Abstract: A process is disclosed for obtaining citrus fiber from citrus pulp. Citrus fiber is obtained having a c* close packing concentration value of less than 3.8. The citrus fiber can be obtained having a viscosity of at least 1000 mPa.s, wherein said citrus fiber is dispersed in standardized water at a mixing speed of from 800 rpm to 1000 rpm, to a 3 w/w% citrus fiber/standardized water solution, and wherein said viscosity is measured at a shear rate of 5 s-1 at 20° C. Citrus fiber can be obtained having a CIELAB L* value of at least 90. The citrus fiber can be used in food products, feed products, beverages, personal care products, pharmaceutical products or detergent products.

Abstract: A process is disclosed for modifying citrus fiber. Citrus fiber is obtained having a c* close packing concentration value of less than 3.8 w %, anhydrous basis. The citrus fiber can have a viscosity of at least 1000 mPa·s, wherein said citrus fiber is dispersed in standardized water at a mixing speed of from 800 rpm to 1000 rpm, to a 3 w/w % citrus fiber/standardized water solution, and wherein said viscosity is measured at a shear rate of 5 s-1 at 20 C. Citrus fiber can be obtained having a CIELAB L* value of at least 90. The citrus fiber can be used in food products, feed products, beverages, personal care products, pharmaceutical products or detergent products.

Abstract: A process is disclosed for obtaining citrus fiber from citrus peel. Citrus fiber is obtained having a c* close packing concentration value of less than 3.8 wt %/ anhydrous base. The citrus fiber can be used in food products, feed products, beverages, personal care products, pharmaceutical products or detergent products.

Abstract: There is provided a process for the preparation of purified ?-(1,3)-D-glucans, comprising the steps of providing an aqueous ?-(1,3)-D-glucan initial solution having a pH of above 11.0, filtering the aqueous ?-(1,3)-D-glucan initial solution to obtain a ?-(1,3)-D-glucan containing filtrate, adjusting the pH of the ?-(1,3)-D-glucan containing filtrate with an acid to a pH of below 5.0 to obtain an acidic ?-(1,3)-D-glucan solution, and heating the acidic ?-(1,3)-D-glucan solution to a temperature in the range of 60 to 160° C.

Abstract: There is provided a process for the preparation of purified ?-(1,3)-D-glucans, comprising the steps of providing an aqueous ?-(1,3)-D-glucan initial solution having a pH of above 11.0, filtering the aqueous ?-(1,3)-D-glucan initial solution to obtain a ?-(1,3)-D-glucan containing filtrate, adjusting the pH of the ?-(1,3)-D-glucan containing filtrate with an acid to a pH of below 5.0 to obtain an acidic ?-(1,3)-D-glucan solution, and heating the acidic ?-(1,3)-D-glucan solution to a temperature in the range of 60 to 160° C.

Abstract: There is provided a process for the preparation of purified ?-(1,3)-D-glucans, comprising the steps of providing an aqueous ?-(1,3)-D-glucan initial solution having a pH of above 11.0, filtering the aqueous ?-(1,3)-D-glucan initial solution to obtain a ?-(1,3)-D-glucan containing filtrate, adjusting the pH of the ?-(1,3)-D-glucan containing filtrate with an acid to a pH of below 5.0 to obtain an acidic ?-(1,3)-D-glucan solution, and heating the acidic ?-(1,3)-D-glucan solution to a temperature in the range of 60 to 160° C.

Abstract: A process is disclosed for obtaining citrus fiber from citrus peel. Citrus fiber is obtained having a c* close packing concentration value of less than 3.8 wt % anhydrous base. The citrus fiber can be used in food products, feed products, beverages, personal care products, pharmaceutical products or detergent products.

Abstract: A process is disclosed for obtaining citrus fiber from citrus pulp. Citrus fiber is obtained having a c* close packing concentration value of less than 3.8. The citrus fiber can be obtained having a viscosity of at least 1000 mPa·s, wherein said citrus fiber is dispersed in standardized water at a mixing speed of from 800 rpm to 1000 rpm, to a 3 w/w % citrus fiber/standardized water solution, and wherein said viscosity is measured at a shear rate of 5 s?1 at 20° C. Citrus fiber can be obtained having a CIELAB L* value of at least 90. The citrus fiber can be used in food products, feed products, beverages, personal care products, pharmaceutical products or detergent products.

Abstract: A process is disclosed for modifying citrus fiber. Citrus fiber is obtained having a c* close packing concentration value of less than 3.8 w %, anhydrous basis. The citrus fiber can have a viscosity of at least 1000 mPa·s, wherein said citrus fiber is dispersed in standardized water at a mixing speed of from 800 rpm to 1000 rpm, to a 3 w/w % citrus fiber/standardized water solution, and wherein said viscosity is measured at a shear rate of 5 s?1 at 20 C. Citrus fiber can be obtained having a CIELAB L* value of at least 90. The citrus fiber can be used in food products, feed products, beverages, personal care products, pharmaceutical products or detergent products.