Abstract: A food product comprises an oligosaccharide composition that is digestion resistant or slowly digestible. The oligosaccharide composition can be produced by a process that comprises producing an aqueous composition that comprises at least one oligosaccharide and at least one monosaccharide by saccharification of starch, membrane filtering the aqueous composition to form a monosaccharide-rich stream and an oligosaccharide-rich stream, and recovering the oligosaccharide-rich stream. Alternatively, the oligosaccharide composition can be produced by a process that comprises heating an aqueous feed composition that comprises at least one monosaccharide or linear saccharide oligomer, and that has a solids concentration of at least about 70% by weight, to a temperature of at least about 40° C.

Abstract: A process for preparing saccharide oligomers uses an aqueous feed composition that comprises at least one monosaccharide or linear saccharide oligomer, and has a solids concentration of at least about 70% by weight. The feed composition is heated to a temperature of at least about 40° C., and is contacted with at least one catalyst that accelerates the rate of cleavage or formation of glucosyl bonds, such as enzyme or acid, for a time sufficient to cause formation of non-linear saccharide oligomers. A product composition is produced that contains a higher concentration of non-linear saccharide oligomers than linear saccharide oligomers.

Abstract: A process for preparing saccharide oligomers uses an aqueous feed composition that comprises at least one monosaccharide or linear saccharide oligomer, and has a solids concentration of at least about 70% by weight. The feed composition is heated to a temperature of at least about 40° C., and is contacted with at least one catalyst that accelerates the rate of cleavage or formation of glucosyl bonds, such as enzyme or acid, for a time sufficient to cause formation of non-linear saccharide oligomers. A product composition is produced that contains a higher concentration of non-linear saccharide oligomers than linear saccharide oligomers.

Abstract: A highly fermentable, high maltose, non-crystallizing starch conversion syrup is produced having a minimum fermentable equivalent of 95%, a maltose content ranging from about 40 to 65%, a dextrose content ranging from about 35 to 50%, a maltotriose content of less than about 3%, and a dextrose content plus maltose content of at least 93%. The methods for producing the above-described syrup comprise either a one-stage conversion of an .alpha.-amylase thinned syrup using a mixture of enzymes, comprising a barley .beta.-amylase, a pullulanase, and a blend of a glucoamylase and a pullulanase or a two-stage conversion of an .alpha.-amylase thinned syrup, comprising two enzymatic conversions, the first using a mixture of .alpha.-amylase, maltogenic .alpha.-amylase, and pullulanase enzymes, and the second using glucoamylase and pullulanase enzymes.