A method for the disintegration and fluid drying of sugar beet material which prevents the material's degradation reaction from taking place and which includes the steps of disintegrating the sugar beet material to particles with a particle surface area of at least 2.0 cm.sup.2, and subsequent immediate exposure of the disintegrated material to a drying gas(es) at a temperature of 25° C. to 160° C. and a flow rate of 5 m.s.sup.31 1 to 40 m.s.sup.−1, where the relative humidity of the drying gas(es) at the inlet to the drying space is at most 85%; and subsequent mixing of the disintegrated material with a flow of drying gas(es) until attaining a value of dry matter of at least 70% by weight.

A method for obtaining juice from sugar-containing raw materials is disclosed. The method includes grinding and extracting sugar by adding a reagent causing a partial destruction of the non-sugar polymer chains within the raw material. The inorganic reagent includes sodium peroxidesulfate (i.e., sodium persulfate), ammonium peroxydisulfate (i.e., ammonium persulfate), or potassium peroxydisulfate (i.e., potassium persulfate), not less than 0.50% weight, and sodium hydroxide or potassium hydroxide, not less than 0.50% weight. The reagent is added to the sugar-containing raw material, the collection of juice, and/or any pulp collection water (e.g., in the beet industry). The total reagent amount added ranges between 0.001-0.02% weight of the raw materials. The mixture is then incubated for 15-20 minutes at a temperature ranging from 25 to 75° C.

Preferred embodiments of the present invention comprise the optional application of concentrations of an aqueous permanganate solution, such as an approximately 0.01% to approximately 50% liquid permanganate solution and preferably comprising approximately 20% sodium permanganate dosed at approximately 1 ppm to approximately 100 ppm to harvested sugar crops, such as sugarcane, sugar beets, and sweet sorghum, at one or more of the sugar processing steps for the crops. The steps where the liquid sodium permanganate may optionally be applied include at a sugar crop cutting step, a sugar crop conveying step, a sugar juice extraction step, a sugar juice clarifying step, and a clarifier muds filtration step. The application of liquid sodium permanganate in the processing of sugar from sugar crops results in reduced equipment fouling, reduced loss in juice purity, reduced scale formation, decreased turbidity in clarified juices, increased sugarcane processing rates, reduced sugar crop production costs, increased sugar product yield, and increased production capacity.

Preferred embodiments of the present invention comprise the optional application of concentrations of an aqueous permanganate solution, such as an approximately 0.01% to approximately 50% liquid permanganate solution and preferably comprising approximately 20% sodium permanganate dosed at approximately 1 ppm to approximately 100 ppm to harvested sugar crops, such as sugarcane, sugar beets, and sweet sorghum, at one or more of the sugar processing steps for the crops. The steps where the liquid sodium permanganate may optionally be applied include at a sugar crop cutting step, a sugar crop conveying step, a sugar juice extraction step, a sugar juice clarifying step, and a clarifier muds filtration step. The application of liquid sodium permanganate in the processing of sugar from sugar crops results in reduced equipment fouling, reduced loss in juice purity, reduced scale formation, decreased turbidity in clarified juices, increased sugarcane processing rates, reduced sugar crop production costs, increased sugar product yield, and increased production capacity.

Systems, apparatuses, and methods for producing and using a sugarcane syrup or powder. In one embodiment, the invention is directed to a system and associated processes for processing sugarcane using a cold processing pipeline in a manner that retains its natural nutritional value while producing a syrup or powder without significant separation of the natural nutrients or use of heat or synthetic chemicals.

A technology for material separation is provided. The technology enables an output of a first material from a rotary lifter. The technology enables a direction of a fluid stream onto the first material in flight based on the output of the first material such that the first material is separated into at least a second material and a third material. The technology enables a conveyance of the second material away from the rotary lifter. The technology enables a removal of the third material via a vacuum port.

A concentrated sugarcane juice powder obtained by a convection current vacuum freeze drying process that includes: selecting and preparing sugarcane stalks by a predetermined quality guideline; extracting sugarcane juice by inserting the sugarcane stalks into a sugarcane juice extracting apparatus having a mesh pattern of micro ridges configured to achieve a maximum extraction efficiency; adding probiotics into the extracted sugarcane juice; freezing the sugarcane juice mixed with the probiotics in molds using an individual quick freezer (IQF) to obtain frozen sugarcane juice blocks; and vacuum freezing said frozen sugarcane juice blocks using a convection current vacuum freeze drying apparatus.

Preferred embodiments of the present invention comprise the optional application of concentrations of an aqueous permanganate solution, such as an approximately 0.01% A to approximately 50% liquid permanganate solution and preferably comprising approximately 20% sodium permanganate dosed at approximately 1 ppm to approximately 100 ppm to harvested sugar crops, such as sugarcane, sugar beets, and sweet sorghum, at one or more of the sugar processing steps for the crops. The steps where the liquid sodium permanganate may optionally be applied include at a sugar crop cutting step, a sugar crop conveying step, a sugar juice extraction step, a sugar juice clarifying step, and a clarifier muds filtration step. The application of liquid sodium permanganate in the processing of sugar from sugar crops results in reduced equipment fouling, reduced loss in juice purity, reduced scale formation, decreased turbidity in clarified juices, increased sugarcane processing rates, reduced sugar crop production costs, increased sugar product yield, and increased production capacity.

A technology for material separation is provided. The technology enables an output of a first material from a rotary lifter. The technology enables a direction of a fluid stream onto the first material in flight based on the output of the first material such that the first material is separated into at least a second material and a third material. The technology enables a conveyance of the second material away from the rotary lifter. The technology enables a removal of the third material via a vacuum port.

Preferred embodiments of the present invention comprise the optional application of concentrations of an aqueous permanganate solution, such as an approximately 0.01% A to approximately 50% liquid permanganate solution and preferably comprising approximately 20% sodium permanganate dosed at approximately 1 ppm to approximately 100 ppm to harvested sugar crops, such as sugarcane, sugar beets, and sweet sorghum, at one or more of the sugar processing steps for the crops. The steps where the liquid sodium permanganate may optionally be applied include at a sugar crop cutting step, a sugar crop conveying step, a sugar juice extraction step, a sugar juice clarifying step, and a clarifier muds filtration step. The application of liquid sodium permanganate in the processing of sugar from sugar crops results in reduced equipment fouling, reduced loss in juice purity, reduced scale formation, decreased turbidity in clarified juices, increased sugarcane processing rates, reduced sugar crop production costs, increased sugar product yield, and increased production capacity.