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.

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 invention relates to a cooling crystallizer (2.0) for saccharose magma in a vertically oriented container (2.1) which has an upper inlet (2.2) for supplying magma and a lower outlet (2.3) for discharging magma, comprising multiple cooling blocks (5.0) which are mutually spaced in a vertical direction. A heat carrier fluid flows through the cooling blocks (5.0), and the cooling blocks are coupled to a heat exchanger in order to dissipate heat from the magma, wherein multiple cooling blocks (5.0) are combined to form a cooling packet (5.1; 5.2), and the cooling packets (5.1; 5.2) are designed as separate cooling circuits with separate heat exchangers (2.1.2; 2.2.2).

The invention relates to a cooling crystallizer (2.0) for saccharose magma in a vertically oriented container (2.1) which has an upper inlet (2.2) for supplying magma and a lower outlet (2.3) for discharging magma, comprising multiple cooling blocks (5.0) which are mutually spaced in a vertical direction. A heat carrier fluid flows through the cooling blocks (5.0), and the cooling blocks are coupled to a heat exchanger in order to dissipate heat from the magma, wherein multiple cooling blocks (5.0) are combined to form a cooling packet (5.1; 5.2), and the cooling packets (5.1; 5.2) are designed as separate cooling circuits with separate heat exchangers (2.1.2; 2.2.2).

A process comprises concentrating a whey composition to at least about 75 weight % solids in one or more evaporators connected in series to form a concentrated whey composition, wherein at least one of the evaporators comprises an evaporator configured to agitate the whey composition within the at least one evaporator, crystallizing at least a portion of the lactose in the concentrated whey composition in a crystallization cascade comprising one or more crystallizing stages to form an at least partially-crystallized whey composition and drying the at least partially-crystallized whey composition to form a dried whey product.

A process comprises concentrating a whey composition to at least about 75 weight % solids in one or more evaporators connected in series to form a concentrated whey composition, wherein at least one of the evaporators comprises an evaporator configured to agitate the whey composition within the at least one evaporator, crystallizing at least a portion of the lactose in the concentrated whey composition in a crystallization cascade comprising one or more crystallizing stages to form an at least partially-crystallized whey composition and drying the at least partially-crystallized whey composition to form a dried whey product.

The present invention relates to a method for preparing fructose or xylulose from biomass comprising glucose or xylose, and a method for separating a mixture of glucose and fructose and a mixture of xylose and xylulose.

A stirrer for a crystallizing evaporator such a crystallizing evaporator for crystallizing sucrose from concentrated beet juice. The stirrer includes at least one active flow-conducting means selected from a group consisting of a plurality of flow-conducting propellers arranged along a shaft of the stirrer and a screw running along the shaft.

A stirrer for a crystallizing evaporator such a crystallizing evaporator for crystallizing sucrose from concentrated beet juice. The stirrer includes at least one active flow-conducting means selected from a group consisting of a plurality of flow-conducting propellers arranged along a shaft of the stirrer and a screw running along the shaft.

Compositions and methods used in the modification of crystallization of aluminum hydroxide from liquor in an aluminum hydroxide production process, such as the Bayer process. More particularly, crystal growth modifier compositions comprising a component of crude corn oil derived from a bioethanol production process and/or a component of biodiesel and methods of using such compositions to modify particle size and distribution of precipitated alumina trihydrate in a precipitation liquor crystallization process.