CN1012960B - Refining method of glucomannan in konjak - Google Patents

Refining method of glucomannan in konjak

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Publication number
CN1012960B
CN1012960B CN 88106313 CN88106313A CN1012960B CN 1012960 B CN1012960 B CN 1012960B CN 88106313 CN88106313 CN 88106313 CN 88106313 A CN88106313 A CN 88106313A CN 1012960 B CN1012960 B CN 1012960B
Authority
CN
China
Prior art keywords
glucomannan
acid
lower alcohol
product
anhydrating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
CN 88106313
Other languages
Chinese (zh)
Other versions
CN1040799A (en
Inventor
胡海宁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
No10 Inst Of No9 Academy Ministry Of Nuclear Industry
Original Assignee
No10 Inst Of No9 Academy Ministry Of Nuclear Industry
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by No10 Inst Of No9 Academy Ministry Of Nuclear Industry filed Critical No10 Inst Of No9 Academy Ministry Of Nuclear Industry
Priority to CN 88106313 priority Critical patent/CN1012960B/en
Publication of CN1040799A publication Critical patent/CN1040799A/en
Publication of CN1012960B publication Critical patent/CN1012960B/en
Expired legal-status Critical Current

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  • Preparation Of Fruits And Vegetables (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

The invention provides a novel method for extracting glucomannan from konjak. The method adds lower carboxylic acid (citric acid, malic acid or acetic acid) into lower alcohol (ethanol) dehydration solvent, and adopts multiple extraction method, so that the product has no discoloration for a long time, no fishy smell and no numb taste, and especially the product precision is greatly improved. The method has the advantages of low cost, simple operation, and high extraction rate, and is suitable for industrial production.

Description

Refining method of glucomannan in giantarum
A kind of method of extracting glucomannan, the particularly method of extraction glucomannan from konjaku.
The method of extracting glucomannan from konjaku has two big classes, and a class is a dry method, and another kind of is wet method.Dry method is with Exposure to Sunlight or the section of warm air drying konjaku, pulverizes grinding for a long time with stamp box or crushing type powder-making machine then and extracts.This method production cycle is long, and extraction yield is low, labor capacity is big, product viscosity is low, color and taste is not good.Day disclosure several wet methods extract the method for glucomannans.Disclose konjaku and mix with anhydrating property solvent (methyl alcohol or ethanol) in Japanese Patent (special public clear 46-39055), pulverized, grind, separate, products obtained therefrom viscosity has improved, and labour intensity is also little, but the product color and taste is not good.Disclose in the Japanese Patent (special public clear 46-39054) and in anhydrating property solvent (lower alcohols), added sulfurous acid alkalescence metal-salt with the color in the bleach product.Though the product that this method obtains is white, placing for some time still can variable color, and taste is not good yet.Have a fish like smell, and contain impurity such as sulphur, alkaloid is also higher in the product, has influenced the quality of product, and extraction yield is also lower in addition.
The purpose of this invention is to provide a kind of quality product height (Se Bai and for a long time nondiscoloration, viscosity height, contain low, the objectionable impurities such as sulfur-bearing not of biological alkali number), extraction yield height, the glucomannan process for purification that productive rate is high.
The present invention adopts anhydrating property of the lower alcohol solvent that has added the low-grade carboxylic acid to remove the impurity in the glucomannan in the konjaku, the low-grade carboxylic acid is inhibited to the tannin pigment dyeing, and alkaloid had salification, the lower alcohol aqueous solution has the extraction separation effect to impurity such as alkaloid, sulphur.Again through the repeatedly purification of lower alcohol, just can obtain the purified glucomannan through the glucomannan after the above-mentioned purification.
Embodiment of the present invention are described in detail in detail below.
The present invention mixes konjaku piece base with anhydrating property of the lower alcohol solvent that has added the low-grade carboxylic acid, broken the wiping of konjaku piece base then, further grinds, and again through centrifugation, discards waste liquid, and precipitation is the thick product of glucomannan.This crude product and the lower alcohol solvent that anhydrates is mixed again, grind, centrifugation repeatedly for several times, thereby obtains high-quality glucomannan.
The present invention has added the low-grade carboxylic acid in anhydrating property of lower alcohol solvent can suppress the effect of tannin pigment dyeing, thereby has guaranteed the white and nondiscoloration of product look, and should acid to alkaloid salification be arranged, thereby has further removed the alkaloid in the product.Anhydrating property solvent mixes with konjaku earlier, can improve the viscosity of product like this.Thick product mixes with anhydrating property of the lower alcohol solvent that does not contain the low-grade carboxylic acid again, and then grinds, separates, and this process 2~5 times has repeatedly further improved product purity, and has improved product viscosity (seeing Table 1).The lower alcohol that the present invention adopts is the aqueous solution such as methyl alcohol, ethanol, and its concentration is 40~80%(volume ratio).The low-grade carboxylic acid is citric acid, oxysuccinic acid or acetic acid, and its add-on is 15~40g/l.The present invention is not high to ingredient requirement yet, can be fresh Amorphophallus rivieri, can be that konjaku is done and coarse products yet.
Embodiment 1: the 5kg fresh Amorphophallus rivieri is mixed with 80%41 ethanolic solns that contain the 125g citric acid, wipe then broken, grind and separate, the glucomannan particle of gained mixes with 2145% ethanolic soln again, and grind, separate, this process repeats once again, just can obtain purified glucomannan particle, purified product was descended dry 4 hours at 70 ℃, just can get qualified product.
Embodiment 2: will mix with 60% ethanolic soln that has heavier fish raw meat pungent taste, 1kg glucomannan particle and 4.51 that color and luster is darker to contain citric acid 50g that dry method makes and stir 40 minutes, and grind, separate, products obtained therefrom is 70 ℃ of oven dry 2.5 hours down.Glucomannan after this art breading is hairtail fishy smell not, and viscosity is improved significantly, and the viscosity number of particle sees Table 2 before and after handling with the portable viscometer determining of NXX-1H.
The glucomannan outward appearance of being extracted by the present invention is snow-white, and good stability, places still to keep original color and luster after 1 year, does not have pungency fishy smell and numb taste, keeps the natural fresh and sweet fragrance of konjaku.Viscosity improves greatly, and alkaloid 0.129% does not have the pollution of materials such as sulfur-bearing, and productive rate also improves greatly, and day present method extraction yield is 7.5~8.4%, and this law is 8.1~10.2%.
Table 1 viscosity ratio
The each time viscosity of starting material solvent total amount access times (1% aqueous solution,
(g) (ml) (branch) CP, 25 ℃)
Known method 1,500 1,000 13 4762
The present invention 1,500 1,000 3 1/3 20315
Glucomannan viscosity (25 ℃ of 1% aqueous solution) before and after table 2 is handled
Dry method particle 5.6(Pas)
This law particle 7.4(Pas)

Claims (4)

1, a kind of method of from konjaku, extracting glucomannan, it is characterized in that konjaku mixes with anhydrating property of the lower alcohol solvent that has added the low-grade carboxylic acid, carry out coarse reduction, grinding then and separate, the particle after the separation mixes with anhydrating property of lower alcohol solvent again, grinds then and separates.
2, extracting method as claimed in claim 1 is characterized in that the low-grade carboxylic acid is citric acid, oxysuccinic acid or acetic acid, and citric acid adding amount is 15~40g/l solution.
3, extracting method as claimed in claim 2 is characterized in that lower alcohol is methyl alcohol, ethanol, and alcohol concn is 40~80%.
4, extracting method as claimed in claim 1, the particle after it is characterized in that separating mixes with anhydrating property of lower alcohol solvent again, grinds then and separates, and its number of times is 2~5 times.
CN 88106313 1988-09-03 1988-09-03 Refining method of glucomannan in konjak Expired CN1012960B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 88106313 CN1012960B (en) 1988-09-03 1988-09-03 Refining method of glucomannan in konjak

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 88106313 CN1012960B (en) 1988-09-03 1988-09-03 Refining method of glucomannan in konjak

Publications (2)

Publication Number Publication Date
CN1040799A CN1040799A (en) 1990-03-28
CN1012960B true CN1012960B (en) 1991-06-26

Family

ID=4834193

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 88106313 Expired CN1012960B (en) 1988-09-03 1988-09-03 Refining method of glucomannan in konjak

Country Status (1)

Country Link
CN (1) CN1012960B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1044964C (en) * 1994-10-06 1999-09-08 华南农业大学 Process for fine konjak powder
CN1081009C (en) * 1996-12-18 2002-03-20 杨康康 Process for making konjaku water solutable edible fiber
CN1058268C (en) * 1998-10-06 2000-11-08 干信 Method for production of fatty amide sodium glucosiduronic acids mannitose from fine powder of konjak
CN100386344C (en) * 2006-04-11 2008-05-07 武汉大学 Quaternary ammonium konjac glucomannan derivatives and their preparation process and use
ATE512990T1 (en) * 2007-11-13 2011-07-15 Cargill Inc METHOD FOR PRODUCING PURIFIED BETA-(1,3)-D-GLUCANS
CN107141368A (en) * 2017-06-21 2017-09-08 安康市巴山佳芋食品有限公司 The extracting method of glucomannans in a kind of konjaku

Also Published As

Publication number Publication date
CN1040799A (en) 1990-03-28

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