Starch sugar and method for recovering protein in derivative production process thereof
A production process and derivative technology, applied in the field of protein recovery, can solve the problems of reducing the service life of the membrane filter element, increasing the burden on the downstream workshop, and low working efficiency of the membrane equipment, so as to achieve long service life, low labor intensity of workers, and production in the workshop good environment effect
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example 1
[0020] (preparation of maltooligosaccharides)
[0021] (1) Starch slurry liquefaction:
[0022] a) Slurry mixing: first pump a certain amount of water into the slurry mixing tank, start the mixing tank to stir, gradually add starch, adjust the starch into starch milk of 15-22°B′e, after stirring evenly, use 5% HCl solution and 5% NaOH solution to adjust the pH to 5.8.
[0023] b) Liquefaction: pump the adjusted starch slurry into the temporary storage tank before liquefaction, add high-temperature-resistant α-amylase according to the weight ratio of amylase and starch content in starch slurry of 0.25g / Kg, stir evenly, and pump into the intelligent The liquefied high-pressure steam jet liquefier (manufactured by Zhaoguang Bioengineering Co., Ltd., model HYZ-7) was used for liquefaction, and the liquefaction temperature was 100°C to obtain a liquefied liquid with good protein flocculation.
[0024] (2) Protein recovery device to recover lumpy protein: pump the liquefied liquid...
example 2
[0029] (preparation of isomaltooligosaccharide)
[0030] (1) Starch liquefaction:
[0031] a) Slurry mixing: first pump a certain amount of water into the slurry mixing tank, start the mixing tank to stir, gradually add cornstarch, adjust the cornstarch into 15-22°B′e starch milk, after stirring evenly, use HCl and NaOH adjusted the pH to 5.7.
[0032] b) Liquefaction: pump the adjusted starch slurry into the temporary storage tank before liquefaction, add high-temperature-resistant α-amylase according to the weight ratio of amylase and starch content in starch slurry of 0.23g / Kg, stir evenly, and pump into the jet The liquefier was used for liquefaction, and the liquefaction temperature was 140°C to obtain a liquefied liquid with better protein flocculation.
[0033] (2) Protein recovery device to recover lumpy protein: pump the liquefied liquid obtained in step (1) into a box-type protein recovery device to filter lumpy protein. The screen surface precision of the protein ...
example 3
[0038] (preparation of sorbitol)
[0039] (1) Starch liquefaction:
[0040] a) Blending: first pump a certain amount of water into the blending tank, start the blending tank to stir, gradually add corn flour that is directly crushed after peeling and degerming of corn kernels, and adjust the corn flour to 15-17°B′e, After stirring evenly, the pH was adjusted to 5.8 with HCl and NaOH.
[0041] b) Liquefaction: pump the prepared slurry into the temporary storage tank before liquefaction, add high temperature resistant α-amylase according to the weight ratio of amylase to dry powder content in the slurry at 0.25g / Kg, stir evenly, and pump into the jet The liquefier was used for liquefaction, and the liquefaction temperature was 128°C to obtain a liquefied liquid with better protein flocculation.
[0042] (3) Protein recovery by ultrafiltration membrane: Cool the crude filtrate obtained in step (2) to 80°C and pump it into the ultrafiltration equipment. The pressure difference b...
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