CA1140389A - Low fat butter - Google Patents

Abstract

File 1326 P/2 CA

LOW FAT BUTTER
ABSTRACT OF THE DISCLOSURE
Low fat butter having good low temperature spreadability and an enhanced protein to fat ratio in comparison to natural butter is prepared from cream in a one step process wherein a small percentage of an emulsifier and a hydrocolloid are incorporated into the cream, and the resulting blend is chilled and worked in a swept surface heat exchanger whereby phase inversion without syneresis occurs. The blend is preferably homogenized and pasteurized prior to phase inversion, whereby the stability and keepability of the resulting product is improved.

Description

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LoW FAT BUTrER
My invention relates to butter having a low fat content, and a process for the production thereof.
Milk fats contain a relatively high proportion of glycerides of saturated fatty acids. Such glycerides have relatively high softening temperatures; as the te~perature of the butter is decreased by refrigeration, for example, the hardness of the butter increases greatly whereby it becomes no longer spreadable. It w~uld be highly desirable to decrease the concentration of these fatty acids in butter so that the butter is spreadable at lower temperatures, particularly where this can be achieved whilst retaining the plastic characteristics of butter at normal ambient temperatures.
It would be further desirable to achieve this decrease in the concentration of saturated fatty acids as these are considered by many authorities to be linked to blood cholester~l formation.

The rheological properties of margerin have long been known to be influenced by varying the fatty acid make-up of the glycerides and also the water content of the emulsion. Whilst it would be possible to modify the chemical make-up of butter fat, e.g. by transesterification, such product would no longer be a true dairy product.
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It has heretofore been proposed to reduce the fat content of butter by increasing the water content thereof. In such proposals butter is first prepared from cream by churning in the traditional manner, and water is reincorporated as a second step.
It would be economically desirable to produce a low fat product from cream in a one step process.
E~rthermore, the churning process for the manufacture of normal butter is essentially a batch process. It would be desirable to produce butter from cream as a continuous process.
Natural butter comprises a water in oil emulsion of about 80% milk fats, 17% water, 1~ to 2~ milk solids not fat (milk solids) and up to akout 2~ salt; nunor quantities of other adjuvants may also be present. It is generally produced by churning dairy cream having up to about 40~ milk fat, 6% milk solids, with the balance water.
In the churning process a phase inversion occurs with the separation of buttermilk from the butter produced, and a concomitent increase in fat content and decrease in milk solids.
Since the milk solids are predominately protein it is apparent that there is a loss o nutritional value in the formation of natural butter from cream. It w~uld be desirable to produce a low fat butter having the nutritional balance in terms of protein to fat ratio akout equal to that of dairy cream.
It is known to produce low fat dairy spreads directly from cream. However, in such processes the product is an oil in water enLlsion. The continuous aqueous phase with its relatively high protein content forms an excellent medium for the propagation of micro-organisms, and such products have little commercial

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acceptance for this reason. Even where the aqueous phase is discontinuous, it may still be conducive to bacterial propagation, partic~llarly where the protein of the product lS
relatively high as herein. It ~uld be desirable to provide a nutritional, low fat butter of good keeping quality.
In accordance with the prime aspect of this invention there is provided low fat butter having good low temperature spreadability.
In a further aspect of the invention there is provided a low fat butter of enhanced nutritional value.
In yet a further aspect of the invention there is provided a low fat butter having an enhanced nutritional value and good keeping qualities.
In another aspect of this invention, there is provided a simple, one step process for the production of low fat butter from cream.
In accordance with one emkodiment of the invention, a low fat butter is produced from a dairy cream by incorporating into such dairy cream a relatively small quantity of a non-ionic emulsifying agent having a hydrophilic-lipophilic ~alance (HLB) as defined in BECHER, EMULSIONS THEORY AND PRACTIOE, ACS MCNCGRAM
135, 1957, in the range of about 3 to 5 inclusive, and a relatively small quantity of a hydrocolloid. The cream is subject to homogenizing conditions so as to produce a relatively fine emwlsion, following which it is chilled and w~rked whereby phase inversion takes place without any substantial syneresis occuring.
The resulting product is then tempered by refrigeration, so as to

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induce a gel structure therein.
me cream will generally have a milk fat content equal to that of the low fat butter to be prepared, and in the range of about 35% to about 60% by weight, there being no criticality in respect thereof. Preferably the cream will contain about 40% by weight miIk fat. Cream of this milk fat content may be readily separated from whole milk by low speed centrifuging, for example Cream of higher miLk fat content may be separated from whole milk by higher speed centrifuging. In addition, a natural cream may be modified to supplement the milk fat of such natural cream by other fatty materials. Preferably such fatty materials will be dairy products such as butter or butter fat; it is also contemplated that fats from non dairy sources,for example vegetable oils,be employed to supplement the milk fat. In general the amount of fat used to modify the cream so as to supplement the milk fat will not comprise more than about 50% by weight of the total fats of the modified cream.
Natural cream containing about 35% about 60% by weight milk fat will normally contain therein c~bout 4% to about 8% by weight of milk protein. When cream is modified by the addition of other fatty materials in the manner indicated above, such modified cream will have a reduced protein content in comparison to the natural cream of an equivalent fat content. It is found necessary to increase the concentration of hydrocolloid as the protein content decreases so as to produce a product of a given firmness and spreadability. Preferably the protein content of m~dified cream is adjusted by the addition of milk or milk powder so as

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to be not less than about 4% by weight of the finished product.
Generally the protein content is maintained in the range of about 4% to about 6% be weight so as to strike a balance between the nutritional value and taste of the finished product and the amount of added hydrocolloid.
The non-ionic emulsifier is preferably of the glyceryl ester type; particularly preferred are those esters of the long chain, saturated fatty acids such as st OE ic acid and palmitic acid. Such esters have a higher setting point than those of the corresponding unsaturated esters, and this is found to ke conducive to forming liquid crystaline phases (gels) in water at a scmewhat higher temperture than that for the unsaturated type.
This ability enables them to be used effectively as water binding, firmung and plasticizing agentS. me non-ionic emulsifier sh~uld have a HLB value in the range of about 3 to 5 inclusive. Preferably the HLB value should be about 3. A preferred emulsifier having the requisite value is distilled glyceryl monostearate having a ooncentration of the mono ester of at least akout 90% with the balance being substantially a di ester. A suitable commercial product of this type is sold under the trade mark DIMONDMN S.
me quantity of the emulsifier will depend to some extent upon the type of emulsifier used and the level of naturally occuring emulsifier present in the cream such as the phospholipids.
Generally, when using the preferred emulsifier the concentration thereof will be within about 0.5% to about 1.5~ by weight, based on the total weight of the ingredients; preferable when the milk fat content is about 40% by weight the concentration of the ~ ~133~39

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emulsifier will be about 0.9%. Where the milk fat is replaced by blending the cream with other fatty materials as disclosed akove, the concentration of phospholipids will generally be decreased, and the concentration of added emulsifier should be proportionately increased so as to produce a product of ccmparable stability and firmness.
The hydrocolloids for use in the present invention function as a firming agent for the low fat butter and increases the stability of the water in oil emNlsion. Suitable hydrocolloids are for example derivatives of alginic acid, gelatin and sodium caseinate. Most preferred is sodium alginate, as this has enabled a more firm product to be produced, in relation to the quantity of hydrocolloid employed, than that which results frcm other hydrocolloids which have so far been employed. From this it will ke apparent that the concentration of hydrocolloid to be employed will depend to some extent upon the desired firmness of the low fat butter, and generally the concentration will be in the range of about 0.3% to about 1.5~ by weight,based upon the total weight of the starting ingredients, where sodium alginate is employed, the other hydrocolloids being utilizable in an amount to give an equivalent desired effect.
m e sequence of addition of the hydrocolloid and emulsifying agent has not been found to be critical. Such additions should be controlled so as to reduce the ca~ing of the additives and to avoid calcuim reaction. Calcium reaction is minimized by the use of sequestering agents and peptizing agents such as sodium tetrapyrophosphate and sodium citrate. It is found that ll~V38~

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the gel strength of the resulting product is improved by the incorporation of the sequesterin~ agent. About 0.1~ by weight of each of these additives,based on the total weight of ingredients, is adequate for the present purposes.
It is found that the method of preparing the product of the invention has a significant bearing upon the properties of the finished product, and also interrelates to some extent with the concentration of emulsifier and hydrocolloid necessary to yield a product of desirable characteristics. The preferred method of preparation of the low fat butter is described in conjunction with the drawings appended hereto, which shows a flow diagram of such method operated in a continuous manner.
In the drawing, the numeral 10 represents a steam jacketed tank which is charged through a line 12 with cream. Such cream may have a milk fat content equal to that of the desired low fat butter, or the milk fat content may be supplemented by the addition of butter in which case tank 10 is desirably equipped with an agitator 14. The temperature of tank 10 is such to render the milk fat liquid, and will normally be maintained at about 50C. The "water soluble" additives such as the hydrocolloid,the sequestering agent~together with an antifungicide such as potassium sorbate~salt~
and water soluble butter flavour where desired are added to the cream by an in line funnel arrangement 15 when dry blended therewith, at circulating pump 16. Alternatively these additives may be dlssolved in milk or water to form a paste or solution prior to addition to the cream if desired, such alternative method further tending to reduce calcium reaction. The outlet

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from pump 16 is in part recirculated to tank 10 through valve 17 and line 18, and part is transferred to steam ~acketed tank ~0.
Here the temperature is further increased to about 70 C. At this temperature the glyceryl monostearate emulsifier is molten, and is readily incorporated into the cream b~ metering in at pump 22.~ Other oil soluble additives such as carotene,butter flavour and colourant may be incorporated at this stage, serving additionally to mollify and dissolve the emulsifier. The output from pump 22 is in part recirculated to tank 20 through valve 24 and line 26, and in part transferred through line 28 to a tw~
stage hcmogenizer 30. The blended cream at about 70C is subject to homDgenization at an initial pressure of 500 PSIG and a final pressure of akout 2000 PSIG. Homogenization is found to have an important effect in retarding microbial growth in the finished product, both by decreasing the size of the water droplets (to about 2 to 3 microns), and also by enhancing the protein absorption of the fat particles (and correspondingly reducing the concentration of protein in the aqueous phase).
It is further found that the reduced p~rticle size increases the ease of the later phase inversion step and lessens the tendency of phase separation which might otherwise occur in such step.
It will be appaent that the hom~gerlization step will assist in incorporating the various additives in the cream.
However, if desired such step may take place prior to blending of the additives although this sequence is less preferred.
~ he outlet from homogenizer 30 is transferred through line 32 to multiplate pasteurizer 40 where the homDgenized cream is subject to a temperature of about 93C to 95 C for a short time pasteurization so as to reduce any microbioal activity.

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Standard plate counts of the fresh finished product generally range fram less than 100 to not more than 1000 p~r gram of product.
It is generally undesirable to maintain the admixed cream at the above temperatures, particularly where it is desired that the finished product be printable, as it is found that such heating weakens the gel strength of the butter. It is surmized that this may be due to the depolymerization~ of the hydrocolloid, although this is by no means certain. A residence time of some 30 seconds is found to be adequate for the purpose of pasteurization.
The output from pasteurizer 40 is passed via line 42 to plate cooler 44 where the temperature is rapidly reduced to akout 32& to 35C, and thence via line 46 to a cold jacketed balance tank 48. Balance tank 48 is equip~ped with a slowly rotating paddlè 49 so as to ~rcmote further cooling and initiate 5 the solidification of milk fat whilst avoiding syneresis.
m e output from balance tank 48 is transferred by pump 50 and line 52 to a continuous throughput tw~ sweep surface heat exchanger arrangement 54 such as a Votator ~ unit. Here the cooled mixture is rapidly chilled to a temperature in the range of about 9C to about 12C, and the chilled mixture is mechanically w~rked, thereby inducing phase inversion but without any appreciable accompanying syneresis. The resulting plastic, water in-oil emulsion is then normally packaged, preferably in tubs, at packaging unit 56 following which it is refrigerated at 2C to 4&
at refrigeration unit 58 for akout 36 hours to complete the gel formation and temper the product. If desired, for example when the low fat butter has a well defined solid form that may be ~i~0~89 - 10 - File 1326 P/2 Q

wrapped, the refrigerating and packaging stations may be reversed in sequence.
It is found that the low fat butter produced in accordance with the above process has excellent keepi~g properties.
Thus such coliform, mould and yeast organisms as may be present in the finished product in accordance with the above defin~d range showed little or no grawth over an extended period, and a shelf life of some three months for the product is entirely feasible. Where long keeping quality is not a problem, lower pasteurization temperatures may be used or the step may be omitted.
In the above illustrated embodiment the blending stage of the process is shown as being operated in a continuous manner.
It may, of course be operated batchwise, in which case tank 20 may be amitted and the output fram line 19 connected directly to homogenizer 30. The te~perature of the cream in tank 10 is raised fram ambient to about 70C and the various additives incorporated by metering through pump 16 at appropriate temperatures.
me follawing examples, in which the parts are hy weight further illustrate the invention;
EX~MPLE 1 97 parts of a natural cream containing 40% milk fats and 8% milk with solids comprising about 65%
milk protein is heated to about 50C to render the solid milk fat content liquid; a dry mixture consisting of 0.5 parts sodium alginate, 0~1 parts each of sodium tetrapyrophosphate, sodium citrate and potassium sorbate, together with 1.2 parts of butter salt is 338~
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admixed with the heated cream in an in-line funnel arrangement.
me temperature of the admixture is raised to about 70C, when ~-~ 0.9 parts of Dimondan S distilled monoglycerides is incorporated together with minor amounts of oil soluble colourant and flavouring.
The hot cream is then homogenized in a tWD stage hcmogenizer wherein the second valve is set at 500 PSIG and the first valve at about 2000 PSIG, thereby forming a emulsion having a particle size about 2-3 microns. The homogenized cream is pasteurized for about 30 seconds at a temperature of 95C, following which it is cooled to 35C in a plate cooler, avoiding vigorous mechanical agitation. m e cooled mixture is slowly stirred to initiate crystallization of the solid milk fats whilst avoiding syneresis.
me cooled mixture is passed into a tWD sweep surface heat exchanger, operating at a~out 10C, wherein phase inversion took place with no syneresis. The resulting product is packaged in tubs and tempered for 36 hours at akout 2 - 4C. The tempered product has average penetrometer readings as shown in Table 1.
Penetrcmeter Values 10 1 mm. at Sample 2C 10C 13 C
20Normal Butter 27 45 69 -Low Fat Butter 149 183 200 TABLE 1: CoMPARISON OF PENE~'R~METER VALUES FOR LCW FAT
BUTTER OF EXAMPLE 1 and NORMAL BUTTER
From the above it may be seen that the spreadability of the low fat butter of the instant invention is much greater than that of natural butter, and it will be appreciated from these values that the low fat butter is easily spreadable even at very low refrigeration temperatures. Additionally, the p~rcentage change 1~4~33~

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in the speadability of the 1QW fat butter is relatively small over the range of tem~erature normally encountered in domestic refrigerators.

S The procedure of Example 1 is repeated, whilst varying the milk solids level of the cream by the addition of milk p~wder.
me protein concentration of the cream is taken as being about 65% that of the milk solids. The amount of sodium alginate necessary to achieve a product having penetrometer values approximately in acoordance with those given in Example 1 is shown in Table 2 below, with Example 1 being shown as a control.
Example Control 2 3 Protein content of cream % 3.9 5.2 6.5 ~ sodium alginate additive 0.70 o.50 0.40 .

TABLE 2: MILK PRorEIN - HYDRDCOLLOID RELATIONSHIP
EXAMPTE,~ 4 - 7 The procedure of Example 1 is followed but using natural cream of different milk fat content and maintaining the miLk solids with the range of about 8 - 10~. The quantity of emLlsifying agent (Dimondan S) necessary to achieve penetrometer values for the low fat butter approximately in accordance with those - 13 - File 1326 P/2 C~

given in Example 1 (Control) is shown in Table 3 below:
Example Control 4 5 6 7 _ Milk Fat % 40 35 45 50 55 5 Emulsifying A~ent ~ 0.90 1.00 0.85 0.75 0.60 TPBLE 3: MILR FAT - EMULSIFIER RELATICNSHIP
It will be appreciated that many changes from the above description as c e within known or customary practice in the art may ke made without departing from the principles of the invention, the essential features of which are set forth in the appended claims.

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Claims (53)

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I CLAIM:

1. A low fat butter comprising:
(a) about 35% to about 60% by weight of fat, at least 50% by weight of said fat being milk fat;
(b) about 0.5% to about 1.5% by weight of at least one non-ionic emulsifier having a hydrophilic-lipophilic balance between about 3 to 5 inclusive;
(c) about 0.3% to about 1.5% by weight of a hydrocolloid;
(d) not less than about 4% by weight of milk protein;
(e) about 35% to about 60% by weight of water.

2. me low fat butter of Claim 1 wherein said fat consists of milk fat.

3. The low fat butter of Claim 1 wherein said fat comprises a out 40% by weight of said composition.

4. The low fat butter of Claim 1 wherein said non-ionic emulsifier is a glyceryl ester of a saturated long chain fatty acid containing not less than about 90% by weight of a mono glyceride.

5. The low fat butter of Claim 4 wherein said non-ionic emulsifier is glyceryl monostearate.

6. The low fat butter of Claim 1, 2 or 3 wherein said hydrocolloid is sodium alginate.

7. The low fat butter of Claim 1, 2 or 3 further comprising a small quantity of a peptizing agent.

8. The low fat butter of Claim 1, 2 or 3 further comprising a small quantity of a sequestering agent.

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9. The low fat butter of Claim 1, 2 or 3 further comprising a small quantity of sodium tetrapyrophosphate and sodium citrate.

10. The low fat butter of Claim 1, 2 or 3 wherein said water comprises about 40% to 50% by weight.

11. A low fat butter consisting essentially of about 40% by weight milk fat, 4% to 6% by weight milk protein, 1% distilled mono glycerides of a higher saturated fatty acid, 0.5% sodium alginate, 0.1% sodium tetrapyrophosphate, 0.1%
sodium citrate, 0.1% sodium sorbate with the balance being water.

12. A process for producing a low fat butter comprising (a) providing a cream having a fat content in the range of about 35% to a out 60% by weight;
(b) incorporating into said cream a minor quantity of a non-ionic emulsifying agent having a hydrophilic to lipophilic balance in the range of about 3 to 5 inclusive, and minor quantity of a hydrocolloid;
(c) subjecting said cream to homogenizing conditions to produce an homogenized cream; then (d) cooling the homogenized cream to form a cooled homogenized cream (e) chilling and working the cooled homogenize cream whereby a phase inversion takes place without any substantial separation of buttermilk.

13. The process as described in Claim 12 wherein said cream is subject to homogenizing conditions subsequent to the incorporation of said emulsifying agent and said hydrocolloid therein.

14. The process as described in Claim 12 wherein said cream is heated to a temperature of not less than about 50°C so as to - 16 - File 1326 P/2 CA

melt solid fats, and incorporating said hydrocolloid into said heated cream.

15. me process as described in Claim 12 wherein said cream is heated to a temperature of not less than about 70°C,and incorporating said non-ionic emulsifying agent into said heated cream.

16. The process as described in Claim 12 wherein said cream is subject to said homogenizing conditions at a temperature of about 70°C.

17. The process as described in Claim 16 wherein said homogenizing conditions comprise a two stage homogenizer operating at pressure of about 500 PSIG at the first stage thereof and a pressure of about 2000 PSIG at the second stage thereof.

18. The process of Claim 12 wherein said cream is pasteurized in a short residence time pasteurizer.

19. The process of Claim 18 wherein said cream is pasteurized at a temperature of about 92°C to 93°C for at least about 30 seconds.

20. The process of Claim 12 wherein said chilling and working is carried out continuously in a swept surface heat exchanger.

21. The process of Claim 20 wherein said working is carried out at a temperature of about 9°C to about 12°C.

22. The process of Claim 12, 13 or 14 wherein said non-ionic emulsifying agent is a distilled monoglyceride ester of a saturated long chain fatty acid.

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23. The process of Claim 12, 13 or 14 wherein said hydrocolloid is sodium alginate.

24. The process of Claim 12, 13 or 14 which includes the incorporation into said cream of a sequestering agent.

25. The process of Claim 12, 13 or 14 which includes the incorporation into said cream of a fungicidal agent.

26. The process of Claim 12, 13 or 14 wherein said cream contains about 42% milk fat and about 4% to about 6% protein.

27. The process of Claim 12, 13 or 14 including tempering the chilled, worked product by refrigeration.

28. A process for producing a low fat butter comprising (a) providing a natural dairy cream having a milk fat content in the range of about 35% to about 60% by weight;
(b) incorporating into said cream a minor quantity of a non-ionic emulsifying agent having a hydrophilic to lipophilic balance in the range of about 3 to 5 inclusive, and minor quantity of a hydrocolloid;
(c) subjecting said cream to homogenizing conditions to produce an homogenized cream; then (d) chilling and working the homogenized cream whereby a phase inversion takes place without any substantial separation of buttermilk.

29. The process as described in Claim 28 wherein said cream is subject to homogenizing conditions subsequent to the incorporation of said emulsifying agent and said hydrocolloid therein.

30. The process as described in Claim 28 wherein said cream is heated to a temperature of not less than about 50°C so as to melt solid fats, and incorporating said hydrocolloid into said heated cream.

31. The process as described in Claim 28 wherein said cream is heated to a temperature of not less than about 70°C, and incorporating said non-ionic emulsifying agent into said heated cream.

32. The process as described in Claim 28 wherein said cream is subject to said homogenizing conditions at a temperature of about 70°C.

33. The process as described in Claim 30, 31 or 32 wherein said homogenizing conditions comprise a two stage homogenizer operating at pressure of about 500 PSIG at the first stage thereof and a pressure of about 2000 PSIG at the second stage thereof.

34. The process of Claim 28 wherein said cream is pasteurized in a short residence time pasteurizer.

35. The process of Claim 34 wherein said cream is pasteurized at a temperature of about 92°C to 93°C for at least about 30 seconds.

36. The process of Claim 28 wherein said chilling and working is carried out continuously in a swept surface heat exchanger.

37. The process of Claim 36 wherein said working is carried out at a temperature of about 9°C to about 12°C.

38. The process of Claim 28, 29 or 30 wherein said non-ionic emulsifying agent is a distilled monoglyceride ester of a saturated long chain fatty acid.

39. The process of Claim 28, 29 or 30 wherein said hydrocolloid is sodium alginate.

40. The process of Claim 28, 23 or 30 which includes the incorporation into said cream of a sequestering agent.

41. The process of Claim 28, 29 or 30 which includes the incorporation into said cream of a fungicidal agent.

42. The process of Claim 28, 29 or 30 wherein said cream contains about 42% milk fat and about 4% to about 6% protein.

43. The process of Claim 28, 29 or 30 including tempering the chilled, worked product by refrigeration.
44. A low fat butter comprising:
(a) about 35% to about 60% by weight of fat, at least 50% by weight of said fat being milk fat;
(b) about 0.5% to about 1.5% by weight of at least one non-ionic emulsifier having a hydrophilic-lipophilic balance between about 3 to 5 inclusive;
(c) about 0.3% to about 1.5% by weight of a hydrocolloid;
(d) not less than about 4% by weight of milk protein;
(e) about 35% to about 60% by weight of water;
when prepared by a process comprising:
(f) providing 100 parts by weight of a cream having a fat content in the range of about 35 parts to about 50 parts by weight, not less than 50% by weight of said fat being milk fat, and not less than about 4% by weight milk protein;
(g) incorporating into said cream between about 0.5 parts to about 1.5 parts by weight of said nonionic emulsifier and between about 0.3 parts to about 1.5 parts by weight of said hydrocolloid;

44. (h) subjecting said cream to homogenizing conditions to produce an homogenized cream; and (i) chilling and working the cooled homogenized cream whereby a phase inversion takes place without any substantial separation of buttermilk.

45. The low fat butter of Claim 44 wherein said fat consists of milk fat.

46. The low fat butter of Claim 44 wherein said cream is a natural dairy cream.

47. The low fat butter of Claim 44, 45 or 46 wherein said non-ionic emulsifier is a glyceryl ester of a saturated long chain fatty acid containing not less than about 90% by weight of a mono glyceride.

48. The low fat butter of Claim 44, 45 or 46 wherein said non-ionic emulsifier is glyceryl monostearate.

49. The low fat butter of Claim 44, 45 or 46 wherein said hydrocolloid is sodium alginate.

50. The low fat butter of Claim 44, 45 or 46 further comprising a small quantity of a peptizing agent which is added to said cream.

51. The low fat butter of Claim 44, 45 or 46 further comprising a small quantity of a sequestering agent which is added to said cream.

52. The low fat butter of Claim 44, 45 or 46 further comprising a small quantity of sodium tetrapyrophosphate and sodium citrate which is added to said cream.

53. A low fat butter consisting essentially of about 40%
by weight milk fat, 4% to 6% by weight milk protein, 1% distilled monoglycerides of a higher saturated fatty acid, 0.5% sodium alginate, 0.1% sodium tetrapyrophosphate, 0.1% sodium citrate, 0.1% sodium sorbate with the balance being water prepared by the process of Claim 44, 45 or 46.