CN1635133A - Gellan gum post-extraction method - Google Patents
Gellan gum post-extraction method Download PDFInfo
- Publication number
- CN1635133A CN1635133A CN 200410064547 CN200410064547A CN1635133A CN 1635133 A CN1635133 A CN 1635133A CN 200410064547 CN200410064547 CN 200410064547 CN 200410064547 A CN200410064547 A CN 200410064547A CN 1635133 A CN1635133 A CN 1635133A
- Authority
- CN
- China
- Prior art keywords
- gelling gum
- gelling
- post extraction
- liquid
- add
- 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.)
- Granted
Links
- 238000000605 extraction Methods 0.000 title claims abstract description 20
- 229920002148 Gellan gum Polymers 0.000 title abstract description 5
- 235000010492 gellan gum Nutrition 0.000 title abstract description 5
- 239000000216 gellan gum Substances 0.000 title abstract description 5
- 239000007788 liquid Substances 0.000 claims abstract description 39
- 238000000034 method Methods 0.000 claims abstract description 25
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 claims abstract description 18
- 125000002252 acyl group Chemical group 0.000 claims abstract description 15
- 239000003960 organic solvent Substances 0.000 claims abstract description 15
- 238000000855 fermentation Methods 0.000 claims abstract description 13
- 230000004151 fermentation Effects 0.000 claims abstract description 13
- 238000000926 separation method Methods 0.000 claims abstract description 10
- 238000001914 filtration Methods 0.000 claims abstract description 6
- 238000001035 drying Methods 0.000 claims abstract description 5
- 238000005189 flocculation Methods 0.000 claims description 18
- 230000016615 flocculation Effects 0.000 claims description 18
- 239000003795 chemical substances by application Substances 0.000 claims description 14
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 12
- 239000012065 filter cake Substances 0.000 claims description 10
- 230000003311 flocculating effect Effects 0.000 claims description 10
- 239000002594 sorbent Substances 0.000 claims description 10
- 238000010792 warming Methods 0.000 claims description 10
- 239000000047 product Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 102000035101 Aspartic proteases Human genes 0.000 claims description 5
- 108091005502 Aspartic proteases Proteins 0.000 claims description 5
- FOCAUTSVDIKZOP-UHFFFAOYSA-N chloroacetic acid Chemical compound OC(=O)CCl FOCAUTSVDIKZOP-UHFFFAOYSA-N 0.000 claims description 5
- 239000000701 coagulant Substances 0.000 claims description 5
- 230000018044 dehydration Effects 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 239000012634 fragment Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 230000003647 oxidation Effects 0.000 claims description 5
- 238000007254 oxidation reaction Methods 0.000 claims description 5
- 239000000049 pigment Substances 0.000 claims description 5
- 210000001082 somatic cell Anatomy 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 5
- 238000001291 vacuum drying Methods 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 229910001562 pearlite Inorganic materials 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims description 3
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 2
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 2
- 229910052728 basic metal Inorganic materials 0.000 claims description 2
- 150000003818 basic metals Chemical class 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 13
- 238000005516 engineering process Methods 0.000 abstract description 6
- 230000020176 deacylation Effects 0.000 abstract 2
- 238000005947 deacylation reaction Methods 0.000 abstract 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 abstract 1
- 229910052783 alkali metal Inorganic materials 0.000 abstract 1
- 150000001340 alkali metals Chemical class 0.000 abstract 1
- 230000006378 damage Effects 0.000 abstract 1
- 238000010298 pulverizing process Methods 0.000 abstract 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 239000007844 bleaching agent Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 2
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- 241001113556 Elodea Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 241000790234 Sphingomonas elodea Species 0.000 description 1
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000013256 coordination polymer Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
The invention relates to a posterior extraction method of Gellan gum belonging to the microbe fermentation production field. The method comprises steps of pretreatment of the fermentation liquor, deacylation, filtration, extraction of the flocculate, solid-liquid separation, drying and pulverization. The invention overcomes the shortcomings of high manufacturing cost, single variety existing in known technology. By the deacylation treatment with different added hypochlorite, Gellan gum with different acyl content can be obtained without destruction of the Gellan gum molecular structure to meet different need. The flocculant employs alkali metal or alkaline earth chloride to substitute for partial organic solvent to improve the production safe reliability.
Description
Technical field
The present invention relates to the microbial fermentation production field, be meant a kind of method for post extraction of gelling gum especially.
Background technology
Gelling gum is to utilize modern biotechnology to carry out aerobic fermentation by the bacterial classification that monospore bacillus waterweed belongs in (pseudomonas elodea), and a kind of transparent gelifying agent through special refinement technique is produced has good thermostability.Consumption is few, and it is good, acidproof, alkaline-resisting to hold flavor property, anti-biological enzyme, and gel-strength can adjust as required, is widely used in industries such as food, medicine, fine chemistry industry.Have only U.S. CP keclo company to realize industrial production at present in the world, production and sales are in monopoly position, and production technology difficulty own is big, so cost an arm and a leg.More domestic universities and colleges also once attempted to produce gelling gum with comparatively easy production technology, but effect is not ideal always.The patent No. is the production technique that discloses a kind of new microbiological polysaccharide Gellan gum in 00125858.3 the patent, but above-mentioned prior art exists with membrane technique in the leaching process of back and extracts gelling gum, price height because of film, and can not regenerate, so manufacturing cost is high, prepared product is a single variety, and shortcoming such as can not meet the different needs.
Summary of the invention
The method for post extraction that the object of the present invention is to provide a kind of low-cost gelling gum that can produce high, medium and low acyl group content as required is to overcome the deficiency that prior art exists.
Overall technology design of the present invention is:
The method for post extraction of gelling gum comprises fermentation liquor pretreatment, the processing of deacylated tRNA base, Gel Treatment, solid-liquid separation; It is characterized in that the processing condition in each step are:
A, fermentation liquor pretreatment: transfer pH value to the 4-5 scope fermented liquid, add the aspartic protease of 10-15ppm and account for fermentating liquid volume 10%-12% (V/V), concentration is 10% (NH
4)
2SO
4(W/V) solution is warming up to 55-60 ℃ with it, keeps 18-24h, adds 1% Mono Chloro Acetic Acid (W/V) and keeps 1-2h;
B, deacylated tRNA base handle: with pretreated fermented liquid and the volume mixture of water by 1: 1, stir, be warming up to 90-95 ℃, add the hypochlorite solutions oxidation acyl group that mixes back volume 0-0.5% (v/v), reacted 15-20 minute, get gelling gum liquid;
C, flocculation are extracted: the gelling gum solution of making in the B step is cooled to 40-45 ℃, adds flocculation agent, gelling gum forms gel;
Concrete technical conceive of the present invention and processing condition are:
Hypochlorite in the B step is selected clorox or Losantin for use.
The flocculating aids (W/V) that adds 1% sorbent material (W/V) and 1.5% in the reaction solution after the deacylated tRNA base is handled in the B step; filter and remove somatic cells fragment and pigment; obtain clarifying gelling gum liquid, sorbent material is selected gac for use, and flocculating aids is selected diatomite or expanded pearlite salt for use.
In the C step gelling gum solution is cooled to 40-45 ℃, adds the flocculation agent of 0.8-1%; Gelling gum forms gel, and then adds the organic solvent of 10-15%, and the gelling gum dehydration is separated out.
Flocculation agent is selected ionogen for use in the C step, and organic solvent is selected alcohol organic solvent for use.
Ionogen is AlCl
3, MgCl
2, CaCl
2, Virahol or the ethanol of alcohol organic solvent more than 90%.
Adopt Plate Filtration gelling gum coagulant liquid in the D step, get the gelling gum filter cake; Filter cake is in 80-85 ℃ of vacuum-drying, control vacuum tightness-0.08Mpa, time 2h, pulverize the gelling gum powder-product.
Substantive distinguishing features that the present invention is obtained and remarkable technical progress are:
Integrated artistic of the present invention is reasonable in design; working method is simple; easily go; adopt the hypochlorite of different dosages to carry out the processing of deacylated tRNA base as required; under the prerequisite of not destroying the gelling gum molecular structure; can obtain possessing the height of variant production characteristic respectively; in; the gelling gum of low acyl group content; different demands have been satisfied; realized the seriation industry production of gelling gum; and avoided simultaneously adopting membrane technique to extract the too high problem of manufacturing cost that gelling gum causes; flocculation agent in technology selects for use the muriate of basic metal or alkaline-earth metal to substitute the part organic floculant; also reduced production cost, improved industrial safe reliability from different degree.
Embodiment
Below embodiments of the invention are described further:
Embodiment 1
The method for post extraction of gelling gum comprises fermentation liquor pretreatment, the processing of deacylated tRNA base, Gel Treatment, solid-liquid separation; Processing condition in each processing step are:
A, fermentation liquor pretreatment: fermented liquid is transferred pH value to 4.5, add the aspartic protease of 11ppm and account for fermentating liquid volume 11%, concentration is 10% (NH
4)
2SO
4(W/V) solution is warming up to 58 ℃ with it, keeps 20h, adds 1% Mono Chloro Acetic Acid (W/V) again and keeps 1.5h;
B, deacylated tRNA base handle: with pretreated fermented liquid and the volume mixture of water by 1: 1, stir, be warming up to 93 ℃, add the chlorine bleach liquor's oxidation acyl group that mixes back volume 0-0.05% (v/v), reacted 15-20 minute, get gelling gum liquid;
Add the flocculating aids (W/V) of 1% sorbent material (W/V) and 1.5% with the mixed fermented liquid of water, filter and remove somatic cells fragment and pigment, obtain clarifying gelling gum liquid, sorbent material is selected gac for use, and flocculating aids is selected diatomite for use.
C, flocculation are extracted: gelling gum solution is cooled to 42 ℃, adds 0.8% flocculation agent; Gelling gum forms gel, and then adds 12% organic solvent, and the gelling gum dehydration is separated out.Flocculation agent is selected AlCl for use
3, organic solvent is selected the Virahol more than 92% for use.
D, solid-liquid separation, drying and crushing: adopt Plate Filtration gelling gum coagulant liquid, get the gelling gum filter cake; Filter cake is in 82 ℃ of vacuum-dryings, control vacuum tightness-0.08Mpa, time 2h, pulverize the gelling gum powder-product of high acyl group content.The gelling gum powder of high acyl group content has gels-soft, resilient characteristic.If do not add clorox in deacylated tRNA base treating processes, what then generate is natural gelling gum.
Embodiment 2
The method for post extraction of gelling gum comprises fermentation liquor pretreatment, the processing of deacylated tRNA base, Gel Treatment, solid-liquid separation; Processing condition in each processing step are:
A, fermentation liquor pretreatment: fermented liquid is transferred pH value to 4.8, add the aspartic protease of 13ppm and account for fermentating liquid volume 12%, concentration is 10% (NH
4)
2SO
4(W/V) solution is warming up to 60 ℃ with it, keeps 19h, adds 1% Mono Chloro Acetic Acid (W/V) again and keeps 2h;
B, deacylated tRNA base handle: the volume mixture of pretreated fermented liquid and water being pressed 1: 1; stir; be warming up to 92 ℃; add the chlorine bleach liquor's oxidation acyl group that mixes back volume 0.3% (v/v), reacted 20 minutes, add the flocculating aids (W/V) of 1% sorbent material (W/V) and 1.5% in the reaction solution after the deacylated tRNA base is handled; filter and remove somatic cells fragment and pigment; obtain clarifying gelling gum liquid, sorbent material is selected gac for use, and flocculating aids is selected expanded pearlite salt for use.
C, flocculation are extracted: gelling gum solution is cooled to 43 ℃, adds 0.9% flocculation agent; Gelling gum forms gel, and then adds 14% organic solvent, and the gelling gum dehydration is separated out.Flocculation agent is selected AlCl for use
3, organic solvent is selected the ethanol more than 92% for use.
D, solid-liquid separation, drying and crushing: adopt Plate Filtration gelling gum coagulant liquid, get the gelling gum filter cake; Filter cake is in 82 ℃ of vacuum-dryings, control vacuum tightness-0.08Mpa, time 2h, pulverize the gelling gum powder-product of low acyl group content.It is big that the gelling gum of low acyl group content possesses intensity, easily the characteristic of embrittlement.
Embodiment 3
The method for post extraction of gelling gum comprises fermentation liquor pretreatment, the processing of deacylated tRNA base, Gel Treatment, solid-liquid separation; Processing condition in each processing step are:
A, fermentation liquor pretreatment: fermented liquid is transferred pH value to 4.2, add the aspartic protease of 14ppm and account for fermentating liquid volume 10%, concentration is 10% (NH
4)
2SO
4(W/V) solution is warming up to 56 ℃ with it, keeps 23h, adds 1% Mono Chloro Acetic Acid (W/V) again and keeps 2h;
B, deacylated tRNA base handle: the volume mixture of pretreated fermented liquid and water being pressed 1: 1; stir; be warming up to 94 ℃; add the chlorine bleach liquor's oxidation acyl group that mixes back volume 0.5% (v/v), reacted 18 minutes, add the flocculating aids (W/V) of 1% sorbent material (W/V) and 1.5% in the reaction solution after the deacylated tRNA base is handled; filter and remove somatic cells fragment and pigment; obtain clarifying gelling gum liquid, sorbent material is selected gac for use, and flocculating aids is selected expanded pearlite salt for use.
C, flocculation are extracted: gelling gum solution is cooled to 44 ℃, adds 1% flocculation agent; Gelling gum forms gel, and then adds 15% organic solvent, and the gelling gum dehydration is separated out.Flocculation agent is selected CaCl for use
2, organic solvent is selected 92% ethanol for use.
D, solid-liquid separation, drying and crushing: adopt Plate Filtration gelling gum coagulant liquid, get the gelling gum filter cake; Filter cake is in 82 ℃ of vacuum-dryings, control vacuum tightness-0.08Mpa, time 2h, pulverize in the gelling gum powder-product of acyl group content.The characteristic of the gelling gum of middle acyl group content is between the gelling gum of high and low acyl group content.
Claims (10)
1, the method for post extraction of gelling gum comprises fermentation liquor pretreatment, the processing of deacylated tRNA base, Gel Treatment, solid-liquid separation; It is characterized in that the processing condition in each step are:
A, fermentation liquor pretreatment: transfer pH value to the 4-5 scope fermented liquid, add the aspartic protease of 10-15ppm and account for fermentating liquid volume 10%-12% (V/V), concentration is 10% (NH
4)
2SO
4(W/V) solution is warming up to 55-60 ℃ with it, keeps 18-24h, adds 1% Mono Chloro Acetic Acid (W/V) and keeps 1-2h;
B, deacylated tRNA base handle: with pretreated fermented liquid and the volume mixture of water by 1: 1, stir, be warming up to 90-95 ℃, add the hypochlorite solutions oxidation acyl group that mixes back volume 0-0.5% (v/v), reacted 15-20 minute, get gelling gum liquid;
C, flocculation are extracted: the gelling gum solution of making in the B step is cooled to 40-45 ℃, adds flocculation agent, gelling gum forms gel;
D, solid-liquid separation, drying and crushing.
2, the method for post extraction of gelling gum according to claim 1 is characterized in that the hypochlorite in the described B step is selected clorox or Losantin for use.
3, the method for post extraction of gelling gum according to claim 1; it is characterized in that adding in the reaction solution after the deacylated tRNA base is handled in the B step flocculating aids (W/V) of 1% sorbent material (W/V) and 1.5%; filter and remove somatic cells fragment and pigment; obtain clarifying gelling gum liquid; sorbent material is selected gac for use, and flocculating aids is selected diatomite or expanded pearlite salt for use.
4, the method for post extraction of gelling gum according to claim 1 and 2 is characterized in that the hypochlorite add-on in the described B step is 0-0.1% (v/v).
5, the method for post extraction of gelling gum according to claim 1 and 2 is characterized in that the hypochlorite add-on in the described B step is 0.1-0.4% (v/v).
6, the method for post extraction of gelling gum according to claim 1 and 2 is characterized in that the hypochlorite add-on in the described B step is 0.4-0.5% (v/v).
7, the method for post extraction of gelling gum according to claim 1 is characterized in that in the C step gelling gum solution being cooled to 40-45 ℃, adds the flocculation agent of 0.8-1%; Gelling gum forms gel, and then adds the organic solvent of 10-15%, and the gelling gum dehydration is separated out.
8, according to the method for post extraction of claim 1 or 7 described gelling gums, it is characterized in that flocculation agent in the C step selects the muriate of basic metal or alkaline-earth metal for use, organic solvent is selected alcohol organic solvent for use.
9, the method for post extraction of gelling gum according to claim 8 is characterized in that ionogen is AlCl
3, MgCl
2, CaCl
2, Virahol or the ethanol of alcohol organic solvent more than 90%.
10, the method for post extraction of gelling gum according to claim 1 is characterized in that adopting Plate Filtration gelling gum coagulant liquid in the D step, gets the gelling gum filter cake; Filter cake is in 80-85 ℃ of vacuum-drying, control vacuum tightness-0.08Mpa, time 2h, pulverize the gelling gum powder-product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410064547 CN1259426C (en) | 2004-11-19 | 2004-11-19 | Gellan gum post-extraction method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410064547 CN1259426C (en) | 2004-11-19 | 2004-11-19 | Gellan gum post-extraction method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1635133A true CN1635133A (en) | 2005-07-06 |
| CN1259426C CN1259426C (en) | 2006-06-14 |
Family
ID=34846396
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200410064547 Expired - Fee Related CN1259426C (en) | 2004-11-19 | 2004-11-19 | Gellan gum post-extraction method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1259426C (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101191138B (en) * | 2006-11-28 | 2010-10-27 | 浙江帝斯曼中肯生物科技有限公司 | Method for producing gellan gum finished product from gellan gum fermentation liquor |
| WO2011003269A1 (en) * | 2009-07-09 | 2011-01-13 | 浙江帝斯曼中肯生物科技有限公司 | Method for post-extracting low acyl gellan gum |
| CN101560261B (en) * | 2009-05-11 | 2011-04-13 | 江南大学 | Cleaner production method of gellan gum |
| EP2348054A1 (en) * | 2009-07-09 | 2011-07-27 | Zhejiang Dsm Zhongken Biotechnology Co., Ltd | Method for post-extracting low acyl gellan gum with high solubility |
| CN101724090B (en) * | 2009-12-01 | 2011-10-26 | 淄博中轩生化有限公司 | Method for refining Gellan gum |
| CN1932026B (en) * | 2006-09-12 | 2011-10-26 | 山东大学 | Deproteinizing process of gullan gum fermenting liquid |
| CN101824095B (en) * | 2009-05-31 | 2012-10-10 | 上海众伟生化有限公司 | Transparent high acyl gellan gum and production method thereof |
| CN103113488A (en) * | 2013-02-22 | 2013-05-22 | 天茁（上海）生物科技有限公司 | Method for extracting low-acyl transparent gellan gum easy to disperse and dissolve |
| CN116135886A (en) * | 2023-04-18 | 2023-05-19 | 广州市乾相生物科技有限公司 | Extraction method of transparent low-acyl gellan gum |
-
2004
- 2004-11-19 CN CN 200410064547 patent/CN1259426C/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1932026B (en) * | 2006-09-12 | 2011-10-26 | 山东大学 | Deproteinizing process of gullan gum fermenting liquid |
| CN101191138B (en) * | 2006-11-28 | 2010-10-27 | 浙江帝斯曼中肯生物科技有限公司 | Method for producing gellan gum finished product from gellan gum fermentation liquor |
| CN101560261B (en) * | 2009-05-11 | 2011-04-13 | 江南大学 | Cleaner production method of gellan gum |
| CN101824095B (en) * | 2009-05-31 | 2012-10-10 | 上海众伟生化有限公司 | Transparent high acyl gellan gum and production method thereof |
| EP2348054A1 (en) * | 2009-07-09 | 2011-07-27 | Zhejiang Dsm Zhongken Biotechnology Co., Ltd | Method for post-extracting low acyl gellan gum with high solubility |
| CN101597341B (en) * | 2009-07-09 | 2011-10-26 | 浙江帝斯曼中肯生物科技有限公司 | Method for post extraction of low-acyl gellan gum with high solubility |
| WO2011003269A1 (en) * | 2009-07-09 | 2011-01-13 | 浙江帝斯曼中肯生物科技有限公司 | Method for post-extracting low acyl gellan gum |
| US8609377B2 (en) | 2009-07-09 | 2013-12-17 | Zhejiang Dsm Zhongken Biotechnology Co., Ltd. | Method for post-extracting low acyl gellan gum |
| EP2348054A4 (en) * | 2009-07-09 | 2014-06-25 | Zhejiang Dsm Zhongken Biotechnology Co Ltd | Method for post-extracting low acyl gellan gum with high solubility |
| CN101724090B (en) * | 2009-12-01 | 2011-10-26 | 淄博中轩生化有限公司 | Method for refining Gellan gum |
| CN103113488A (en) * | 2013-02-22 | 2013-05-22 | 天茁（上海）生物科技有限公司 | Method for extracting low-acyl transparent gellan gum easy to disperse and dissolve |
| CN103113488B (en) * | 2013-02-22 | 2015-12-23 | 天茁（上海）生物科技有限公司 | The extracting method of the low acyl transparent type gelling gum of a kind of easy dispersion and dissolving |
| CN116135886A (en) * | 2023-04-18 | 2023-05-19 | 广州市乾相生物科技有限公司 | Extraction method of transparent low-acyl gellan gum |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1259426C (en) | 2006-06-14 |
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