Maltose production and refining method
A refining method and maltose technology, which are applied in the production of sugar, maltose production, sugar production, etc., can solve the problems of increased maintenance and cleaning workload, uneven cooking effect, and high production cost, so as to avoid the phenomenon of aging starch, thoroughly The effect of cooking and gelatinization and the effect of improving the efficiency of resin use
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Embodiment 1
[0026] Adjust the Baume degree of starch slurry to 14, pH value to 5.6, add Liquozyme Supra0.12 Kg / t (干淀粉) , stir well.
[0027] After the first American automatic control of water heater jet liquefaction, the temperature is 105°C and the flow rate is 17m 3 / h. After cooling to 94°C and holding the heat for 120 minutes, the second American automatic control water heater sprays, the temperature is 125°C, and the flow rate is 17m 3 / h.
[0028] Cool to 59°C, automatically adjust the pH value to 4.8, add β-amylase NOKEZYM SBA 1.13 Kg / t to the automatic enzyme adding system (干淀粉) , Promozyme D2 1.27 Kg / t (干淀粉) . After 15 hours, add Maltogenase L 0.14 Kg / t (干淀粉) . The saccharification reaction lasted for 40 hours. At this time, the maltose content of the saccharification liquid was 90.01% ultra-high maltose syrup.
Embodiment 2
[0030] Adjust the Baume degree of starch slurry to 17, pH value to 5.8, add Liquozyme Supra 0.14 Kg / t (干淀粉) , stir well.
[0031] After the first American automatic control water heater jet liquefaction, the temperature is 109 ℃, the flow rate is 20m 3 / h. After cooling to 98°C and holding for 90 minutes, the second American automatic control water heater sprays, the temperature is 140°C, and the flow rate is 20m 3 / h.
[0032] Cool to 63°C, automatically adjust the pH value to 5.6, add β-amylase NOKEZYM SBA 1.32 Kg / t to the automatic enzyme adding system (干淀粉) , Promozyme D2 1.0 Kg / t (干淀粉) . After 15 hours, add Maltogenase L 0.19 Kg / t (干淀粉) . The saccharification reaction lasted for 60 hours. At this time, the maltose content of the saccharification liquid was 92.28% ultra-high maltose syrup.
Embodiment 3
[0034] Adjust the Baume degree of starch slurry to 15, pH value to 5.7, add Liquozyme Supra 0.13 Kg / t (干淀粉) , stir well.
[0035] After the first American automatic control of water heater jet liquefaction, the temperature is 107°C and the flow rate is 18m 3 / h. After cooling to 96°C and holding the heat for 100 minutes, the second American automatic control water heater sprays, the temperature is 135°C, and the flow rate is 18m 3 / h.
[0036]Cool to 61°C, automatically adjust the pH value to 5.3, add β-amylase NOKEZYM SBA 1.22 Kg / t to the automatic enzyme adding system (干淀粉) , Promozyme D2 1.18 Kg / t (干淀粉) . After 15 hours, add Maltogenase L 0.17 Kg / t (干淀粉) . The saccharification reaction lasted for 55 hours. At this time, the maltose content of the saccharification liquid was 93.75% ultra-high maltose syrup.
[0037] The above maltose syrup is processed by membrane filtration to remove macromolecular substances and impurities, etc., with a flow rate of 8 m 3 / h; Aft...
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