Device and method for preparing starch sugar for high-temperature corn drying
A technology of high-temperature drying and starch sugar, which is applied in sterilization methods, biochemical equipment and methods, and methods of supporting/immobilizing microorganisms, etc. Liquefaction and saccharification light transmittance improvement, reduced modified starch content, improved liquefaction effect and saccharification effect
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Embodiment 1
[0047] Applicable to high-temperature drying corn to prepare starch sugar, including a starch milk separation unit disc separator for separating coarse starch milk, a starch emulsification unit, and a solid phase separation unit for separating the liquefied liquid after starch emulsification. Saccharification flocculation unit for saccharification and protein flocculation.
[0048] The solid phase separation unit for separating the liquefied liquid after starch emulsification includes a primary cooling device, a decanter centrifuge connected to the primary cooling device and a secondary cooling device connected to the liquid phase separation port of the decanter centrifuge. In the device, the liquefied liquid is separated from the light phase and the heavy phase by a decanter centrifuge after the first stage of cooling, and the light phase enters the saccharification and flocculation unit after the second stage of cooling for saccharification. The protein drying device 4 conne...
Embodiment 2
[0062] (1) Separating the coarse starch milk obtained by processing the high-temperature dried corn through a disk separator to obtain gluten water and starch milk. The feed concentration of the coarse starch milk in the main separation disk separator is 10.0Bé. After machine separation, the bottom flow concentration is 17.7Bé, and the top flow dry matter content is 2.5%;
[0063] (2) After liquefaction, the liquefied liquid with a temperature of 95°C enters the plate heat exchanger for primary cooling, and the temperature of the liquefied liquid is reduced from 95°C to 80°C by adjusting the cooling water flow of the plate heat exchanger;
[0064] (3) The liquefied liquid after the first-level cooling enters the decanter centrifuge for separation, and the feed flow rate is 13m 3 / h, the solid content in the feed is 1.2%, the parameters of the decanter centrifuge are a differential speed of 10 rpm, and a separation factor of 3000. After being separated by a decanter centrifuge...
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