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US4447532A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the manufacture of low D.E. maltodextrins

Assignee: Kraft Heinz Foods Co
•
Filing: 1982-04-29
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Granted: 1984-05-08
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Expires: 2002-04-29
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Abstract

Abstract A process for the production of a low D.E. maltodextrin product having a bland non-sweet taste which includes the steps of (1) cooking non-waxy starch in the presence of alpha-amylase to gelatinize and liquefy the starch, (2) dextrinizing the liquefied starch hydrolyzate with alpha-amylase at a temperature above about 93° C. until a D.E. within the range of 10-13 is obtained, (3) stopping the dextrinization reaction by the addition of sufficient mineral acid to inactivate the enzyme within about 30-60 minutes while maintaining the hydrolyzate temperature at least above about 93° C., and then (4) refining the low D.E. maltodextrin while maintaining the hydrolyzate at a temperature of at least above 76° C. until a dry product is obtained. The dry product is preferably produced by spray drying.

Inventors

  • 👤 Lowell E. Coker
  • 👤 Kalyanasundram Venkatasubramanian

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 21:27
CPC Classifications
C; C12; C12P; C12P19/00; C12P19/14; C13; C13K; C13K1/00; C13K1/06

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 172 words
A process for producing a low D.E. starch hydrolyzate which comprises (1) liquefying non-waxy corn starch in the presence of an alpha amylase by heating at a temperature within the range of from about 104°-107° C., (2) maintaining the liquefied starch hydrolyzate of step (1) at a temperature above about 93° C. in the presence of alpha-amylase so as to dextrinize the hydrolyzate to a D.E. level within the range of from about 10-13, (3) terminating the reaction of step (2) by the addition of sufficient mineral acid to lower the pH of the dextrinized hydrolyzate to a level at which residual alpha-amylase is inactivated within the period of from about thirty to about sixty minutes while maintaining the hydrolyzate temperature at least above about 93° C., (4) refining the resulting hydrolyzate from step (3) while maintaining the hydrolyzate at a temperature of at least above about 76° C. during the refining operations, and (5) spray drying the refined hydrolyzate of step (4) so as to produce a dry free-flowing starch hydrolyzate.
Claim 2
Dependent Claim 172 words
A process for producing a low D.E. starch hydrolyzate which comprises (1) liquefying non-waxy corn starch in the presence of an alpha amylase by heating at a temperature within the range of from about 104°-107° C., (2) maintaining the liquefied starch hydrolyzate of step (1) at a temperature above about 93° C. in the presence of alpha-amylase so as to dextrinize the hydrolyzate to a D.E. level within the range of from about 10-13, (3) terminating the reaction of step (2) by the addition of sufficient mineral acid to lower the pH of the dextrinized hydrolyzate to a level at which residual alpha-amylase is inactivated within the period of from about thirty to about sixty minutes while maintaining the hydrolyzate temperature at least above about 93° C., (4) refining the resulting hydrolyzate from step (3) while maintaining the hydrolyzate at a temperature of at least above about 76° C. during the refining operations, and (5) spray drying the refined hydrolyzate of step (4) so as to produce a dry free-flowing starch hydrolyzate.
Claim 3
Dependent Claim 49 words
The process of claim 1, wherein the pH of the starch hydrolyzate during step (2) is maintained within the range of from about pH 5 to about pH 6 and the temperature of the hydrolyzate is maitained in a range of from about 95° C. to about 98° C.
Claim 4
Dependent Claim 225 words
A process for producing a low D.E. starch hydrolyzate which comprises (1) liquefying non-waxy corn starch in the presence of an alpha-amylase by heating at a temperature within the range of from about 104°-107° C., (2) maintaining the liquefied starch hydrolyzate of step (1) at a temperature above about 93° C. in the presence of alpha-amylase so as to dextrinize the hydrolyzate to a D.E. level within the range of from about 10-13, (3) terminating the reaction of step (2) by the addition of sufficient mineral acid to lower the pH of the dextrinized hydrolyzate to a level at which residual alpha-amylase is inactivated within the period of from about thirty to about sixty minutes while maintaining the hydrolyzate temperature at least above about 93° C., (4) refining the resulting hydrolyzate from step (3) by treatment with activated carbon while maintaining the hydrolyzate at a temperature of at least above about 76° C., (5) removing the activated carbon by filtration while maintaining the hydrolyzate at a temperature of at least above about 76° C., (6) evaporating the hydrolyzate filtrate of step (5) while maintaining the hydrolyzate at a temperature of at least above about 76° C. to a dry solids content such that permits the hydrolyzate to be spray dried, and (7) spray drying the hydrolyzate so as to produce a dry free-flowing starch hydrolyzate.
Claim 5
Dependent Claim 225 words
A process for producing a low D.E. starch hydrolyzate which comprises (1) liquefying non-waxy corn starch in the presence of an alpha-amylase by heating at a temperature within the range of from about 104°-107° C., (2) maintaining the liquefied starch hydrolyzate of step (1) at a temperature above about 93° C. in the presence of alpha-amylase so as to dextrinize the hydrolyzate to a D.E. level within the range of from about 10-13, (3) terminating the reaction of step (2) by the addition of sufficient mineral acid to lower the pH of the dextrinized hydrolyzate to a level at which residual alpha-amylase is inactivated within the period of from about thirty to about sixty minutes while maintaining the hydrolyzate temperature at least above about 93° C., (4) refining the resulting hydrolyzate from step (3) by treatment with activated carbon while maintaining the hydrolyzate at a temperature of at least above about 76° C., (5) removing the activated carbon by filtration while maintaining the hydrolyzate at a temperature of at least above about 76° C., (6) evaporating the hydrolyzate filtrate of step (5) while maintaining the hydrolyzate at a temperature of at least above about 76° C. to a dry solids content such that permits the hydrolyzate to be spray dried, and (7) spray drying the hydrolyzate so as to produce a dry free-flowing starch hydrolyzate.

References Cited (Backward Citations)

US2683682A Cited
US3849194A Cited
US3853706A Cited
US3663369A Cited
US4298400A Cited
US3912590A Cited
US4062728A Cited
US3974034A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-05-08 1987-11-07 1988-05-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-05-08 1991-11-07 1992-05-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-05-08 1995-11-07 1996-05-08 $7700.00 Window Closed / Lapsed

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