A glucose in solid form containing a matrix phase and a plurality of carbohydrate crystals within said matrix phase, the matrix phase containing amorphous glucose and water, wherein the carbohydrate crystals comprise glucose and optionally one or more other carbohydrate(s), and optionally wherein the glucose in solid form is coated with a dry powder coating. The glucose in solid form may comprise at least 50 wt % dry substance (DS) glucose and may comprise one or more other carbohydrate(s) besides glucose. A method for manufacturing solidified glucose is also provided.

The present invention relates to a digestible carbohydrate composition comprising at least 65% (w/w) glucose-based saccharides on a dry basis, wherein said saccharides have a reducing end and D-glucose monomers linked with alternating α1-6 and α1-3 glycosidic linkages, wherein a maltose unit is present at the reducing end; and 0.1 to 30% (w/w) of fructose equivalents on a dry basis; wherein said glucose-based saccharides have an average degree of polymerization greater than 12.

The present invention relates to a digestible carbohydrate composition comprising at least 65% (w/w) glucose-based saccharides on a dry basis, wherein said saccharides have a reducing end and D-glucose monomers linked with alternating α1-6 and α1-3 glycosidic linkages, wherein a maltose unit is present at the reducing end; and 0.1 to 30% (w/w) of fructose equivalents on a dry basis; wherein said glucose-based saccharides have an average degree of polymerization greater than 12.

A method for chromatographically separating a first saccharide from a liquid eluent comprising the first saccharide and a second saccharide by passing the liquid eluent through a bed comprising a gel-type strong acid cation exchange resin in calcium form, wherein the resin is provided in bead form and is characterized by comprising at least 20% whole cracked beads.

A method for chromatographically separating a first saccharide from a liquid eluent comprising the first saccharide and a second saccharide by passing the liquid eluent through a bed comprising a gel-type strong acid cation exchange resin in calcium form, wherein the resin is provided in bead form and is characterized by comprising at least 20% whole cracked beads.

A method for chromatographically separating a first saccharide from a liquid eluent comprising the first saccharide and a second saccharide by passing the liquid eluent through a bed comprising a gel-type strong acid cation exchange resin in calcium form, wherein precipitated barium sulfate is incorporated within the resin.

A method for chromatographically separating a first saccharide from a liquid eluent comprising the first saccharide and a second saccharide by passing the liquid eluent through a bed comprising a gel-type strong acid cation exchange resin in calcium form, wherein precipitated barium sulfate is incorporated within the resin.

This disclosure relates to a method and a system for processing grapes. An example system includes a simulated moving bed (SMB) device configured to receive a feed stream and an eluent stream as inputs and provide an extract stream and a raffinate stream as outputs. The feed stream includes a grape juice, the extract stream includes a high-sugar grape juice, and the raffinate stream includes a low-sugar grape juice. The system also includes fermentation equipment configured to produce a low-alcohol wine from the low-sugar grape juice.

A method for purifying a mixture in a multicolumn chromatography system. The method successively and cyclically collects a raffinate, injects the mixture to be separated, collects an extract, and injects eluent. The mixture to be separated contains fructose and has a dry matter mass concentration of 45 to 55%. The method is carried out at a temperature of 50 to 62° C.

A method for purifying a mixture in a multicolumn chromatography system. The method successively and cyclically collects a raffinate, injects the mixture to be separated, collects an extract, and injects eluent. The mixture to be separated contains fructose and has a dry matter mass concentration of 45 to 55%. The method is carried out at a temperature of 50 to 62° C.