Preparation process of maltooligosaccharide syrup with high maltotetraose content
The technology of maltotetraose and maltose syrup is applied in the field of preparation of maltose oligosaccharide, which can solve the problem of inability to meet the requirement of adding high-end products, and achieve the effects of rapidly adjusting metabolic rate, reducing production cost and improving saccharification efficiency.
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Embodiment 1
[0038] (1) adding water to cornstarch to form starch slurry, the mass concentration of dry matter in the starch slurry is 13%, and the pH of the starch slurry is adjusted to be 6.0;
[0039] (2) adding high temperature resistant α-amylase to the starch slurry in (1), the addition amount is 0.01L / ton of starch;
[0040] (3) The feed liquid in (2) was liquefied by spraying once at 110°C for 15 minutes, kept in a laminar flow tank for 80 minutes, and liquefied by spraying twice at 130°C for 10 minutes to obtain a liquefied liquid with a DE value of 4.2%.
[0041] (4) Rapidly cooling the liquefied liquid prepared in (3) to 60° C. through a flash heat exchanger;
[0042] (5) First add pullulanase to the feed solution in (4) to react for 1 hour, then add maltotetraose for saccharification reaction, the addition amount of both maltotetraose and pullulanase is 0.5L / ton of starch , after 12 hours of saccharification reaction, the reaction solution was obtained;
[0043] (6) Decoloriz...
Embodiment 2
[0048] (1) adding water to cornstarch to form starch slurry, the mass concentration of dry matter in the starch slurry is 21.5%, and the pH of the starch slurry is adjusted to be 6.0;
[0049] (2) adding high temperature resistant α-amylase to the starch slurry in (1), the addition amount is 0.01L / ton of starch;
[0050] (3) The feed liquid in (2) was liquefied by spraying once at 110°C for 15 minutes, kept in a laminar flow tank for 80 minutes, and liquefied by spraying twice at 130°C for 10 minutes to obtain a liquefied liquid with a DE value of 3.8%;
[0051] (4) Rapidly cooling the liquefied liquid prepared in (3) to 60° C. through a flash heat exchanger;
[0052] (5) First add pullulanase to the feed solution in (4) to react for 1 hour, then add maltotetraose for saccharification reaction, the addition amount of both maltotetraose and pullulanase is 0.5L / ton of starch , after 12 hours of saccharification reaction, the reaction solution was obtained;
[0053] (6) Decolor...
Embodiment 3
[0055] (1) adding water to cornstarch to form starch slurry, the mass concentration of dry matter in the starch slurry is 21.5%, and the pH of the starch slurry is adjusted to be 6.0;
[0056] (2) adding high temperature resistant α-amylase to the starch slurry in (1), the addition amount is 0.045L / ton of starch;
[0057] (3) The feed liquid in (2) was liquefied by spraying once at 110°C for 15 minutes, kept in a laminar flow tank for 80 minutes, and liquefied by spraying twice at 130°C for 10 minutes to obtain a liquefied liquid with a DE value of 5.3%;
[0058] (4) Rapidly cooling the liquefied liquid prepared in (3) to 60° C. through a flash heat exchanger;
[0059] (5) First add pullulanase to the feed solution in (4) to react for 1 hour, then add maltotetraose for saccharification reaction, the addition amount of both maltotetraose and pullulanase is 0.5L / ton of starch , after 12 hours of saccharification reaction, the reaction solution was obtained;
[0060] (6) Decolo...
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