CN1373135A - Process for extracting L-arabinose from acacia gum by two-column method - Google Patents
Process for extracting L-arabinose from acacia gum by two-column method Download PDFInfo
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- CN1373135A CN1373135A CN 02116353 CN02116353A CN1373135A CN 1373135 A CN1373135 A CN 1373135A CN 02116353 CN02116353 CN 02116353 CN 02116353 A CN02116353 A CN 02116353A CN 1373135 A CN1373135 A CN 1373135A
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- arabinose
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Abstract
A two-column process for extracting L-arabinose from acacia gum includes hydrolyzing in inorganic acid, alkali neutralizing, extracting in alcohol, filtering, dissolving in acetic acid at 60-90 deg.C to obtain coarse L-arabinose mixture, separating by the first column to obtain the mixture of pure rhamnose and mixture of L-arabinose and galactose, and separating by the second column to obtain pure L-arabinose. The cellulose, alumina, starch, silica gel and developing solvent are filled in columns. Its advantages are low cost and high yield and purity of product.
Description
Technical field
The invention relates to the method for process for extracting L-arabinose from acacia gum by two-column.Belonging to the gum arabic is raw material, produces the technology of L-arabinose.
Background technology
L-arabinose is used to prepare medicine anticancer, antiviral, the treatment cardiovascular disorder mainly as medicine intermediate; Can also be used for the preparation of bacteria culture medium and be used for synthetic perfume as biochemical reagents.
L-arabinose exists with the form of hemicellulose L-arabinan and L-arabinan-D-semi-lactosi usually, is present in autumn Caragana arborescens glue, cherry gum, pear tree glue, rye, wheat bran, beet pulp and the Larch usually, in the maize peel etc.By these natural matters of hydrolysis and carry out aftertreatment and obtain L-arabinose.Prior preparation method is as follows:
With Arabic PYCNANTHA glue is raw material, with the H of 0.01N
2SO
4After the hydrolysis, transfer to neutrality with negatively charged ion IR-4B (OH) resin, with the reactant alcohol extraction, extraction liquid carries out column chromatography through the ethyl acetate semi-saturation aqueous solution to be separated.Can obtain L-arabinose and derivative thereof after the separation, and a spot of D-semi-lactosi, L-rhamnosyl and unknown material (EP 1987,0115068).
With Arabic SUNDRA glue is the raw material hydrolysis, is medium with the semi-saturation aqueous solution of butanols, carries out chromatographic separation, obtains the D-semi-lactosi, L-arabinose, and the L-rhamnosyl, ratio is 3: 2: 1.(S.Mukher?jee?and?A.N.S.Shrivastava,J.Sci.Ind.Research?India,1956,168,566-7)
After being the raw material hydrolysis with ANOGEISSNS SCHIMPERI glue, use alcohol extraction, after column chromatography separate can obtain L-arabinose and semi-lactosi (R.A.Paris and Marc Durand.Ann.Harm.franc.1965,14,755-61).
With asafoetide glycan glue is that raw material is hydrolyzed, and can obtain L-arabinose, the sugar of L-rhamnosyl and multiple trace, as: (Isaac Cole, Nature 1964,202 (4937), 1109-10) for D-glucose aldehydic acid, D-semi-lactosi.
After being the raw material hydrolysis with the plant aloe, be that developping agent separates with propyl carbinol-acetate by paper chromatography, can obtain pectinose (J.K.N.Jones and G.H.S.Thomas.Can.J.Chem.Soc 1962,39,192-202).
With Arabic catechu is raw material with 10% H
2SO
4Aqueous hydrolysis can obtain L-arabinose, D-semi-lactosi, L-rhamnosyl and aldobiouronic acid (G.O.Aspinall and T, B.Christensen.J.Chem.Soc.1961,3461).
With black Australia (tree) glue is that raw material carries out acidic hydrolysis, can obtain mixing sugar, wherein contain L-arabinose, D-semi-lactosi, L-rhamnosyl and D-glucose aldehydic acid, its mol ratio is: 1: 5: 1: 1 (Karl Freudenberg, Hans Molter, and Gustav Dietrich.Chem.Ber.1947,80,53-5).
Be that the tamarack that raw material will contain a small amount of biglycan places cold water with the glycan, extract with solution and can obtain Arabic latex sugar.With this syrup separate the pectinose that can obtain 1: 6 and semi-lactosi and a spot of wood sugar and rhamnosyl (S.Rose and A.S.Dutta, J.Indian.J.Chem.Soc.963,40,257-62)
With the beech wood is that raw material is hydrolyzed under acidic conditions, can obtain pectinose, its quality accounts for 0.7% of beech wood, the primary product of its hydrolysis but is a wood sugar, the quality of pectinose is 1.4% (G.O.Asinall, B.L.Hirst, and A.Nicolson of wood sugar quality, J.Chem.Soc.1959,1697-1706; C.A.49,12310b).
With the hemicellulose is raw material, by with the polysulfide reaction decomposes.The product of its decomposition mainly is a wood sugar, and be mixed with a spot of semi-lactosi and pectinose (E.L.Hirst and A.S., Perlin, J.Chem.Soc.1954,2622-7).
With Kalarba PROCERA (tree) glue is that raw material is through hydrolysis, chromatographic separation, can obtain D-glucuronic acid, D-semi-lactosi, L-rhamnosyl and unsettled L-arabinose (S.Mukher jee and A.N.Shrivastava, J.Chem.Soc.1958,80,2536-8).
The hydrolysis head product that above-mentioned most methods produced all contains multiple sugar, and this class mixture requires high to refining purification techniques, therefore be unfavorable for separating purifying, generally be that the high performance thin layer chromatography plate made with Zeo-karb, diatomite blended ion exchange resin, anionite-exchange resin, storng-acid cation exchange resin, zeolite molecular sieve, with the silica gel of the impregnated aminocarbonyl propyl bonding of SODIUM PHOSPHATE, MONOBASIC etc. separates and purifies, but difficulty is very big.Because complicated operation such as high temperature separation etc. or produce little effect, it is all very low to extract the productive rate and the output that obtain L-arabinose, all can't be applied to suitability for industrialized production.
Summary of the invention
The objective of the invention is about a kind of method of process for extracting L-arabinose from acacia gum by two-column is provided.This method has that technology is simple, production cost is low, product yield and the high characteristics of purity, is applicable to suitability for industrialized production.
In order to achieve the above object, the present invention is realized by following technical proposals.Adopt gum arabic, at first with comprising that the vitriolic mineral acid is hydrolyzed, acid concentration is 5~10%, hydrolysis temperature is 30~100 ℃, and then be neutralized to neutrality with the alkali that comprises hydrated barta, the reaction solution that obtains is after concentrating, use methyl alcohol, alcohol extraction, remove by filter insolubles, the resistates that the alcoholic solution evaporation concentration obtains is removed insolubles after adding the acid heat dissolving, cooling obtains the mixture of thick L-arabinose, this mixture separates the mixture that obtains pure rhamnosyl and L-arabinose and semi-lactosi through first chromatographic column, the mixture of L-arabinose and semi-lactosi separates through second chromatographic column and obtains purity and reach 96~99.5% L-arabinose, it is characterized in that the resistates acetate heat of solution after the pure extraction liquid evaporation concentration, solvent temperature is 60~90 ℃, and the acetate volumetric usage is 1~4 times of gum arabic weight.Two chromatographic column inner stuffings are Mierocrystalline cellulose, aluminum oxide, starch, silica gel, and the used developping agent of first chromatographic column is: propyl carbinol: ethyl acetate: Virahol: acetate: water=35: 100: 60: 35: 30; The used developping agent of second chromatographic column is: ethyl acetate: Virahol: water=65: 22: 11.
The invention has the advantages that technology is simple, production cost is low, the purity height of product.
Embodiment
Example 1
Get gum arabic 50g, put it in the four-hole bottle of the 1000ml that weighs in advance, add 1% hydrochloric acid 500ml, heating, temperature control is at 55 ℃, about stirring and refluxing 3h.When reaction finishes, take by weighing the Ca (OH) of the equivalent that is about as much as acid
28H
2O adds and to be equivalent in the water of its weight twice, and more than the heat temperature raising to 70 ℃, under stirring condition, at leisure it is joined in the solution after the hydrolysis, and solution is neutralized to neutrality.Solution after the neutralization remains on about 60 ℃, carries out underpressure distillation, and in resistates, the methyl alcohol that adds 5 times of volumes stirs backflow 3h down as extraction agent.More than the solution left standstill 6h after backflow finishes, filter, filtrate is distilled.In resistates, add the acetate of about 200mL, be heated to 80 ℃ of dissolvings, filter out and remove insolubles, leave standstill and be cooled to room temperature, separate out precipitation and about 60 ℃, toast about 4h, promptly obtain thick product 12.1g.Calculate the productive rate 78.1% of thick product.The 12.1g raw sugar is isolated the mixture of the pure rhamnosyl of 2.4g and 9.6g L-arabinose and semi-lactosi through first chromatographic column.The first chromatographic column inner stuffing is a silica gel, and used developping agent is: propyl carbinol: ethyl acetate: Virahol: acetate: water=35: 100: 60: 35: 30.Separated to obtain 8.4 gL-pectinoses through second chromatographic column by the mixture of 9.6g L-arabinose and semi-lactosi, its purity is 96% and the 1.2g semi-lactosi.The second chromatographic column post inner stuffing is a silica gel, and used developping agent is: ethyl acetate: Virahol: water=65: 22: 11.Example 2
Get gum arabic 50g, put it in the four-hole bottle of the 1000ml that weighs in advance, add 2.5% hydrochloric acid 500ml, heating, temperature control is at 65 ℃, about stirring and refluxing 4h.When reaction finishes, take by weighing the Ca (OH) of the equivalent that is about as much as acid
28H
2O adds and to be equivalent in the water of its weight twice, and more than the heat temperature raising to 70 ℃, under stirring condition, at leisure it is joined in the solution after the hydrolysis, and solution is neutralized to neutrality.Solution after the neutralization remains on about 50 ℃, carries out underpressure distillation, and in resistates, 80% ethanol that adds 5 times of volumes stirs backflow 3h down as extraction agent.More than the solution left standstill 6h after backflow finishes, filter, filtrate is distilled.Add the acetate of about 50mL in resistates, heating for dissolving leaves standstill and is cooled to room temperature, filters out and removes insolubles, and toast about 4h about 60 ℃, promptly obtains thick product 13.2g.Calculate the productive rate 85.1% of thick product.The 13.2g raw sugar is separated the mixture that obtains the pure rhamnosyl of 1.74g and 9.0g L-arabinose and semi-lactosi through first chromatographic column.The first chromatographic column inner stuffing is a Mierocrystalline cellulose, and used developping agent is: propyl carbinol: ethyl acetate: Virahol: acetate: water=35: 100: 60: 35: 30.Separated to obtain the 9.0g L-arabinose through second chromatographic column by the mixture of 11.3g L-arabinose and semi-lactosi, purity is 99.5% and the 2.3g semi-lactosi.The second chromatographic column post inner stuffing is a Mierocrystalline cellulose, and used developping agent is: ethyl acetate: Virahol: water=65: 22: 11.
Claims (1)
1. the method for a process for extracting L-arabinose from acacia gum by two-column, this method adopts gum arabic, at first with comprising that the vitriolic mineral acid is hydrolyzed, acid concentration is 5~10%, hydrolysis temperature is 30~100 ℃, and then be neutralized to neutrality with the alkali that comprises hydrated barta, the reaction solution that obtains is after concentrating, use methyl alcohol, alcohol extraction, remove by filter insolubles, the resistates that extraction liquid obtains after concentrating is removed insolubles after adding the acid dissolving, the mixture that is precipitated as thick L-arabinose is separated out in cooling, this mixture separates the mixture that obtains pure rhamnosyl and L-arabinose and semi-lactosi through first chromatographic column, the mixture of L-arabinose and semi-lactosi separates through second chromatographic column and obtains purity and reach 96~99.5% L-arabinose, it is characterized in that: the used acid of the heat of solution of resistates is acetate, solvent temperature is 60~90 ℃, the acetate volumetric usage is 1~4 times of gum arabic weight: two chromatographic column inner stuffings are Mierocrystalline cellulose, aluminum oxide, starch, silica gel, the used developping agent of first chromatographic column is: propyl carbinol: ethyl acetate: Virahol: acetate: water=35: 100: 60: 35: 30; The used developping agent of second chromatographic column is: ethyl acetate: Virahol: water=65: 22: 11.
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2407573A (en) * | 2003-10-30 | 2005-05-04 | Danisco Sweeteners Oy | Production of arabinose |
WO2005042788A1 (en) | 2003-10-30 | 2005-05-12 | Danisco Sweeteners Oy | Separation process |
CN101279247B (en) * | 2008-01-07 | 2011-07-06 | 西北大学 | Use of starch in preparation of chromatographic separating medium |
CN101475607B (en) * | 2009-01-15 | 2013-02-27 | 浙江诚意药业有限公司 | Method for separating and extracting monosaccharide from gum |
WO2023130594A1 (en) | 2022-01-06 | 2023-07-13 | 唐传生物科技(厦门)有限公司 | Arabinose as well as preparation and use thereof |
-
2002
- 2002-03-28 CN CNB021163537A patent/CN1164602C/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2407573A (en) * | 2003-10-30 | 2005-05-04 | Danisco Sweeteners Oy | Production of arabinose |
WO2005042788A1 (en) | 2003-10-30 | 2005-05-12 | Danisco Sweeteners Oy | Separation process |
CN101279247B (en) * | 2008-01-07 | 2011-07-06 | 西北大学 | Use of starch in preparation of chromatographic separating medium |
CN101475607B (en) * | 2009-01-15 | 2013-02-27 | 浙江诚意药业有限公司 | Method for separating and extracting monosaccharide from gum |
WO2023130594A1 (en) | 2022-01-06 | 2023-07-13 | 唐传生物科技(厦门)有限公司 | Arabinose as well as preparation and use thereof |
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