Process for directly producing high-quality sorbitol by taking starch as raw material
A sorbitol, high-quality technology, applied in the preparation of organic compounds, chemical instruments and methods, organic chemistry, etc., can solve the problems that affect the purity and performance of sorbitol finished products, limit the use area and scope, and low raw material utilization rate, etc. To achieve the effect of improving product quality and its performance, improving product quality, and improving production efficiency
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Embodiment 1
[0023] Embodiment 1: take starch as raw material production sorbitol
[0024] Get the starch, add process water to adjust the size, control the Baume degree of the starch milk after the size adjustment to be 18, adjust the pH value of the starch milk to 4.5, add liquefaction enzyme (i.e. α-amylase) to the starch milk to liquefy, The amount of liquefying enzyme added is 0.30kg / t starch dry basis, starch milk is sprayed and liquefied through a liquefaction injector, the spray temperature is 120°C, the pH value of the liquefied liquid is controlled at 5.0, and the glucose value (DE value, Dextrose Equivalent) is 17%. , the pH value of the liquefied liquid is adjusted to 4.2 after heat exchange, adding glucoamylase (that is, α-1,4-glucose hydrolase), the amount of glucoamylase added is 0.37kg / t starch dry basis, and kept at 55°C for ≥48h, the process During intermittent stirring, when the DE value reaches the requirement ≥ 95%, and no dextrin is detected by alcohol, the subsequent...
Embodiment 2
[0030] Embodiment 2: take starch as raw material production sorbitol
[0031] Get the starch, add process water to adjust the size, control the Baume degree of the starch milk after the size adjustment to be 16, adjust the pH value of the starch milk to 5.5, add liquefying enzyme (i.e. α-amylase) to the starch milk to liquefy, The amount of liquefaction enzyme added is 0.40kg / t starch dry basis, and the starch milk is sprayed and liquefied by the liquefaction injector, the injection temperature is 130°C, the pH value of the liquefied liquid is controlled at 5.5, and the glucose value (DE value, Dextrose Equivalent) is 15%. , the pH value of the liquefied liquid is adjusted to 4.8 after heat exchange, and glucoamylase (that is, α-1,4-glucose hydrolase) is added. During intermittent stirring, when the DE value reaches the requirement ≥ 95%, and no dextrin is detected by alcohol, the subsequent decolorization process is carried out.
[0032] The above feed solution was decoloriz...
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