Methods of manufacturing inositol-stabilized arginine-silicate (“ASI”) complexes with reduced or eliminated clumping and with increased solubility.

Methods of manufacturing inositol-stabilized arginine-silicate (“ASI”) complexes with reduced or eliminated clumping and with increased solubility.

Disclosed is a method for the manufacture of a spray-dried powder consisting essentially of LNT and/or LNnT, the spray-dried powder, its use for the manufacture of nutritional compositions, and nutritional compositions containing the spray-dried powder.

Disclosed is a method for the manufacture of a spray-dried powder consisting essentially of LNT and/or LNnT, the spray-dried powder, its use for the manufacture of nutritional compositions, and nutritional compositions containing the spray-dried powder.

Methods and industrial scale set-ups for manufacturing spray-dried powders are provided. During the process, a solvent is used. The process is done batchwise such that the emulsification mass ratio is low when removal of the solvent is started. Preferred solvents are isopropyl acetate and ethyl acetate.

Methods and industrial scale set-ups for manufacturing spray-dried powders are provided. During the process, a solvent is used. The process is done batchwise such that the emulsification mass ratio is low when removal of the solvent is started. Preferred solvents are isopropyl acetate and ethyl acetate.

A manufacturing method for a plant-based water-soluble dry powder, comprising the steps of; preparing a first mixture by mixing water with oats; comminuting solid components in the first mixture; heating the first mixture to a temperature range between 60° - 70° C.; adding α- and/or β-amylases and incubating for at least 40 min at 60° - 70° C.; filtering the first mixture; adding liquid fat or oil to the first mixture in a ratio of 65 wt. - % of the first mixture and 35 wt% liquid fat or oil; and spray drying the mixture of first mixture and fat or oil.

A manufacturing method for a plant-based water-soluble dry powder, comprising the steps of; preparing a first mixture by mixing water with oats; comminuting solid components in the first mixture; heating the first mixture to a temperature range between 60° - 70° C.; adding α- and/or β-amylases and incubating for at least 40 min at 60° - 70° C.; filtering the first mixture; adding liquid fat or oil to the first mixture in a ratio of 65 wt. - % of the first mixture and 35 wt% liquid fat or oil; and spray drying the mixture of first mixture and fat or oil.

A system for producing free-flowing powder with a narrow particle size distribution from liquid compositions comprising in combination: a feeding reservoir comprising said liquid compositions: a pumping device to pump said liquid composition into at least one atomizing device: said at least one atomizing device composed of at least one fluid nozzle to distribute an upward gaseous drying medium over said nozzle: two lateral streamlined tube-like devices for supplying said liquid composition and pressurized gas to said at least one nozzle from two opposite directions: a cylindrical plenum chamber wherein the fluid nozzle is located: an accelerating zone of a drying medium consisting of a cylindrical pipe located at the bottom of the cylindrical plenum: a conical-cylindrical drying chamber equipped with a manhole, a multi-nozzle manifold and insulation panels: and an intermediate drying medium consisting of a single bed or multi-beds of inert carriers within the drying chamber.

A system for producing free-flowing powder with a narrow particle size distribution from liquid compositions comprising in combination: a feeding reservoir comprising said liquid compositions: a pumping device to pump said liquid composition into at least one atomizing device: said at least one atomizing device composed of at least one fluid nozzle to distribute an upward gaseous drying medium over said nozzle: two lateral streamlined tube-like devices for supplying said liquid composition and pressurized gas to said at least one nozzle from two opposite directions: a cylindrical plenum chamber wherein the fluid nozzle is located: an accelerating zone of a drying medium consisting of a cylindrical pipe located at the bottom of the cylindrical plenum: a conical-cylindrical drying chamber equipped with a manhole, a multi-nozzle manifold and insulation panels: and an intermediate drying medium consisting of a single bed or multi-beds of inert carriers within the drying chamber.