Method for extracting diosgenin for joint production of starch suger by prehy drolysis of yellow ginger by multienzyme process

A starch sugar, pre-hydrolysis technology, applied in steroids, fermentation, organic chemistry and other directions, can solve the problems of large consumption of raw materials, large amount of wastewater, low alcohol concentration, etc., to reduce the total amount of acid hydrolyzate, chemical consumption The effect of decreasing oxygen content and increasing saponin yield

Inactive Publication Date: 2004-09-15
TAIGU INVESTMENT WUHAN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Fresh turmeric contains starch ≥ 18%, and dried turmeric contains starch ≥ 45%, which is discharged from waste water after acid hydrolysis, resulting in waste of resources
[0004] 2. The composition of wastewater is complex, the discharge volume is large, and the pollution is serious
[0005] 3. The yield of saponin is low, and the consumption of raw materials is large. The yield of fresh turmeric saponin is 0.6-0.8%, and the yield of dry turmeric saponin is 1.8-2.0%.
This method has the following disadvantages: 1. in order to ensure the saponin yield when separ

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Fresh turmeric 1000g, soak in water at normal temperature for 6 hours, wash it, and pulverize it with a universal pulverizer to obtain a slurry with a particle size of about 1mm, mix it with water according to the ratio of fresh turmeric to water 1:2.5; place the slurry in Rapidly heat up to 90-95°C in a 5000ml beaker, add 2.0ml (enzyme solution concentration 18000U / L, the same below) commercially available α high-temperature amylase, and enzymolyze at 90-95°C for 2.5 hours under stirring; wait until the temperature drops to 55 ℃, add 3.5ml (enzyme solution concentration 18000U / L the same below) commercially available glucoamylase, react at 55-60℃ and pH4-5 for 8 hours to obtain saccharified material; saccharified material is centrifuged to obtain filter cake and sugar solution, the saccharified solution is filtered with a hollow fiber UF membrane at 40-50°C; the centrifugal filter cake and the membrane filter residue are combined, and a hydrochloric acid solution with a...

Embodiment 2

[0020] Soak 400g of dried turmeric slices (moisture content 10%) in water at room temperature for 10 hours, wash it, and pulverize it with a universal grinder to obtain a powder with a particle diameter of about 4mm. The powder is 1:6.5 according to the ratio of turmeric to water Mix and refine to obtain a slurry with a particle size of 0.5-1mm; place the slurry in a 5000ml beaker and rapidly heat up to 85°C, add 3ml of commercially available α-medium-temperature amylase (the same as the enzyme solution concentration of 18000U / L), and stir Enzymolysis at 80-90°C for 2 hours; when the temperature dropped to 55°C, add 4.5ml of commercially available glucoamylase, react at 55-60°C and pH4-5 for 10 hours to obtain a saccharification solution; the saccharification solution was separated by centrifugation , its filtrate is 100nm zirconia membrane filtration with aperture at 40-50 DEG C; Combine centrifugal filter cake and membrane filter residue, add the hydrochloric acid solution of...

Embodiment 3

[0022] 1000g of fresh turmeric, soaked in water at normal temperature for 8 hours, washed it, and pulverized it with a universal pulverizer to obtain a powder with a particle size of 2-3mm. The powder was mixed and refined according to the ratio of turmeric and water in a ratio of 1:2. Obtain a slurry with a particle size of 0.5-1mm; place the slurry in a 5000ml beaker and rapidly heat up to 95°C, add 4ml of commercially available α-high temperature amylase, and enzymolyze it at 95-100°C for 3 hours under stirring; wait until the temperature drops to At 60°C, add 2.0ml of commercially available glucoamylase, and react at 55-60°C and pH4-5 for 6 hours to obtain a saccharified liquid; the saccharified liquid is separated by centrifugation, and the filtrate is oxidized at 40-50°C with a pore size of 200nm Aluminum membrane filtration; Merge centrifugal filter cake and membrane filter residue, add water 500ml to wash filter residue, add the hydrochloric acid solution of concentrati...

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Abstract

The invention provides a saponin extracting method with multi-enzyme hydrolytic which hydrolyses brown Windsor in advance and produce starch sugar. The method cleans the brown Windsor and grinds it into pulp, then adds in alpha starch enzyme to be liquefied, adds in saccharifying enzyme, heats and carries on deactivation, then the saccharified materials are separated centrifugally, gets the filtered cake and starch sugar liquiud, the sugar liquid is separated with hyperfiltration membrane with 1000-10000daltons aperture catching molecular weight or tiny filtration membrane of 100-200nm and gets the starch sugar liquid, the filter residues are mixed into centrifugated filter cake and gets sugar residue, adds in chlorhydric acid or sulfuric acid to hydrolyse the sugar residue, the hydrolysed product is filtered, cleaned, and dried, extracted by solvent, finally gets the saponin product.

Description

technical field [0001] The invention relates to a method for extracting saponin (sapogenin) by using Dioscorea scutellariae and turmeric to prehydrolyze and co-produce starch sugar through a multi-enzyme method. Background technique [0002] At present, most of the methods for domestic production of saponin are to adopt the process of direct acid hydrolysis of turmeric to prepare saponin after crushing and pre-fermentation. This method mainly has the following problems: [0003] 1. The starch component of turmeric has not been utilized. Fresh turmeric contains starch ≥ 18%, dried turmeric contains starch ≥ 45%, and it is discharged from waste water after acid hydrolysis, resulting in waste of resources. [0004] 2. The composition of wastewater is complex, the discharge volume is large, and the pollution is serious. Wastewater discharged per ton of saponin 450-500M 3 , where COD value is 30000~110000mg / L; pH value: 0.2-1.5. [0005] 3. The yield of saponin is low, and th...

Claims

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Application Information

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IPC IPC(8): C07J71/00C12P19/14C12P33/20
Inventor 李华才徐晓东郭永龙张金安
Owner TAIGU INVESTMENT WUHAN
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