Process for the oxidation of starch-based materials
A technology for oxidizing starch and powdery materials, applied in chemical instruments and methods, hydrogen peroxide, chemical/physical processes, etc., can solve problems such as changing the color of coarse powder
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no. 1 approach
[0027] When using such a device, according to a first embodiment of the invention, the method of oxidizing a starch-containing powdery material comprises the following steps:
[0028] a) feeding a continuous flow of starch-containing powdery material to a first reactor of the type described above, wherein the rotor rotates at a speed greater than or equal to 50 rpm to disperse the continuous flow of starch-containing powdery material into the Particle flow of the above materials;
[0029] b) feeding a continuous flow of aqueous hydrogen peroxide into said reactor together with said continuous flow of starch-containing powdery material, said continuous flow of aqueous hydrogen peroxide being dispersed into a flow of tiny droplets by said rotor;
[0030] c) centrifuging the granules and the droplets against the inner wall of the first reactor to form a highly turbulent, dynamic, thin tubular fluid layer in which the granules of starch-containing pulverulent material are mixed wi...
Embodiment 1
[0116] A stream of powdered potato starch with a moisture content of 20% was fed continuously (100 kg / h) through the opening 6 to the reactor R in which the vane rotor 8 was rotating at a speed of 700 rpm. Simultaneously, a stream of 36 volumes of aqueous hydrogen peroxide solution corresponding to about 10.9% w / v was fed continuously (10 l / h) through the opening 5 .
[0117] The temperature of the inner wall is maintained at about 20°C.
[0118] At the feed inlet of reactor R, the starch stream is immediately mechanically dispersed into granules, which are immediately centrifuged against the inner wall of the reactor, where a dynamic, tubular, thin fluid layer forms. Simultaneously, the aqueous hydrogen peroxide solution supplied through the opening 5 is finely atomized by the blades of the rotor 8, and the blades of the rotor 8 also immediately centrifuge the obtained extremely fine droplets. The latter are thus introduced into a fluid layer of dynamic, tubular, thin starch...
Embodiment 2
[0130] Be that the cornstarch flow of the powder of 18% water content is continuously supplied (80kg / h) reactor R " through opening 306 ", and wherein blade rotor 308 rotates with the speed of 800rpm. Simultaneously, is equivalent to about 9.1%w / v excess Hydrogen oxide solution flow was continuously fed (10 l / h) through opening 305, and a continuous flow of 30 volumes of 9% w / v ammonia solution was continuously fed (10 l / h) through inlet 310. The temperature of the inner wall was maintained at about 20° C. .
[0131] After an average residence time in the reactor of about 30 seconds, the powder with a water content of 33% was continuously discharged from the opening 307 .
[0132] The wet powder is continuously supplied to the turbo dryer T' at a flow rate of 80kg / h through the injector 351 through the opening 405, and at the same time through the opening 406 at a temperature of 100°C (flow rate 400m 3 / h) Supply air flow.
[0133] In the turbo dryer T', the wall temperature...
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