Method for applying one-step liquefaction process to starch sugar production
An application method and technology of starch sugar, applied in the application field of one-step liquefaction method in the production of starch sugar, can solve the problems of poor protein flocculation, poor liquefaction quality, uneven liquefaction, etc., and achieve complete liquefaction, good liquefaction quality, and method simple effect
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Embodiment 1
[0011] The technical scheme solved by the present invention is to prepare starch milk, first put the starch into the batching tank, add water under the condition of stirring, mix well, the weight percentage of starch and water is: starch 30%, water 70%, starch milk The Baume degree is Be17; then add a sodium carbonate solution with a mass concentration of 30%, adjust the pH value to 5.5, add 0.3% of the starch weight of α-amylase resistant to 105°C high temperature, and mix to form a mixed slurry. The pump is pumped into the liquefier, the liquefier is fed with water vapor, the mixed slurry is heated to 105°C, and the mixed slurry enters the diffusion tank under the outlet pressure of the liquefier of 0.5MPa, and is further uniformly refined for 8 seconds. After being uniformly refined, it enters the protein separation tank and passes After the filter plate in the protein separation tank is filtered, the protein is separated, and the protein outlet flows out of the protein sepa...
Embodiment 2
[0013] The technical scheme solved by the present invention is to prepare starch milk, first put the starch into the batching tank, add water under the condition of stirring, mix well, the weight percentage of starch and water is: starch 35%, water 65%, starch milk The Baume degree is Be17.5; then add a sodium carbonate solution with a mass concentration of 35%, adjust the pH value to 5.7, add 0.4% of the starch weight of α-amylase resistant to high temperatures at 108°C, and mix to form a mixed slurry , pumped into the liquefier, the liquefier was fed with water vapor, the mixed slurry was heated to 108°C, and at the outlet pressure of the liquefier 0.55MPa, it entered the diffusion tank, and was further uniformly refined for 10 seconds. After uniform refinement, it entered the protein separation tank , after being filtered through the filter plate in the protein separation tank, the protein is separated, and the protein is discharged from the protein outlet of the protein sep...
Embodiment 3
[0015] The technical scheme solved by the present invention is to prepare starch milk, first put the starch into the batching tank, add water under the condition of stirring, mix well, the weight percentage of starch and water is: starch 40%, water 60%, starch milk The Baume degree is Be18; then add a sodium carbonate solution with a mass concentration of 40%, adjust the pH value to 6, add 0.5% of the starch weight of α-amylase resistant to 110°C high temperature, and mix to form a mixed slurry. The pump is pumped into the liquefier, the liquefier is fed with water vapor, the mixed slurry is heated to 110°C, and the mixed slurry enters the diffusion tank under the outlet pressure of the liquefier of 0.6MPa, and is further uniformly refined for 12 seconds. After uniform refinement, it enters the protein separation tank and passes After the filter plate in the protein separation tank is filtered, the protein is separated, and the protein is discharged from the protein outlet of t...
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