Low D.E. starch hydrolysates of improved stability prepared by enzymatic hydrolysis of dextrins

Claim 2

A low D.E. starch hydrolysate having a D.E. in the range of from about 9 to about 20, a relatively narrow molecular weight distribution such that its weight average molecular weight to its number average molecular weight ratio of Mw/Mn is less than about 20 and said hydrolysate being further characterized as containing less than about 20% by weight, dry basis, of starch oligosaccharides having a degree of polymerization greater than about 200.

Claim 3

The low D.E. starch hydrolysate of claim 1, wherein said ratio of Mw/Mn is less than about 17.

Claim 4

The low D.E. starch hydrolysate of claim 1, wherein said ratio of Mw/Mn is less than about 15.

Claim 5

The low D.E. starch hydrolysate of claim 1, wherein its ratio of Mw/Mn is less than about 15 and said hydrolysate being further characterized as having less than about 15% by weight, dry basis, of starch oligosaccharides having a degree of polymerization greater than 200.

Claim 6

The low D.E. starch hydrolysate of claim 1, which is further characterized as having a descriptive ratio of at least about 2, said descriptive ratio being the quotient obtained by dividing the sum of the percentage of saccharides, dry basis, having a degree of polymerization of 1 to 6, by the D.E.

Claim 7

A low D.E. starch hydrolysate having a D.E. in the range of from about 9 to about 16, a relatively narrow molecular weight distribution such that its weight average molecular weight to its number average molecular weight ratio of Mw/Mn is less than about 15 and being further characterized as having less than about 15% by weight, dry basis, of starch oligosaccharides having a degree of polymerization greater than about 200, said starch hydrolysate having a descriptive ratio of at least about 2, said descriptive ratio being the quotient obtained by dividing the sum of the percentage of saccharides, dry basis, having a degree of polymerization of 1 to 6, by the D.E.

Claim 8

A low D.E. starch hydrolysate having a D.E. in the range of from about 9 to about 16, a relatively narrow molecular weight distribution such that its weight average molecular weight to its number average molecular weight ratio of Mw/Mn is less than about 15 and being further characterized as having less than about 15% by weight, dry basis, of starch oligosaccharides having a degree of polymerization greater than about 200, said starch hydrolysate having a descriptive ratio of at least about 2, said descriptive ratio being the quotient obtained by dividing the sum of the percentage of saccharides, dry basis, having a degree of polymerization of 1 to 6, by the D.E.

Claim 9

A highly concentrated, non-brazing low D.E. syrup comprising a starch hydrolysate having a D.E. in the range of from about 9 to about 20, a relatively narrow molecular weight distribution such that its weight average molecular weight to its number average molecular weight of Mw/Mn is less than about 20 and being further characterized as having less than about 20% by weight, dry basis, of starch oligosaccharides having a degree of polymerization greater than about 200, which when dissolved in water to a solids content of at least about 50% by weight, remains substantially hazefree over a relatively long period of time.

Claim 10

A highly concentrated, non-brazing low D.E. syrup comprising a starch hydrolysate having a D.E. in the range of from about 9 to about 20, a relatively narrow molecular weight distribution such that its weight average molecular weight to its number average molecular weight of Mw/Mn is less than about 20 and being further characterized as having less than about 20% by weight, dry basis, of starch oligosaccharides having a degree of polymerization greater than about 200, which when dissolved in water to a solids content of at least about 50% by weight, remains substantially hazefree over a relatively long period of time.

Claim 11

The syrup of claim 7, which has a solids content of about 65-75% by weight, dry basis.

Claim 12

The syrup of claim 7, wherein said starch hydrolysate is derived from corn starch.

Claim 13

The syrup of claim 7, wherein the D.E. is in the range of from about 9-16.

Claim 14

A process for producing a low D.E. starch hydrolysate of improved stability which comprises treating a starch dextrin having a degree of branching between about 7% and about 16% with a bacterial alpha-amylase enzyme at a temperature of from about 60°C to about 85°C to achieve a hydrolysate product having a D.E. in the range of from about 9 to about 20, whereby a stable, haze-free starch hydrolysate syrup is produced.

Claim 15

A process for producing a low D.E. starch hydrolysate of improved stability which comprises treating a starch dextrin having a degree of branching between about 7% and about 16% with a bacterial alpha-amylase enzyme at a temperature of from about 60°C to about 85°C to achieve a hydrolysate product having a D.E. in the range of from about 9 to about 20, whereby a stable, haze-free starch hydrolysate syrup is produced.

Claim 16

The process in accordance with claim 11, wherein said starch dextrin is prepared by subjecting starch in its natural dry state to the action of hydrochloric acid at a temperature in the range of from about 100°C to about 180°C.

Claim 17

A process for producing a low D.E. starch hydrolysate which comprises: a. dextrinizing starch by introducing a bed of starch powder into a vessel, maintaining an upward flow of gas through said bed by introducing the gas from beneath said bed and withdrawing it from an outlet above the top of said bed, the upward velocity of said gas flow being sufficient to suspend and vigorously agitate the starch particles within said bed but insufficient to convey a substantial portion of the starch out through said upward outlet, heating said bed in said agitated condition to dextrinizing temperature and maintaining said dextrinizing temperature to provide a starch dextrin having a degree of branching of at least about 7%, b. cooling said bed of agitated starch and withdrawing said starch dextrin from said vessel, c. subjecting a mixture of said starch dextrin and water at a solids content less than about 50% by weight, dry basis, to the hydrolytic action of bacterial alpha-amylase at a temperature of about 60°C to about 85°C and a pH of from about 6 to about 9 to achieve a hydrolysate product having a D.E. of from about 9 to about 20, d. stopping the hydrolytic reaction, and e. recovering the hydrolysate so produced.

Claim 18

A process for producing a low D.E. starch hydrolysate which comprises: a. dextrinizing starch by introducing a bed of starch powder into a vessel, maintaining an upward flow of gas through said bed by introducing the gas from beneath said bed and withdrawing it from an outlet above the top of said bed, the upward velocity of said gas flow being sufficient to suspend and vigorously agitate the starch particles within said bed but insufficient to convey a substantial portion of the starch out through said upward outlet, heating said bed in said agitated condition to dextrinizing temperature and maintaining said dextrinizing temperature to provide a starch dextrin having a degree of branching of at least about 7%, b. cooling said bed of agitated starch and withdrawing said starch dextrin from said vessel, c. subjecting a mixture of said starch dextrin and water at a solids content less than about 50% by weight, dry basis, to the hydrolytic action of bacterial alpha-amylase at a temperature of about 60°C to about 85°C and a pH of from about 6 to about 9 to achieve a hydrolysate product having a D.E. of from about 9 to about 20, d. stopping the hydrolytic reaction, and e. recovering the hydrolysate so produced.

Claim 19

The process in accordance with claim 13, wherein said bed of starch powder is acidified prior to introducing it into said vessel.

Claim 20

The process in accordance with claim 13, wherein the starch is heated to a dextrinizing temperature in the range of from about 65°C to about 210°C.

Claim 21

The process in accordance with claim 13, wherein said dextrinizing and hydrolytic reactions are continuous.

Claim 22

The process in accordance with claim 13, wherein said starch dextrin has a degree of branching in the range of from about 9% to about 12%.

Claim 23

The process in accordance with claim 13 wherein the conversion is carried out under conditions to produce a hydrolysate having a D.E. in the range of from about 9 to about 16.