Patent US4254150A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4254150A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing a foodstuff of cereal

Assignee: Sulzer Escher Wyss GmbH
•
Filing: 1978-12-19
•
Granted: 1981-03-03
•
Expires: 1998-12-19
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract In a process for producing a foodstuff, more particularly a fodder from cereal, it is disclosed to saccharify the starch contained in the cereal to form dextrose by enzymatic degradation of the starch in the cereal grain. All the cereal substances, both those containing starch and those not containing starch, are treated together in the process of enzymatic degradation of the starch in the cereal grain until the starch has been converted to dextrose in the cereal grain. The product is then dried.

Inventors

  • 👤 Hartwig Fritze
  • 👤 Kurt Koenemann
  • 👤 Richard Koenemann

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 14:18
CPC Classifications
A; A23; A23K; A23K10/00; A23K10/10; A23K10/14; A23L; A23L7/00; A23L7/10; A23L7/104; A23L7/107

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 294 words
A process for producing foodstuff flakes from cereal by enzymatic conversion of starch in situ to dextrose comprising the steps of a. forming a mash consisting of 20% to 40% whole cereal grains or grains ground to coarse to medium fine grist and water; b. allowing the mash to swell for a period of 1-2 hours while maintaining it at a temperature below the gelatinization point of the starch; c. adding to the swelled mash alpha amylase in an amount between 0.05% and 0.5% based on the dry cereal; d. adjusting the pH of the mash to 6.5 to 7 by the addition of sodium hydroxide solution; e. heating the mash resulting from the preceding steps in a steam injection cooker to a temperature of 100° to 110° C., then passing the mash at that temperature through a tube type converter with a retention time of 3 to 5 minutes, and thereafter passing the mash through a circulatory reaction vessel with a retention time of about 1 hour and at a temperature of 95° C. to thereby effect conversion of starch to maltodextrin; f. cooling the maltodextrin-containing mash, readjusting its pH to a level effective to promote the action of amyloglucosidase by the addition of a second pH regulator, and then feeding the mash to a reaction tank; g. adding amyloglucosidase to the mash in the reaction tank; h. storing the mash containing amyloglucosidase in the reaction tank for a period of 24 to 48 hours to effect conversion of maltodextrin to dextrose; i. drying the whole dextrose-containing mash resulting from the preceding steps on a single roll dryer to form a thermoplastic film; j. removing and cooling said film to make it friable; and k. comminuting the cooled, friable film to form flakes.
Claim 2
Dependent Claim 294 words
A process for producing foodstuff flakes from cereal by enzymatic conversion of starch in situ to dextrose comprising the steps of a. forming a mash consisting of 20% to 40% whole cereal grains or grains ground to coarse to medium fine grist and water; b. allowing the mash to swell for a period of 1-2 hours while maintaining it at a temperature below the gelatinization point of the starch; c. adding to the swelled mash alpha amylase in an amount between 0.05% and 0.5% based on the dry cereal; d. adjusting the pH of the mash to 6.5 to 7 by the addition of sodium hydroxide solution; e. heating the mash resulting from the preceding steps in a steam injection cooker to a temperature of 100° to 110° C., then passing the mash at that temperature through a tube type converter with a retention time of 3 to 5 minutes, and thereafter passing the mash through a circulatory reaction vessel with a retention time of about 1 hour and at a temperature of 95° C. to thereby effect conversion of starch to maltodextrin; f. cooling the maltodextrin-containing mash, readjusting its pH to a level effective to promote the action of amyloglucosidase by the addition of a second pH regulator, and then feeding the mash to a reaction tank; g. adding amyloglucosidase to the mash in the reaction tank; h. storing the mash containing amyloglucosidase in the reaction tank for a period of 24 to 48 hours to effect conversion of maltodextrin to dextrose; i. drying the whole dextrose-containing mash resulting from the preceding steps on a single roll dryer to form a thermoplastic film; j. removing and cooling said film to make it friable; and k. comminuting the cooled, friable film to form flakes.
Claim 3
Dependent Claim 29 words
A process as defined in claim 1 including the step of adding supplements and/or fillers to the dextrose-containing treated mash before the latter is subjected to said drying step.
Claim 4
Dependent Claim 22 words
A process as defined in claim 2 in which said supplements and fillers include flour waste, or groats and/or minerals and flavorings.
Claim 5
Dependent Claim 50 words
A process as defined in claim 1 wherein said mash containing maltodextrin is cooled in a circulatory mixing cooler equipped with static mixing elements; said second regulator is added to the mash in said cooler; and said cooling and said addition of the second regulator take place simultaneously and continuously.
Claim 6
Dependent Claim 23 words
A process as defined in claim 1 in which said step of adding amyloglucosidase is performed while the reaction tank is being filled.
Claim 7
Dependent Claim 23 words
A process as defined in claim 5 in which the amyloglucosidase is added when the reaction tank is about half full of mash.
Claim 8
Dependent Claim 47 words
A process as defined in claim 1 in which said cooled maltodextrin-containing mash is fed to a series of reaction tanks which are filled in sequence, the process being controlled so that the time required to fill a tank equals the time required to empty a tank.
Claim 9
Dependent Claim 38 words
A process as defined in claim 7 in which the number of reaction tanks is so correlated with the length of time the mash is storred in each tank that one tank is filled while another is emptied.

References Cited (Backward Citations)

US3137639A Cited
US3249512A Cited
US3280006A Cited
US3311542A Cited
US3336137A Cited
US3617300A Cited
US3663369A Cited
US3910820A Cited
US3922198A Cited
US3922196A Cited
US4056636A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-03-02 1984-09-01 1985-03-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-03-02 1988-09-01 1989-03-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-03-02 1992-09-01 1993-03-03 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag