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US3741552A Expired / Lapsed US ⏱️ 0.0 years remaining

System and method for carbonating beverages

Assignee: Scott Technologies Inc
•
Filing: 1969-03-24
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Granted: 1973-06-26
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Expires: 1989-03-24
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Abstract

Abstract A method and a system for carbonating a liquid product. The improved method attainable with the instant system provides a multi-stage carbonation procedure which achieves more accurate and more dependable control of the degree of carbonation of the final product. A primary carbonation process is utilized to precarbonate the liquid product prior to a final carbonating procedure which is capable of providing a uniformly carbonated, stable product. The primary carbonating step is effective to precondition the product prior to the secondary carbonating procedure, such that control of the end product may be achieved by adjustment in the primary carbonation process. The primary and secondary carbonation processes are isolated, one from the other, such that primary carbonation may take place at substantially constant pressure, unaffected by any pressure variations that might occur in the secondary treatment.

Inventors

  • 👤 S Skoli
  • 👤 C Witt
  • 👤 H Mojonnier

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 11:37
CPC Classifications
B; B01; B01F; B01F23/00; B01F23/20; B01F23/23; B01F23/236; B01F23/2363; Y; Y10; Y10S; Y10S261/00; Y10S261/07

Claims Analysis

Total Claims: 29
Claim 1
Independent Claim 212 words
A system for carbonating a liQuid product, said system comprising: a closed fluid line; means for supplying liquid product to said fluid line at a substantially constant pressure; primary carbonating means associated with said fluid line for introducing carbon dioxide into said product at a preset rate to attain a degree of carbonation of said product; secondary carbonating apparatus receiving the product after primary carbonation, said apparatus including a tank within which said carbon dioxide atmosphere is established, a plurality of baffled plates or the like positioned within said tank, such that liquid product will flow thereover to subject said product to the carbon dioxide atmosphere, means for maintaining said atmosphere at a predetermined pressure level, and means to maintain the temperature of said product within a selected temperature range whereby the subjecting of said product to this controled atmosphere of carbon dioxide attains a final desired degree of carbonation; and control means providing the communication between said primary fluid line and the secondary carbonating apparatus, said control means including means for isolating said fluid line from the pressure in said secondary carbonating apparatus so that a substantially constant pressure in said fluid line will be maintained during primary carbonation, unaffected by the pressure of said atmosphere in the secondary carbonating apparatus.
Claim 2
Independent Claim 212 words
A system for carbonating a liQuid product, said system comprising: a closed fluid line; means for supplying liquid product to said fluid line at a substantially constant pressure; primary carbonating means associated with said fluid line for introducing carbon dioxide into said product at a preset rate to attain a degree of carbonation of said product; secondary carbonating apparatus receiving the product after primary carbonation, said apparatus including a tank within which said carbon dioxide atmosphere is established, a plurality of baffled plates or the like positioned within said tank, such that liquid product will flow thereover to subject said product to the carbon dioxide atmosphere, means for maintaining said atmosphere at a predetermined pressure level, and means to maintain the temperature of said product within a selected temperature range whereby the subjecting of said product to this controled atmosphere of carbon dioxide attains a final desired degree of carbonation; and control means providing the communication between said primary fluid line and the secondary carbonating apparatus, said control means including means for isolating said fluid line from the pressure in said secondary carbonating apparatus so that a substantially constant pressure in said fluid line will be maintained during primary carbonation, unaffected by the pressure of said atmosphere in the secondary carbonating apparatus.
Claim 3
Dependent Claim 33 words
A system as defined in claim 1 wherein said means for supplying the product to said fluid line include degerating apparatus for removing substantially all air and other gases from said liquid product.
Claim 4
Dependent Claim 37 words
A system as defined in claim 2 wherein said deaerating apparatus includes means to cool the liquid product after deaeration, such that the temperature of said product upon entering said fluid line is within a preselected range.
Claim 5
Dependent Claim 43 words
A system as defined in claim 1 wherein said means for providing a product to a fluid line include a mixing unit which combines a base liquid with a flavoring additive or the like to produce a non-carbonated, mixed product for subsequent carbonation.
Claim 6
Dependent Claim 25 words
A system as defined in claim 1 wherein said secondary carbonating apparatus includes means to maintain the carbon dioxide atmosphere at a predetermined pressure level.
Claim 7
Dependent Claim 74 words
A system as defined in claim 1 wherein said control means isolating the primary carbonating apparatus from the secondary carbonating apparatus includes a pressure modulated valve, and means for operating said valve such that said valve functions as an orifice varying device to regulate the rate of flow in said fluid line with relation to the amount of product available for supply to said line, thereby maintaining substantially constant flow conditions in said line.
Claim 8
Dependent Claim 27 words
A system as defined in claim 1 wherein said means for supplying product to said fluid line includes a pump discharging fluid at substantially a constant pressure.
Claim 9
Dependent Claim 26 words
A system as defined in claim 1 wherein said primary carbonating means include means to directly introduce carbon dioxide into product flowing in said fluid line.
Claim 10
Dependent Claim 128 words
Apparatus for use in a system for producing a carbonated beverage product, said apparatus including: a closed fluid line; means for supplying non-carbonated liquid product to said line at a substantially constant pressure; primary carbonating means associated with said line for introducing carbon dioxide into said line at a preset rate to effect pre-carbonation of said product; and valve means adapted to provide communication between said fluid line and a pressurized secondary carbonating means at a point downstream from the point where said primary carbonation takes place, said valve means including means for isolating said fluid line from the pressure in the secondary carbonating means so that the introduction of carbon dioxide into said fluid line may take place with the product therein at a substantially constant pressure.
Claim 11
Dependent Claim 128 words
Apparatus for use in a system for producing a carbonated beverage product, said apparatus including: a closed fluid line; means for supplying non-carbonated liquid product to said line at a substantially constant pressure; primary carbonating means associated with said line for introducing carbon dioxide into said line at a preset rate to effect pre-carbonation of said product; and valve means adapted to provide communication between said fluid line and a pressurized secondary carbonating means at a point downstream from the point where said primary carbonation takes place, said valve means including means for isolating said fluid line from the pressure in the secondary carbonating means so that the introduction of carbon dioxide into said fluid line may take place with the product therein at a substantially constant pressure.
Claim 12
Dependent Claim 28 words
Apparatus as defined in claim 9, wherein said primary carbonating means includes adjustable control means foR setting the rate of flow of carbon dioxide into said fluid line.
Claim 13
Dependent Claim 52 words
Apparatus as defined in claim 9, wherein said means for supplying non-carbonated liquid to said fluid line includes a reservoir and a float arrangement operably connected with said valve means, whereby said valve means may be operated by said float to control the rate of flow of product in said fluid line.
Claim 14
Independent Claim 131 words
A method for carbonating a liquid product, said method comprising the steps of: providing a product to be carbonated to a closed fluid line; maintaining the product to said line under substantially constant, predetermined pressure conditions; precarbonating the product while in said fluid line to effect an initial carbonation of said product; introducing said product to a secondary carbonating process wherein said liquid product is subjected to a pressurized atmosphere of carbon dioxide to attain a desired degree of carbonation of said product; and isolating said fluid line from the pressure in the secondary carbonating process, such that the pressure in said line is unaffected by said secondary process and said precarbonating of the product takes place with the pressure in said line substantially constant for a given rate of flow.
Claim 15
Independent Claim 131 words
A method for carbonating a liquid product, said method comprising the steps of: providing a product to be carbonated to a closed fluid line; maintaining the product to said line under substantially constant, predetermined pressure conditions; precarbonating the product while in said fluid line to effect an initial carbonation of said product; introducing said product to a secondary carbonating process wherein said liquid product is subjected to a pressurized atmosphere of carbon dioxide to attain a desired degree of carbonation of said product; and isolating said fluid line from the pressure in the secondary carbonating process, such that the pressure in said line is unaffected by said secondary process and said precarbonating of the product takes place with the pressure in said line substantially constant for a given rate of flow.
Claim 16
Dependent Claim 22 words
A method as defined in claim 12 wherein said step of pre-carbonating the product includes introducing carbon dioxide directly into the product.
Claim 17
Dependent Claim 28 words
A method as defined in claim 13 further including adjusting the rate of flow of carbon dioxide depending on the degree of carbonation desired and that being attained.
Claim 18
Dependent Claim 54 words
A method as defined in claim 12 wherein said step of subjecting the pre-carbonated product to a secondary carbonating process includes flowing said pre-carbonated product over a plurality of plates in an atmosphere of carbon dioxide so that said pre-carbonated product may absorb or expel carbon dioxide to attain the desired degree of carbonation.
Claim 19
Dependent Claim 33 words
A method as defined in claim 15 further including the step of maintaining the pressure of said carbon dioxide atmosphere at substantially a predetermined level to assure proper carbonation to the degree desired.
Claim 20
Dependent Claim 40 words
A method as defined in claim 16 further including the step of maintaining the temperature of the pre-carbonated product between the desired temperature range during the subjection of said product to the carbon dioxide atmosphere in said secondary carbonating process.
Claim 21
Dependent Claim 45 words
A method as defined in claim 12 wherein said step of providing a liquid product to a fluid line includes deaerating of said product prior to introduction into said line such that said product is substantially free of air and other gases prior to carbonation.
Claim 22
Dependent Claim 35 words
A method as defined in claim 18 wherein said step of deaerating the liquid includes the step of cooling said liquid to a temperature within a preselected range for efficient absorption of carbon dioxide gas.
Claim 23
Dependent Claim 36 words
A method as defined in claim 12 wherein said step of providing said product to a fluid line includes mixing a base liquid with a flavoring additive or the like to produce a mixed liquid product.
Claim 24
Independent Claim 231 words
A system for producing a carbonated soft drink beverage or a similar product, said system comprising: means for cooling a base liquid to be used in the production of the final carbonated product; mixing apparatus receiving said cooled liquid for combining therewith in a predetermined ratio a flavoring additive to produce a non-carbonated mixed product; a closed fluid line for receiving the non-carbonated mixed product from said mixing apparatus; means for delivering the non-carbonated product to said fluid line from said mixing apparatus under substantially constant pressure conditions; primary carbonating apparatus associated with said fluid line for directly introducing carbon dioxide into said non-carbonated mixed product in said line to effect a primary carbonation resulting in a pre-carbonated product; secondary carbonating apparatus in the form of a carbonator-cooler connected with said fluid line downstream of the point at which sAid primary carbonation takes place, said carbonator-cooler including means to maintain the pre-carbonated product within a narrow temperature range and means for subjecting said product to a carbon dioxide atmosphere to achieve the final degree of carbonation desired; and variable orifice means interposed between said fluid line and said secondary carbonating means to isolate said fluid line from the internal pressure of said carbonator-cooler so that carbon dioxide may be introduced into said line during primary carbonation with the pressure of said line substantially constant and unaffected by that of said carbonator-cooler.
Claim 25
Independent Claim 231 words
A system for producing a carbonated soft drink beverage or a similar product, said system comprising: means for cooling a base liquid to be used in the production of the final carbonated product; mixing apparatus receiving said cooled liquid for combining therewith in a predetermined ratio a flavoring additive to produce a non-carbonated mixed product; a closed fluid line for receiving the non-carbonated mixed product from said mixing apparatus; means for delivering the non-carbonated product to said fluid line from said mixing apparatus under substantially constant pressure conditions; primary carbonating apparatus associated with said fluid line for directly introducing carbon dioxide into said non-carbonated mixed product in said line to effect a primary carbonation resulting in a pre-carbonated product; secondary carbonating apparatus in the form of a carbonator-cooler connected with said fluid line downstream of the point at which sAid primary carbonation takes place, said carbonator-cooler including means to maintain the pre-carbonated product within a narrow temperature range and means for subjecting said product to a carbon dioxide atmosphere to achieve the final degree of carbonation desired; and variable orifice means interposed between said fluid line and said secondary carbonating means to isolate said fluid line from the internal pressure of said carbonator-cooler so that carbon dioxide may be introduced into said line during primary carbonation with the pressure of said line substantially constant and unaffected by that of said carbonator-cooler.
Claim 26
Dependent Claim 37 words
A system as defined in claim 21 further including deaerating means for said liquid such that said liquid is substantially free of air and other gases prior to mixing with a flavoring additive and subsequent carbonation thereof.
Claim 27
Dependent Claim 29 words
A system as defined in claim 21 wherein said primary carbonating apparatus includes means to adjust the rate of flow of carbon dioxide to the product in said line.
Claim 28
Dependent Claim 25 words
A system as defined in claim 21 wherein said carbonator-cooler includes means to maintain the pressure of the carbon dioxide atmosphere at a preselected level.
Claim 29
Dependent Claim 50 words
A system as defined in claim 21 wherein said mixing apparatus includes a reservoir for the non-carbonated mixed product, and means associated with said reservoir to control said variable orifice means and thereby regulate the rate of flow to said carbonator-coller dependent upon the amount of product in said reservoir.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-06-25 1976-12-25 1977-06-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-06-25 1980-12-25 1981-06-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-06-25 1984-12-25 1985-06-26 $7700.00 Window Closed / Lapsed

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