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Industrial production method for extracting stachyose from radix rehmanniae

A production method, the technology of stachyose, is applied in the field of industrialized production of extracting stachyose from Rehmannia glutinosa, which can solve the problems of complex processing aids, high operating costs, and inapplicability to industrial production, so as to reduce product risk and process aids. The effect of less agent and easy operation of equipment

Inactive Publication Date: 2016-02-10
CHINA NAT RES INST OF FOOD & FERMENTATION IND CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The above technologies all use rehmannia glutinosa as raw material to produce stachyose products, but there are the following technical defects: 1) the purity of stachyose is not high, and the yield is low; 2) the process is complicated, the operation cost is high, and it is not suitable for industrial production; 3) The complexity of processing aids reduces the controllability of product risks: for example, the use of macroporous adsorption resins will increase the possibility of introducing heavy metal ions into the final product

Method used

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  • Industrial production method for extracting stachyose from radix rehmanniae

Examples

Experimental program
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Effect test

Embodiment 1

[0024] (1) Juice extraction: according to the mass ratio of 1:6, add water to 200kg of dried raw land slices and extract at 85°C for 1 hour, take the juice, take the residue and continue to extract the juice for 3 times according to the above process, the obtained juice is mixed and then pumped into the sandwich pot;

[0025] (2) Impurity removal: Heat the liquid in the jacketed pot to 70°C, pass through a 200-mesh vibrating screen, and then pump it into a centrifuge to remove impurities;

[0026] (3) Decolorization: pump the centrifuged supernatant into a decolorization tank, heat it to 80°C, add activated carbon powder 10‰ (m / v), diatomaceous earth 3‰ (m / v), and keep warm for 1 hour for decolorization. Pump the decolorized feed liquid into the plate and frame filter for filtration, and the filtrate is introduced into the storage tank;

[0027] (4) Ion exchange: Cool the feed liquid in the storage tank to 20°C, pump the feed liquid into the anion and cation column for decont...

Embodiment 2

[0031] (1) Juice extraction: According to the mass ratio of 1:10, add 400kg of fresh rehmannia glutinosa slices and add water to leaching for 4 hours at 40°C, take the juice, take the residue and continue to extract the juice once according to the above process, and mix the obtained juice Then pump into the jacketed pot;

[0032] (2) Impurity removal: Heat the liquid in the jacketed pot to 45°C, pass through a 200-mesh vibrating screen, and then pump it into a centrifuge to remove impurities;

[0033] (3) Decolorization: pump the centrifuged supernatant into a decolorization tank, heat it to 65°C, add activated carbon powder 40‰ (m / v), diatomaceous earth 8‰ (m / v), and keep warm for 1.5 hours for decolorization. Pump the decolorized feed liquid into the plate and frame filter for filtration, and the filtrate is introduced into the storage tank;

[0034] (4) Ion exchange: Cool the feed liquid in the storage tank to 15°C, pump the feed liquid into the anion and cation column for...

Embodiment 3

[0038] (1) Juice extraction: According to the mass ratio of 1:2, add water to 200kg of dried raw land slices and extract at 90°C for 0.5 hours to extract the juice, continue to extract the juice from the residue according to the above process for 5 times, mix the obtained juice and pump it into the sandwich pot;

[0039] (2) Impurity removal: heat the liquid in the jacketed pot to 85°C, pass through a 200-mesh vibrating screen, and then pump it into a centrifuge to remove impurities;

[0040] (3) Decolorization: pump the centrifuged supernatant into a decolorization tank, heat it to 95°C, add 1‰ (m / v) of activated carbon powder, 1‰ (m / v) of diatomaceous earth, and keep warm for 0.5 hours for decolorization. Pump the decolorized feed liquid into the plate and frame filter for filtration, and the filtrate is introduced into the storage tank;

[0041] (4) Ion exchange: Cool the feed liquid in the storage tank to 30°C, pump the feed liquid into the anion and cation column for dec...

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Abstract

The invention relates to an industrial production method for extracting stachyose from radix rehmanniae. The method comprises the following steps: (1) carrying out juice extraction; (2) carrying out impurity removal; (3) carrying out decoloring; (4) carrying out ion exchange; (5) carrying out vacuum concentration; and (6) carrying out sterilizing and spray drying, thereby obtaining a powdery stachyose product, of which the stachyose purity is higher than 70%.

Description

technical field [0001] The invention relates to a production method of stachyose, in particular to an industrial production method for extracting stachyose from rehmannia glutinosa. Background technique [0002] Stachyose is a functional oligosaccharide that naturally exists in the Lamiaceae stachyus plant and can significantly promote the proliferation of beneficial bacteria in the human intestinal tract. It is known as "natural super strong bifidus factor". Stachyose has a clear structure, molecular formula C 24 h 42 o 21 , molecular weight 666.59, it is composed of fructose, glucose, galactose, and galactose polymerization, and the effective usage amount is 0.5-3 grams per day. At present, stachyose in the market is obtained by extracting and separating the traditional Chinese vegetable caddis worm as raw material. Compared with products such as isomalto-oligosaccharide and fructo-oligosaccharide (effective use amount 8-15 g / day) obtained through enzyme engineering tra...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07H3/06C07H1/08
Inventor 张金泽周志桥林静高加涛段素芳桑若杰
Owner CHINA NAT RES INST OF FOOD & FERMENTATION IND CO LTD
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