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Process for producing starch sugar

A production process and technology for starch sugar, applied in the field of starch sugar production technology, can solve the problems of unfriendly environment, poor production environment, increase the color of saccharification liquid and difficulty in refining, etc., and achieve improved purity, low operating cost, and removal of macromolecules. material effect

Active Publication Date: 2012-02-01
双桥(厦门)有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional production process of starch sugar is liquefaction, saccharification, decolorization, plate-and-frame filter press or vacuum drum filter filtration, ion exchange, and concentration. During the saccharification process, a large amount of sugar residue containing impurities such as protein and fat exists, which affects the glucoamylase. effect, and the decomposition of miscellaneous enzymes contained in the enzyme preparation produces by-products and pigments, which increases the color of the saccharification solution and the difficulty of refining; and because there are a large amount of impurities such as protein and fat, diatomaceous earth or perlite must be used Only filter aids and activated carbon can decolorize and filter the sugar liquid smoothly. Sugar residues containing filter aids or activated carbon cannot be used as raw materials for animal feed, and can only be discharged as solid waste, which is not environmentally friendly; plate and frame filter press and vacuum transfer Traditional starch sugar filtration equipment such as drum filter is intermittently produced, and there is a large amount of solid waste and sewage from cleaning equipment, and the production environment is relatively poor.

Method used

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  • Process for producing starch sugar

Examples

Experimental program
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Effect test

Embodiment 1

[0040] (1) Starch mixing: 100 parts by mass of cornstarch and water are added to make starch milk with 18-19 degrees Baume, and the pH value is adjusted to 5.4 with 5% dilute hydrochloric acid solution or 5% sodium carbonate solution ~5.6, add Liquozyme Supra high temperature resistant α-amylase equivalent to 0.030% of the edible starch mass;

[0041] (2) Liquefaction: At 105°C~110°C, the material is continuously sprayed for 5 minutes for the first time, and after flash evaporation, it is kept at 95~100°C for 90 minutes; then at 130°C~135°C, the material is subjected to the second spraying Continuous spray treatment for 3 minutes, flash depressurization and temperature reduction, liquefied liquid at 98 ° C for 20 minutes;

[0042] (3) Primary extraction of sugar slag: the liquefied liquid directly enters the first-stage floater without cooling down, and the liquefied liquid passes through the floater for 20 minutes. The clear liquid from the bottom of the device flows out of ...

Embodiment 2

[0049] (1) Starch mixing: 100 parts by mass of cornstarch, add water to make starch milk with 16-17 degrees Baume, adjust the pH value to 5.4 with 5% dilute hydrochloric acid solution or 5% sodium carbonate solution ~5.6, add Liquozyme Supra high temperature resistant α-amylase equivalent to 0.030% of the edible starch mass;

[0050] (2) Liquefaction: At 105°C~110°C, the material is continuously sprayed for 5 minutes for the first time, and after flash evaporation, it is kept at 95~100°C for 60 minutes; then at 125°C~130°C, the material is subjected to the second spraying Continuous spraying treatment for 3 minutes, after flash depressurization and cooling, add 0.005% edible starch quality Liquozyme Supra high-temperature-resistant α-amylase, and keep the liquefied solution at 98°C for 20 minutes;

[0051] (3) Primary extraction of sugar slag: the liquefied liquid directly enters the primary floater without cooling down. The time for the liquefied liquid to pass through the fl...

Embodiment 3

[0058] (1) Starch mixing: 100 parts by mass of cornstarch, add water to make starch milk with 16-17 degrees Baume, adjust the pH value to 5.4 with 5% dilute hydrochloric acid solution or 5% sodium carbonate solution ~5.6, add Liquozyme Supra high temperature resistant α-amylase equivalent to 0.030% of the edible starch mass;

[0059] (2) Liquefaction: At 105°C~110°C, the material is continuously sprayed for 5 minutes for the first time, and after flash evaporation, it is kept at 95~100°C for 60 minutes; then at 125°C~130°C, the material is subjected to the second spraying Continuous spraying treatment of 3min, flash depressurization and temperature reduction, liquefied liquid is kept at 98°C for 20min;

[0060] (3) Primary extraction of sugar slag: the liquefied liquid is cooled to 65-75°C and enters the primary floater. The time for the liquefied liquid to pass through the floater is 30 minutes. Adjust the outflow valve of the lower clear liquid of the floater to control the...

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Abstract

The invention discloses a process for producing starch sugar. The process comprises the following steps of: pulp-conditioning edible starch; liquefying; passing liquefied starch through a primary floating clarifier, guiding an upper floating sugar dreg liquid into a primary buffer tank, and then entering a primary disc-type centrifuge to be centrifugated and separated so as to extract sugar dregs; combining a clear sugar liquid flowing out of the primary disc-type centrifuge and a clear sugar liquid flowing out of the primary floating clarifier and flowing into a saccharifying tank to be saccharified into a saccharified liquid; passing the saccharified liquid through a secondary floating clarifier, guiding an upper floating sugar dreg liquid into a secondary buffer tank, and then enteringa secondary disc-type centrifuge to be separated so as to extract sugar dregs; combining a clear sugar liquid flowing out of the secondary disc-type centrifuge and a clear sugar liquid flowing out ofthe secondary floating scum clearing device and filtering by passing through a membrane micro-filtration system; and flowing a micro-filtered concentrated liquid containing dregs back to the secondary buffer tank, entering a micro-filtered clear sugar liquid into an ion exchange system to be decolorized and desalted, and then finally concentrating into a product. According to the process for producing the starch sugar disclosed by the invention, filter aids and activated carbon are not required in the clarification and the filtration processes, and high-purity sugar liquid can be obtained through the efficient operation of solid-liquid separation equipment; and meanwhile, sugar dregs without the filter aids and the activated carbon are extracted and can be used as a feedstuff raw materialfor animals, thereby changing waste into valuable, and no discharge of filtered solid wastes during the whole process exists.

Description

technical field [0001] The invention relates to a starch sugar production process, in particular to a starch sugar production process in which filter aid and activated carbon are not required to be added during the clarification process of starch sugar liquid, and sugar residue without filter aid or activated carbon is simultaneously obtained. Background technique [0002] Starch sugar is more and more widely used in various fields. As a bee feed and fermentation carbon source, especially in the food industry such as beverages, candies, cakes, beer, chewing gum, soy sauce, etc., it has obvious advantages over other sweeteners. With the improvement of people's consumption concept and consumption level, the demand for starch sugar continues to increase, and the improvement of the production capacity and product quality of starch sugar is particularly important. [0003] The clarification, filtration and decolorization of starch sugar is one of the key steps in the production ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C12P19/22C12P19/20C12P19/14C12P19/02A23K1/00A23K20/163
Inventor 徐正康周彦斌罗建勇黄立新陈文峰周春海冯炳洪万振平汤桂标徐丽霞
Owner 双桥(厦门)有限公司
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