High yield method for combined production of crystallized fructose, mannitol and sorbierite

A technology for crystallizing fructose and mannitol, applied in the field of preparation of hexavalent alcohol, can solve the problems of difficult filtration, poor quality of mannitol and high production cost, and achieve the effects of reducing concentration consumption, reducing evaporation load and improving utilization rate

Inactive Publication Date: 2007-07-11
SHANDONG XIWANG SUGAR
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the source of inulin is mainly extracted from the fruit of the plant Jerusalem artichoke, and it is difficult to source raw materials for industrial production.
(3) Carry out enzymatic conversion of mannose under the action of mannose isomerase, the conversion rate can reach more than 80%, and then crystallize to obtain crystalline fructose, but the source of mannose is very problematic, and mannose isomerization Enzymes cannot be mass-produced industrially, and industrial production cannot be realized, and this method is not advisable
However, the source of pure mannose is problematic and does not meet the requirements of industrial production
(4) Electrolytic reduction method: glucose can be reduced under electrolytic conditions to generate a mixture of mannitol and sorbitol, and then crystallized and extracted to obtain mannitol. This method has long reaction time, low efficiency, large power consumption, and low yield, only 15 %about
(5) Kelp extraction method: Dried kelp contains 5% to 15% mannitol, which can be extracted by physical crystallization after concentration. The mannitol extracted by this method is of poor quality, difficult to filter, and high heat source, so it is not suitable for It is used in medicine, and this method consumes a lot of steam, energy and manpower, and the production cost is too high
(6) Using glucose as raw material: epimerizing glucose into mannose (the conversion rate is generally 27% to 33%) and hydrogenating invert sugar to obtain a mixture of about 30% mannitol sorbitol, which is crystallized The mannitol product is obtained. This method has an industrialized production device, but the yield is not high, only reaching 24% to 26%.
However, in the methods related to the preparation of crystalline fructose, mannitol and sorbitol in the prior art, there is no report on the method of co-producing crystalline fructose, mannitol and sorbitol with starch raw material as raw material with high yield

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] (1) Starch raw material A is formulated into starch milk with a concentration of 30% by weight, and the pH is adjusted to 5.5 with soda ash. After adding high-temperature-resistant amylase, liquefaction and saccharification are carried out by conventional methods to obtain a concentration of 35% and a glucose value of 96. % invert sugar solution B.

[0041] (2) Invert sugar solution B is filtered, decolorized, and ion-exchange resin is used to remove impurities in a conventional manner, then evaporated to a dry matter weight percentage concentration of 50%, adjust the pH to 8.15, add 45ppm of magnesium ions, and dissolve at a temperature of 60°C. The isomerized sugar solution C containing 42% fructose, 53% glucose and 5% oligosaccharide was obtained after the reaction for 3 hours.

[0042] (3) Utilize the simulated moving bed device to process the isomerized sugar liquid C to separate fructose and glucose; use calcium-type cation exchange resin as the adsorbent, use wat...

Embodiment 2

[0053] (1) The starch raw material A is prepared into starch milk with a concentration of 27% by weight, the pH is adjusted to 5.8 with soda ash, and after adding high-temperature-resistant amylase, liquefaction and saccharification are carried out in a conventional method to obtain invert sugar solution B;

[0054] (2) Invert sugar solution B is filtered, decolorized, and ion-exchange resin is used to remove impurities in a conventional manner, then evaporated to a dry matter weight percentage concentration of 45%, adjust the pH to 8.25, add 43ppm of magnesium ions, and isotropic at a temperature of 58 ° C. After 2.5 hours of structuring reaction, isomerized sugar solution C containing fructose, glucose and oligosaccharides was obtained;

[0055] (3) Utilize the simulated moving bed device to process the isomerized sugar solution C to separate fructose and glucose; use calcium-type cation exchange resin as the adsorbent, and use water as the eluent to continuously feed, water,...

Embodiment 3

[0066] (1) The starch raw material A is prepared into starch milk with a concentration of 32% by weight, the pH is adjusted to 5.2 with soda ash, and after adding high-temperature-resistant amylase, liquefaction and saccharification are carried out in a conventional method to obtain invert sugar solution B;

[0067] (2) Invert sugar solution B is filtered, decolorized, and ion-exchange resin is used to remove impurities in a conventional manner, then evaporated to a dry matter weight percentage concentration of 55%, adjust the pH to 8.1, add 48ppm of magnesium ions, and isotropic at a temperature of 56°C. After 4 hours of structuring reaction, isomerized sugar solution C containing fructose, glucose and oligosaccharides was obtained;

[0068] (3) Utilize the simulated moving bed device to process the isomerized sugar solution C to separate fructose and glucose; use calcium-type cation exchange resin as the adsorbent, and use water as the eluent to continuously feed, water, and ...

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PUM

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Abstract

The invention discloses a high receiving rate joint crystallizing method of fructose, mannitol and sorbitol, which comprises the following steps: enzymolyzing starch into glucose; transmitting glucose into fructose through glucose isomerase; separating fructose from glucose through analoging mobile bed; obtaining the component with rich fructose and glucose; crystallizing the fructose; transmitting glucose into mannitol under acid condition based on molybdate as catalyst; separating the mannitol from glucose; blending glucose component and glucose mother liquid to saccharify; combining the glucose component; repeating the epimerism reaction; combining the mannitol and crystallized fructose mother liquid; hydrogenating; obtaining the composite alcohol solution with mannitol and sorbitol; crystallizing; refining to obtain the mannitol crystal.

Description

technical field [0001] The invention relates to a preparation method of hexahydric alcohol, in particular to a method for co-producing crystallized fructose, mannitol and sorbitol with high yield by using starch raw material as raw material. Background technique [0002] At present, the industrial method of producing crystalline fructose has the following several according to raw material source: (1) take sucrose as raw material, through hydrolysis, obtain the mixture of fructose and glucose, through adsorption separation, obtain high-purity fructose and glucose, high-purity fructose is passed through Crystallization and separation can obtain crystalline fructose, but the yield of this method is low. (2) The inulin can be 100% converted into fructose by hydrolyzing it. However, the source of inulin is mainly extracted from the fruit of the plant Jerusalem artichoke, and it is difficult to source raw materials for industrial production. (3) Carry out enzymatic conversion of...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C12P19/02C12P7/18
Inventor 王勇李伟阿纳斯孙宗宝滕俊强崔立平杨会敏
Owner SHANDONG XIWANG SUGAR
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