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US4438147A Expired / Lapsed US ⏱️ 0.0 years remaining

Foaming creamer and method of making same

Assignee: Nestec SA
•
Filing: 1982-06-25
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Granted: 1984-03-20
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Expires: 2002-06-25
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Abstract

Abstract A powder-form foaming creamer suitable for use in beverages is prepared by spray-drying a mixture containing a non-dairy fat, a non-dairy carbohydrate and a proteinaceous foam stabilizer. In the spray-drying step, the mixture is atomized by forcing it through a narrow orifice under a high pressure. The dried powder withstands severe handling and retains the ability to produce a foam in the final beverage.

Inventors

  • 👤 Paul L. Hedrick, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 04:55
CPC Classifications
A; A23; A23B; A23B2/00; A23B2/90; A23B2/93; A23C; A23C11/00; A23C11/02; A23C11/04; A23C11/08; A23G; A23G1/00; A23G1/30; A23G1/56; A23G9/00; A23G9/04; A23G9/20; A23C2260/00; A23C2260/20; A23G2220/00; A23G2220/02

Claims Analysis

Total Claims: 36
Claim 1
Independent Claim 83 words
A method of making a foaming creamer comprising: (a) forming a liquid mixture comprising water and solids, said mixture being devoid of an effective amount of surface tension reducing agents, said solids including at least about 5% non-dairy fat, at least about 30% water-soluble non-dairy carbohydrate, and between 0% and about 50% dry skim milk, there being present in said solids an effective amount of a proteinaceous foam stabilizer; (b) blending an inert gas to gassify said mixture; (c) homogenizing said mixture; and
Claim 2
Independent Claim 83 words
A method of making a foaming creamer comprising: (a) forming a liquid mixture comprising water and solids, said mixture being devoid of an effective amount of surface tension reducing agents, said solids including at least about 5% non-dairy fat, at least about 30% water-soluble non-dairy carbohydrate, and between 0% and about 50% dry skim milk, there being present in said solids an effective amount of a proteinaceous foam stabilizer; (b) blending an inert gas to gassify said mixture; (c) homogenizing said mixture; and
Claim 3
Dependent Claim 60 words
(d) spray-drying said mixture, after said gas-blending and homogenizing steps, by: (1) forcing the mixture through an orifice under a spray pressure sufficient to finely atomize the mixture, and (2) contacting the atomized mixture with a gaseous drying medium at an elevated temperature, to thereby produce a substantially dry powder devoid of an effective amount of surface tension reducing agents.
Claim 4
Dependent Claim 60 words
(d) spray-drying said mixture, after said gas-blending and homogenizing steps, by: (1) forcing the mixture through an orifice under a spray pressure sufficient to finely atomize the mixture, and (2) contacting the atomized mixture with a gaseous drying medium at an elevated temperature, to thereby produce a substantially dry powder devoid of an effective amount of surface tension reducing agents.
Claim 5
Dependent Claim 25 words
A method as claimed in claim 1 in which said non-dairy fat and said non-dairy carbohydrate together constitute at least about 85% of said solids.
Claim 6
Dependent Claim 19 words
A method as claimed in claim 2 in which said carbohydrate constitutes less than about 75% of said solids.
Claim 7
Dependent Claim 19 words
A method as claimed in claim 3 in which said fat constitutes at least about 20% of said solids.
Claim 8
Dependent Claim 19 words
A method as claimed in claim 4 in which said fat constitutes less than about 50% of said solids.
Claim 9
Dependent Claim 33 words
A method as claimed in claim 5 in which said solids include at least about 2% of a casein salt, said casein salt constituting at least a portion of said proteinaceous foam stabilizer.
Claim 10
Dependent Claim 29 words
A method as claimed in claim 6 in which no skim milk is included in said solids and said casein salt constitutes at least about 3.5% of said solids.
Claim 11
Dependent Claim 30 words
A method as claimed in claim 7 in which said solids include a gum in an amount sufficient to impart to said mixture a viscosity increase of at least 20%.
Claim 12
Dependent Claim 15 words
A method as claimed in claim 8 in which said casein salt is sodium caseinate.
Claim 13
Dependent Claim 23 words
A method as claimed in claim 8 in which said solids constitute between about 48% and about 52% of said mixture by weight.
Claim 14
Dependent Claim 28 words
A method as claimed in claim 8 in which said gum is a cellulosic gum, said cellulosic gum constituting between about 0.1% and about 1.0% of said solids.
Claim 15
Dependent Claim 18 words
A method as claimed in claim 11 in which said cellulosic gum constitutes about 0.5% of said solids.
Claim 16
Dependent Claim 15 words
A method as claimed in claim 12 in which said gum is a carboxymethylcellulose gum.
Claim 17
Independent Claim 69 words
A method of making a foaming creamer comprising: (a) forming a liquid mixture comprising water and solids, said mixture being devoid of an effective amount of surface tension reducing agents, said solids including at least about 5% non-dairy fat, at least about 30% water-soluble non-dairy carbohydrate, and between 0% and about 50% dry skim milk, there being present in said solids an effective amount of a proteinaceous foam stabilizer;
Claim 18
Independent Claim 69 words
A method of making a foaming creamer comprising: (a) forming a liquid mixture comprising water and solids, said mixture being devoid of an effective amount of surface tension reducing agents, said solids including at least about 5% non-dairy fat, at least about 30% water-soluble non-dairy carbohydrate, and between 0% and about 50% dry skim milk, there being present in said solids an effective amount of a proteinaceous foam stabilizer;
Claim 19
Dependent Claim 83 words
(b) blending an inert gas to gassify said mixture; (c) homogenizing said mixture; and (d) spray-drying said mixture, after said gas-blending and homogenizing steps, by: (1) forcing the mixture through an orifice less than about 3.8 mm. in diameter under a spray pressure of at least about 42 kg/cm 2 , and (2) contacting the atomized mixture with a gaseous drying medium at an elevated temperature, to thereby produce a substantially dry powder devoid of an effective amount of surface tension reducing agents.
Claim 20
Dependent Claim 83 words
(b) blending an inert gas to gassify said mixture; (c) homogenizing said mixture; and (d) spray-drying said mixture, after said gas-blending and homogenizing steps, by: (1) forcing the mixture through an orifice less than about 3.8 mm. in diameter under a spray pressure of at least about 42 kg/cm 2 , and (2) contacting the atomized mixture with a gaseous drying medium at an elevated temperature, to thereby produce a substantially dry powder devoid of an effective amount of surface tension reducing agents.
Claim 21
Dependent Claim 33 words
A method as claimed in claim 14 in which said spray pressure is at least about 140 kg/cm 2 and said orifice is between about 1.5 mm and about 3.8 mm in diameter.
Claim 22
Dependent Claim 25 words
A method as claimed in claim 14 in which a swirling motion is imparted to said mixture as said mixture is forced through said orifice.
Claim 23
Dependent Claim 31 words
A method as claimed in claim 1 in which said gas blending step includes the step of introducing the gas into the mixture while maintaining the mixture under a superatmospheric pressure.
Claim 24
Dependent Claim 24 words
A method as claimed in claim 17 in which said mixture is maintained under superatmospheric pressure from said gas-introducing step to said spray-drying step.
Claim 25
Dependent Claim 27 words
A method as claimed in claim 18 in which said gas blending step includes the step of dispersing said gas in said mixture after said gas-introducing step.
Claim 26
Dependent Claim 20 words
A method as claimed in claim 19 in which said gas blending step is performed prior to said homogenizing step.
Claim 27
Dependent Claim 36 words
A method as claimed in claim 1 in which the amount of said gas blended with said mixture is selected to provide a dried powder having a bulk density between about 0.30 and about 0.35 grams/cc.
Claim 28
Dependent Claim 22 words
A method as claimed in claim 1 in which said gas is selected from the group consisting of carbon dioxide and nitrogen.
Claim 29
Dependent Claim 13 words
A method as claimed in claim 22 in which said gas is nitrogen.
Claim 30
Dependent Claim 20 words
A method as claimed in claim 1 in which said skim milk constitutes at least about 10% of said solids.
Claim 31
Dependent Claim 22 words
A method as claimed in claim 24 in which said skim milk constitutes between about 35% and about 45% of said solids.
Claim 32
Dependent Claim 26 words
A method as claimed in claim 14 further comprising the step of blending a flow enhancing agent with the dry creamer resulting from said spray-drying step.
Claim 33
Dependent Claim 32 words
A method of making a beverage mix comprising making a creamer by a method as claimed in claim 26, then fluidizing the creamer and mixing the fluidized creamer with a beverage powder.
Claim 34
Dependent Claim 34 words
A creamer made by a method as claimed in claim 1 or claim 2 or claim 6 or claim 7 or claim 8, the creamer having a foam index of at least about 4.
Claim 35
Dependent Claim 19 words
A creamer as claimed in claim 28 in which said foam index is between about 4 and about 8.
Claim 36
Dependent Claim 19 words
A creamer as claimed in claim 29 having a bulk density between about 0.30 gm/cc and about 0.35 gm/cc.

References Cited (Backward Citations)

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US2933393A Cited
US3013881A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-03-20 1987-09-19 1988-03-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-03-20 1991-09-19 1992-03-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-03-20 1995-09-19 1996-03-20 $7700.00 Window Closed / Lapsed

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