A fermented beverage and method for producing the same are provided. A method of producing a fermented beverage may include providing acid whey. The acid whey may be fermented. Fermentation of the acid whey may be arrested. Flavoring may be added to the fermented acid whey.

A method of preserving a flavor profile of a fermented beverage and controlling an alcohol content within the fermented beverage are provided. A desired alcohol content for the fermented beverage may be determined. The fermented beverage may be flash pasteurized to kill substantially all of a yeast used utilized for fermenting the fermented beverage. The flash pasteurized fermented beverage may be rapidly chilled.

A concentrated fruit juice powder obtained by a convection current vacuum freeze drying process that includes: selecting and preparing fruits by predetermined quality guideline; extracting fruit juice by inserting the fruits into a screw press juicing apparatus having a precutter and a screw press whose body surface varies non-linearly, which is configured to achieve a maximum extraction efficiency; adding probiotics into the extracted fruit juice; freezing the fruit juice mixed with the probiotics in molds using an individual quick freezer (IQF) to obtain frozen fruit juice blocks; and vacuum freezing the frozen fruit juice blocks using a convection current vacuum freeze drying apparatus.

A system for further filtering a liquid extract material after an initial extraction process. In an embodiment, the system includes a semi-rigid filter cup that is substantially cylindrical, the filter cup having a top and a bottom, wherein the top is oriented to receive filter media prior to a filtration process, and material to be filtered during the filtration process. The filter cup includes an integrated deformable flange at the top of the filter cup, an integrated top o-ring that is integrated into the top of the integrated deformable flange and an integrated bottom o-ring that is integrated into the bottom of the integrated deformable flange.

A filter aid composition may include a first acid-treated silica-based filter aid having a first particle size distribution and a second acid-treated silica-based filter aid having a second particle size distribution. A method of making a filter aid composition may include providing a first silica-based filter aid having a first particle size distribution, providing a second silica-based filter aid having a second particle size distribution, and blending the first silica-based filter aid with the second silica-based filter aid to form the filter aid composition. A method of filtering a fluid may include providing a filter aid composition including a first acid-treated silica-based filter aid and a second acid-treated silica-based filter aid and filtering the fluid through the filter aid composition. The filter aid composition may have a multimodal particle size distribution such that the first particle size distribution has a d50 greater than the second particle size distribution.

A filter aid composition may include a first acid-treated silica-based filter aid having a first particle size distribution and a second acid-treated silica-based filter aid having a second particle size distribution. A method of making a filter aid composition may include providing a first silica-based filter aid having a first particle size distribution, providing a second silica-based filter aid having a second particle size distribution, and blending the first silica-based filter aid with the second silica-based filter aid to form the filter aid composition. A method of filtering a fluid may include providing a filter aid composition including a first acid-treated silica-based filter aid and a second acid-treated silica-based filter aid and filtering the fluid through the filter aid composition. The filter aid composition may have a multimodal particle size distribution such that the first particle size distribution has a d50 greater than the second particle size distribution.

A carrot concentrate having a. between 0.115 and 0.25 wt. % Carotenoid (relative to the total weight of the carrot concentrate); b. between 7-24 wt. % edible oil (relative to the total weight of the carrot concentrate); c. between 20 and 75 wt. % (DM) of sugars (relative to the dry matter of the carrot concentrate); wherein the dry matter content of the carrot concentrate ranges between 40 and 75 wt. % relative to the total of the concentrate, wherein the wt. % (DM) means the wt. % of the component relative to the dry matter content, wherein the ratio of edible oil to carotenoids ranges between 40 and 210, and wherein the carrot concentrate has a color diluted in yoghurt, at dosage equivalent to a carotenoid concentration of 0.3795 mg/100 g, wherein the color is defined in the CIELAB color space, and wherein the color is described by a L*-value ranging between 93 and 98, an a*-value ranging between 2.5 and +1.0, and a b*-value ranging between 21.5 and 30. A process for making the carrot concentrate and food products containing the carrot concentrate.

A carrot concentrate having a. between 0.115 and 0.25 wt. % Carotenoid (relative to the total weight of the carrot concentrate); b. between 7-24 wt. % edible oil (relative to the total weight of the carrot concentrate); c. between 20 and 75 wt. % (DM) of sugars (relative to the dry matter of the carrot concentrate); wherein the dry matter content of the carrot concentrate ranges between 40 and 75 wt. % relative to the total of the concentrate, wherein the wt. % (DM) means the wt. % of the component relative to the dry matter content, wherein the ratio of edible oil to carotenoids ranges between 40 and 210, and wherein the carrot concentrate has a color diluted in yoghurt, at dosage equivalent to a carotenoid concentration of 0.3795 mg/100 g, wherein the color is defined in the CIELAB color space, and wherein the color is described by a L*-value ranging between 93 and 98, an a*-value ranging between 2.5 and +1.0, and a b*-value ranging between 21.5 and 30. A process for making the carrot concentrate and food products containing the carrot concentrate.

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.