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Separation method of D-glucuronic acid gamma-lactone

A glucuronic acid and separation method technology, applied in the field of separation of D-glucuronic acid γ-lactone, can solve the problems of difficult separation of crystals, easy decomposition of D-glucuronic acid, high cost, etc., to overcome the difficulty of crystal separation, The effect of reducing production cost and simplifying production process

Inactive Publication Date: 2010-08-04
SHAANXI UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] D-glucuronic acid γ-lactone has wide application prospects in the medicine, food, and health care products industries. At present, the nitric acid oxidation process is mainly used in the industry. The biggest disadvantage of this process is: serious pollution, and the product needs to be separated by low temperature freezing. High energy consumption, not in line with national industrial policies
However, this method uses butyl acetate as the secondary water-carrying agent, which has high cost, and due to the high boiling point of butyl acetate, D-glucuronic acid is easy to decompose, the liquid is viscous, and the problems of crystals being difficult to separate are still not well resolved. solve

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Example 1: 1) First, 100g corn starch, 150mL water and 0.1g FeSO 4 Add to a three-necked flask with stirring, adjust the pH to 10 with 0.1mol / L NaOH, and slowly add 6g of H while stirring 2 O 2 , React at 45℃ for 4h, after the reaction is heated to boiling to obtain oxidized starch liquid; the purpose is to allow excess H 2 O 2 Decompose by heating to avoid further oxidation of the aldehyde groups (glucuronic acid, glucose) in the enzymatic hydrolysis solution to obtain oxidized starch with carboxyl content ≥ 8% and carbonyl content ≤ 0.2%;

[0016] 2) Cool and adjust the pH of the oxidized starch solution to 6.2, add the α-amylase with an activity of 20000μ / g at the ratio of 120μα-amylase / g starch, hydrolyze it at 90℃ for 0.5h, and then heat it to boiling. Keep it for 10 minutes to kill α-amylase to obtain liquefied liquid;

[0017] 3) Cool the liquefied liquid to 62°C and adjust its pH to 4.5. Add the glucoamylase with an activity of 10000μ / g at the ratio of 120μ glucoamyla...

Embodiment 2

[0021] Example 2: 1) First, 100g corn starch, 180mL water and 0.08g FeSO 4 Add to a three-necked flask with stirring, adjust the pH to 9 with 0.1mol / L NaOH, slowly add 8g of H while stirring 2 O 2 , React at 45℃ for 4h, after the reaction is heated to boiling to obtain oxidized starch liquid; the purpose is to allow excess H 2 O 2 Decompose by heating to avoid further oxidation of the aldehyde groups (glucuronic acid, glucose) in the enzymatic hydrolysis solution to obtain oxidized starch with carboxyl content ≥ 8% and carbonyl content ≤ 0.2%;

[0022] 2) Cool and adjust the pH of the oxidized starch solution to 6.5, add the α-amylase with an activity of 20000μ / g at the ratio of 140μα-amylase / g starch, hydrolyze it at 86°C for 1.5h, and then heat it to boiling. Keep it for 10 minutes to kill α-amylase to obtain liquefied liquid;

[0023] 3) Cool the liquefied liquid to 65°C and adjust its pH to 4.2, add glucoamylase with an activity of 10000μ / g at the ratio of 140μ glucoamylase / g st...

Embodiment 3

[0027] Example 3: 1) First, 100g corn starch, 160mL water and 0.05g FeSO 4 Add to a three-necked flask with stirring, adjust the pH to 11 with 0.1mol / L NaOH, and slowly add 5g of H while stirring 2 O 2 , React at 45℃ for 4h, after the reaction is heated to boiling to obtain oxidized starch liquid; the purpose is to allow excess H 2 O 2 Decompose by heating to avoid further oxidation of the aldehyde groups (glucuronic acid, glucose) in the enzymatic hydrolysis solution to obtain oxidized starch with carboxyl content ≥ 8% and carbonyl content ≤ 0.2%;

[0028] 2) Cool and adjust the pH of the oxidized starch solution to 6.0, add the α-amylase with an activity of 20000μ / g at the ratio of 100μ α-amylase / g starch, hydrolyze at 88°C for 1h, then heat to boiling and keep 10min, kill α-amylase to obtain liquefied liquid;

[0029] 3) Cool the liquefied liquid to 61°C and adjust its pH to 4.0, add glucoamylase with an activity of 10000μ / g at the ratio of 100μ glucoamylase / g starch, and keep it...

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Abstract

The invention relates to a separation method of D-glucuronic acid gamma-lactone, which carries out alcoholic fermentation on glucose and other fermentable saccharides in a zymolysis product by adopting an alcoholic fermentation process according to the property differences of oxidized starch and the zymolysis product to seperate the glucuronic acid of the zymolysis product from the glucose and other fermentable saccharides. The invention reduces the dosage of alcohol, thereby lowering the production cost of glucuronic acid lactone. Each index of the glucuronic acid obtained by the separation method meets the standard of the national formulary, and the invention simplifies the production process and lowers the production cost.

Description

Technical field [0001] The invention belongs to the production field of pharmaceutical raw materials or health care products, and particularly relates to a method for separating D-glucuronic acid γ-lactone. Background technique [0002] D-glucuronic acid γ-lactone has a wide range of application prospects in the medicine, food, and health care industry. At present, the industry mainly uses nitric acid oxidation process. The biggest disadvantage of this process is: serious pollution, and the product needs to be frozen and separated at low temperature. The energy consumption is relatively large, which does not conform to the national industrial policy. The glucuronide oxidation method is used to produce glucuronide in foreign countries. The oxidation reaction requires Pt / C as a catalyst, which is costly and the catalyst is not easy to obtain. Yuan Hua et al. used the method of loading oxidizer to load Pt in the perovskite. To a certain extent, the production cost is reduced, but t...

Claims

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Application Information

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IPC IPC(8): C12P19/00C12P19/14C07H13/02C07H1/06C12R1/865
Inventor 李祥马建中王勇赵倩张青郭凌华
Owner SHAANXI UNIV OF SCI & TECH