A kind of sweet potato starch impurity removal production process
A sweet potato starch and production technology technology, applied in the field of sweet potato starch removal and separation production technology, can solve the problems that the ash content index can only be controlled at more than 0.4%, the protein is more than 0.2%, etc., so as to maintain the natural state of existence and nutritional value, product The effect of quality improvement and good economic benefits
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Embodiment 1
[0027] The sweet potato starch impurity removal production process of the present invention, for the sweet potato starch milk after cleaning, crushing and sieving, is processed according to the following flow process, to remove the ash content, protein and pectin content therein:
[0028] ①Use the integrated three-stage desander to remove the sand and soil impurities in the sweet potato starch milk by using the difference in material specific gravity, and reduce the ash content in the starch product; the starch emulsion enters the desander along the tangential direction, and the specific gravity of starch and water is relatively small. Discharged from the top, the specific gravity of the silt enters the lower silt collector to separate the silt from the starch;
[0029] ②A two-stage high-speed disc separator is used. For the starch emulsion that has undergone sand removal treatment, the centrifugal force generated during the high-speed rotation of the disc separator and the den...
Embodiment 2
[0032]The difference between the impurity removal production process of sweet potato starch in this example and that in Example 1 is that in step 1), three stages and twelve groups of sand removers are used for sand removal treatment: the concentration of starch emulsion is controlled at 8°Be′ -10°Be′ enters the primary desander, the slurry inlet pressure is controlled between 0.35MPa-0.4MPa, the light phase liquid discharged from the top of the primary desander enters the secondary desander; in turn, the secondary desander The light phase liquid enters the third-stage desander, and the sand content in the mud and sand collector at the lower part of the third-stage desander has less sediment and then enters the first-stage desander, and the cycle works to make the concentration of the light-phase liquid discharged from the top of the third-stage desander Control it at 6°Be'-8°Be'. By adjusting the valve to control the drop of slurry feeding pressure and concentration (so that ...
Embodiment 3
[0034] The difference between the production process of sweet potato starch in this example and Example 1 or Example 2 is that in step 2), a two-stage six-group high-speed disk separator is used to remove the ash and protein content in the starch milk: three The starch emulsion discharged from the top of the desander with a concentration of 6°Be'-8°Be' enters a separator, and the feed flow rate is controlled at 25-28m 3 / hour for the first stage separation;
[0035] Then dilute the starch emulsion with a concentration of 18°Be'~20°Be' after the primary separation to a concentration of 6°Be'-8°Be', and then enter the next separator for concentration and separation. The sweet potato protein and other non-starch substances inside are discharged from the light phase liquid port.
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