Method for producing high purity malt sugar product

A production method and maltose technology, applied in the field of starch and starch sugar production, can solve problems such as unfavorable crystal formation, complex process, limited use, etc., and achieve the effects of convenient storage and transportation, avoidance of refining process, and simple preparation method.

Inactive Publication Date: 2005-03-02
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In the preparation of maltose syrup, there are mainly the following deficiencies: the DE value is high after starch liquefaction, the existence of glucose in the syrup will affect the quality of the product, such as not conducive to the formation of crystals, the viscosity of the syrup is reduced, etc.; Incompleteness will lead to high content of oligosaccharides with DP≥3
[0008] At the same time, the maltose syrup is viscous, which brings great inconvenience to the storage and transportation of the product. The 98% high-purity maltose prepared by the existing technology needs 85% maltose syrup. After adsorption, ion exchange, membrane separation, Multiple refinements such as crystallization, complex process, high production cost, and limited use (mainly used for injections for patients with diabetes and hypertension in medical treatment)

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] ——Add high-temperature α-amylase with an amount of 6.5 LU / g starch to cornstarch milk with a concentration of 25% and pH 5.8, and stir for 20 minutes;

[0033] ——Through the second spray liquefaction, the first time is 115°C, 30s; the second time is 125°C, 10min;

[0034] ——Cool to 92°C, add high-temperature α-amylase at the same time, spray liquefaction for the third time, 135°C, 5min;

[0035] ——Cool to 58°C, adjust the pH, add β-amylase, pullulanase and maltotriose hydrolase, synergistically hydrolyze for 24-48 hours, the enzyme dosage is 1.5DP / g starch, 0.6PUN / g starch and 4.0 MANU / g starch;

[0036] ——add medium-temperature amylase, 0.2KNU / g starch, and saccharify to 60hr;

[0037] At this time, the maltose content of the saccharified liquid was 94.5% high-purity maltose syrup.

[0038] - decolorize the above maltose syrup with activated carbon (75-80°C, 30min);

[0039] ——Ion exchange resin treatment, fine filtration through 0.45μm filter membrane;

[0040] —...

Embodiment 2

[0042] ——Add high-temperature α-amylase with an amount of 4.5LU / g starch to potato starch milk with a concentration of 15% and pH 5.4, and stir for 15 minutes;

[0043] ——Through the second spray liquefaction, the first time is 115°C, 30s; the second time is 125°C, 10min;

[0044] ——Cool to 90°C, add high-temperature α-amylase, spray liquefaction for the third time, 135°C, 5min;

[0045] ——Cool to 60°C, adjust pH, add β-amylase, pullulanase and maltotriose hydrolase, synergistically hydrolyze for 24-48 hours, the enzyme dosage is 1.2DP / g starch, 0.5PUN / g starch and 3.5 MANU / g starch;

[0046] ——add medium-temperature amylase, 0.18KNU / g starch, and saccharify to 60hr;

[0047] At this time, the maltose content of the saccharified liquid was 96% high-purity maltose syrup.

[0048] ——Adjust pH, add composite catalyst nickel-aluminum-molybdenum, carry out reduction reaction at specific temperature and hydrogen pressure, and obtain corresponding maltitol;

[0049] - Decolorize th...

Embodiment 3

[0055] ——Add high-temperature α-amylase with an amount of 7.2LU / g starch to cassava starch milk with a concentration of 30% and a pH of 5.6, and stir for 25 minutes;

[0056] ——Through the second spray liquefaction, the first time is 115°C, 30s; the second time is 125°C, 10min;

[0057] ——Cool to 88°C, add high-temperature α-amylase at the same time, spray liquefaction for the third time, 135°C, 5min;

[0058] ——Cool to 62°C, adjust the pH, add β-amylase, pullulanase and maltotriose hydrolase, synergistically hydrolyze for 24-48 hours, the enzyme dosage is 2.0DP / g starch, 0.7PUN / g starch and 5.5 MANU / g starch;

[0059] ——add medium-temperature amylase, 0.20KNU / g starch, and saccharify to 60hr;

[0060] At this time, the maltose content of the saccharified liquid was 92.5% high-purity maltose syrup.

[0061] ——Adjust pH, add composite catalyst nickel-aluminum-molybdenum, carry out reduction reaction at specific temperature and hydrogen pressure, and obtain corresponding malt...

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Abstract

The production process of high purity malt sugar products, including malt sugar syrup, malt sugar alcohol and solid malt sugar, includes the following steps: adding high temperature alpha-amylase into starch milk, spray liquefication, cooling, adding beta-amylase, pullulan enzyme and maltotriose hydrolase for synergetic hydrolysis, and adding medium temperature amylase to saccharify to obtain malt sugar syrup, which may be further processed to obtain other products. The present invention has simple technological process and low production cost, and expands the use of malt sugar syrup.

Description

technical field [0001] The invention relates to starch and starch sugar production technology, in particular to a production method of maltose products including high-purity maltose syrup, maltitol and solid maltose. Background technique [0002] High-purity maltose syrup is widely used as a nutritional sweetener and filling agent in the food industry such as high-grade candy, health drinks, oral liquids, malted milk extracts, pastries, and beverages; Prevent the occurrence of dental caries; in the pharmaceutical industry, various Chinese patent medicines and cough syrups can be prepared, which have the effects of moistening the lungs, treating abdominal pain, and coughing. [0003] High-purity maltose syrup can be used to produce maltitol after hydrogenation, and can also be used to produce pure maltose. High-purity maltitol has anti-caries activity and can be used as a low-calorie functional sweetener, fat substitute, and high-grade anti-caries ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): A23L33/125C13K7/00
Inventor 高群玉
Owner SOUTH CHINA UNIV OF TECH
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