C. The emulsifier/stabilizer blend was added to the melted fat (70 C.) and this cocktail was added to the water phase while stirring. The resulting mix was pasteurized at 82 C. for 120 seconds, homogenized (140/35 bar and 75 C.-82 C.), and followed by a rapid in line cooling step to 4 C. using a plate heat exchanger. The mix was held overnight at 2-7 C. prior to freezing. Ice cream mixes were frozen using an APV MF 50 ice cream freezer (scraped surface heat exchanger) at a mix flow rate of 18 L/h, an extrusion temperature of 5.5 C. to 6.2 C. and an overrun at the freeze outlet of about 100%. After filling, the ice cream was directly, frozen overnight in a hardening freezer at <25 C. and then stored in freezer of 18/20 C. A part of the samples was subjected to a heat shock test.

TABLE-US-00008 TABLE 8 Example 1 2 Processability ice + +/ cream preparation* Melting % w/w 12 72 Melting % w/w 14 86 after Heat shock Sensory + Fat Particle Size Distribution PSD fresh** 1.1/2.0 0.7/1.7 d(0.5)/d(0.9) water (m) PSD fresh** 1.1/1.9 0.7/1.7 d(0.5)/d(0.9) SDS/EDTA (m) PSD after ripening 0.8/2.1 1.0/2.1 d(0.5)/d(0.9) Water (m) PSD after ripening 0.8/2.0 0.9/2.0 d(0.5)/d(0.9) SDS/EDTA (m) *+ = Good processability during ice cream preparation: ability to incorporate the air, visual good appearance, homogeneous, smooth. +/: able to keep air in product, however quickly melting and not firm **Samples were diluted direct after homogenization, before cooling in water or SDS/EDTA.

[0123] Table 8 shows again that ice cream prepared with a lower concentration sodium caseinate, at higher fat/protein ratio, provides much better physical and sensorial properties than ice cream prepared with a higher sodium caseinate content. It also appears that at higher protein levels the fat particle size distribution is not really different, meaning that at higher protein levels the emulsions are probably overstabilised or in other words show a too weak churning ability.

Example 5: Ice Cream Comprising Butterfat

[0124] Ice cream mixes were prepared according to the formulations shown in Table 9 below.

TABLE-US-00009 TABLE 9 Example % w/w 1 2 3 4 Coconut fat: Hardened 10.0 10.0 coconut fat K93 Fujioil Europe Butter (82.1% fat) 12.18 12.18 Sodium Caseinate 0.55 1.10 0.55 1.10 (Excellion EM7, FrieslandCampina DMV) Dextrose 3.8 3.8 3.7 3.8 Sucrose 10.7 10.95 10.8 10.6 Glucodry 355 9.7 9.1 10.0 10.0 (Sedamyl) Cremodan 709 VEG 0.5 0.5 0.5 0.5 (Danisco)** Water 62.6 62.4 64.5 64.0 Total 100.0 100.0 100.0 100.0 Protein content % w/w 0.62 1.12 0.5 1.0 Caseinate protein 0.6 1.2 0.5 1.0 level* Fat:protein ratio 17.4 8.6 20.7 10.4 *Na caseinate calculated with 90.7% protein of which is 100% caseinate protein; protein from butter 80% casein protein. **Cremodan 709 VEG is a commercially available emulsifier/stabilizer cocktail for ice-cream preparation where the emulsifier is of the type mono- and diglycerides, partly unsaturated and the stabilizers are locust bean gum, guar gum and carrageenan.

[0125] Water, protein powder and carbohydrate ingredients were combined using a mix tank and subsequently subjected to high shear at a temperature of 60 C. The emulsifier/stabilizer blend was added to the melted fat (70 C.) and this cocktail was added to the water phase while stirring. The resulting mix was pasteurized at 82 C. for 120 seconds, homogenized (140/35 bar and 75 C.-82 C.), and followed by a rapid in line cooling step to 4 C. using a plate heat exchanger. The mix was held overnight at 2-7 C. prior to freezing. Ice cream mixes were frozen using an APV MF 50 ice cream freezer (scraped surface heat exchanger) at a mix flow rate of about 18 L/h, an extrusion temperature of 5.5 C. to 6.2 C. and an overrun at the freeze outlet of about 100%. After filling, the ice cream was directly, frozen overnight in a hardening freezer at <25 C. and then stored in freezer of 18/20 C. A part of the samples was subjected to a heat shock test.

TABLE-US-00010 TABLE 10 Example 1 2 3 4 Processability ice + + + + cream preparation* Melting % w/w 6.4 11.5 11.4 10.8 Melting % w/w 8.3 14.6 11.0 9.9 after Heat shock Sensory + + + + Fat particle size distribution of ice cream mix PSD fresh** 0.9/1.7 0.7/1.6 0.9/1.8 0.7/1.6 d(0.5)/d(0.9) water (m) PSD fresh** 0.9/1.6 0.7/1.6 0.8/1.7 0.7/1.6 d(0.5)/d(0.9) SDS/EDTA (m) PSD after ripening 0.9/1.7 0.7/1.6 0.9/1.8 0.7/1.6 d(0.5)/d(0.9) Water (m) *+ = Good processability during ice cream preparation: ability to incorporate the air, visual good appearance, homogeneous, smooth. **Samples were diluted in water or SDS/EDTA after cooling down.

[0126] The results presented in Table 10 show that at a dosage of 0.5% and 1% protein from caseinate, good quality ice cream can be prepared with both milkfat and vegetable fat, based on resistance to heat shock, sensory, melting behavior, processability and particle size distribution of the ice cream mixture after homogenization and after overnight ripening.

Example 6: Ice Cream Comprising Ca Caseinate as a Protein Source

[0127] Ice cream mixes were prepared according to the formulations shown in Table 11 below.

TABLE-US-00011 TABLE 11 Example % w/w 1 2 Coconut fat Hardened coconut fat K93 5 5 (Fuji oil Europe) Sodium Caseinate (Excellion EM7, 1.1 FrieslandCampina DMV) Calcium Caseinate (Excellion Calcium 0.56 caseinate S (FrieslandCampina DMV) SMP medium heat (Promex) 1.42 Dextrose 3.5 4.0 Sucrose 12.4 12.5 Glucodry 355 (Sedamyl) 11.8 12.2 Cremodan 709 VEG** (Danisco) 0.6 0.6 Emusifier/stabilizer Water 64.7 64.6 Total 100.0 100.0 Protein content % w/w 1.0 1.0 Casein(ate) protein level* 0.9 1 Fat:protein ratio 6.1 5.4 *SMP: calculated with 80% casein protein and Na caseinate calculated with 90.7% protein of which is 100% caseinate protein. **Cremodan 709 VEG is a commercially available emulsifier/stabilizer cocktail for ice-cream preparation where the emulsifier is of the type mono- and diglycerides, partly unsaturated and the stabilizers are locust bean gum, guar gum and carrageenan.

[0128] Water, protein powder and carbohydrate ingredients were combined using a mix tank and subsequently subjected to high shear at a temperature of 60 C. The emulsifier/stabilizer blend was added to the melted fat (70 C.) and this cocktail was added to the water phase while stirring. The resulting mix was pasteurized at 82 C. for 120 seconds, homogenized (175/20 bar and 75 C.-82 C.), and followed by a rapid in line cooling step to 4 C. using a plate heat exchanger. The mix was held overnight at 2-7 C. prior to freezing. Ice cream mixes were frozen using an APV MF 50 ice cream freezer (scraped surface heat exchanger) at a mix flow rate of about 18 L/h, an extrusion temperature of 5.5 C. to 6.2 C. and an overrun at the freeze outlet of about 100%. After filling, the ice cream was directly, frozen overnight in a hardening freezer at <25 C. and then stored in freezer of 18/20 C. A part of the samples was subjected to a heat shock test.

TABLE-US-00012 TABLE 12 Example 1 2 Processability* + + Sensory** + + Melting % w/w 3 7 Melting % w/w after 4 10 Heat shock *Good processability ice cream preparation: + = Ability to incorporate the air, visual good appearance.; homogeneous, smooth. **Creamy mouthfeel, nice white appearance.

[0129] The results presented in Table 12 show that it is also possible to prepare good quality ice cream with calcium caseinate in combination with skimmed milk powder.

Example 7: Ice Cream Comprising Polysorbate 80 (Polyoxyethylene (20) Sorbitan Mono-Oleate) as Emulsifier

[0130] Ice cream mixes were prepared according to the formulation shown in Table 13 below.

TABLE-US-00013 TABLE 13 Example % w/w 1 2 Coconut fat Hardened coconut fat K93 10 10 (Fuji oil Europe) Sodium Caseinate (Excellion EM7, 1.1 1.1 FrieslandCampina DMV)* Polysorbate 80 0.15 0.20 (Croda, Germany) Locust bean gum L150 0.18 0.18 (Unipectin AG, Germany) Guar gum Carrastab T40-20 0.06 0.06 (Caldic, Netherlands) Carrrageenan Satiagel ADG 16U 0.02 0.02 (Cargill, Netherlands) Dextrose 3.8 3.8 Sucrose 10.6 10.6 Glucodry 330 (Sedamyl) 9.7 9.7 Water 64.4 64.3 Total 100.00 10.00 Protein content % w/w 1.1 1.1 Casein(ate) protein level* 1.0 1.0 Fat:protein ratio 9.1 9.1 *Na caseinate calculated with 90.7% protein of which is 100% caseinate protein.

[0131] Water, protein powder, carbohydrate, emulsifier and stabilizer ingredients were combined using a mix tank and subsequently subjected to high shear at a temperature of 65 C. The melted fat (75 C.) was added to the water phase while stirring. The resulting mix was pasteurized at 82 C. for 120 seconds, homogenized (175/20 bar and 75 C.-82 C.), and followed by a rapid in line cooling step to 4 C. using a plate heat exchanger. The mix was held overnight at 2-7 C. prior to freezing. Ice cream mixes were frozen using an APV MF 50 ice cream freezer (scraped surface heat exchanger) at a mix flow rate of about 18 L/h, an extrusion temperature of 5.5 C. to 6.2 C. and an overrun at the freeze outlet of about 100%. After filling, the ice cream was directly, frozen overnight in a hardening freezer at <25 C. and then stored in freezer of 18/20 C. A part of the samples was subjected to a heat shock test.

TABLE-US-00014 TABLE 14 Example 1 2 Melting w/w % after 7.1 4.9 heat shock Melting w/w % after 4.5 2.0 heat shock Processing during + + extrusion Sensory + +

[0132] The results presented in Table 14 show that it is possible to prepare good quality ice cream using Polysorbate 80 as an emulsifier.