CN1047805A - A kind of polysaccharide-k extracting new process - Google Patents

A kind of polysaccharide-k extracting new process Download PDF

Info

Publication number
CN1047805A
CN1047805A CN 90102310 CN90102310A CN1047805A CN 1047805 A CN1047805 A CN 1047805A CN 90102310 CN90102310 CN 90102310 CN 90102310 A CN90102310 A CN 90102310A CN 1047805 A CN1047805 A CN 1047805A
Authority
CN
China
Prior art keywords
krestin
leachate
adds
sporophore
precipitate
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.)
Pending
Application number
CN 90102310
Other languages
Chinese (zh)
Inventor
郑经康
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.)
CHANGCHUN PHARMACEUTICAL FACTORY
Original Assignee
CHANGCHUN PHARMACEUTICAL FACTORY
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 CHANGCHUN PHARMACEUTICAL FACTORY filed Critical CHANGCHUN PHARMACEUTICAL FACTORY
Priority to CN 90102310 priority Critical patent/CN1047805A/en
Publication of CN1047805A publication Critical patent/CN1047805A/en
Pending legal-status Critical Current

Links

Landscapes

  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

A kind of polysaccharide-k extracting new process belongs to the pharmaceutical technology technical field, and this technology is: manyzoned polypore sporophore is added water boil, adding calcium hydroxide in this leachate makes krestin form complex and precipitates and separate out, in complex, add acid then, make the precipitate dissolving, in lysate, add ethanol, the krestin precipitation is separated out, filter,, promptly get Powdered krestin with washing with alcohol, drying, adopt this technological advantage to be: leachate does not need to concentrate, thereby can reduce a large amount of energy consumptions; Can obtain more stable krestin complex as intermediate, be convenient to store.

Description

A kind of polysaccharide-k extracting new process
The invention belongs to the pharmaceutical technology technical field.
The technology of existing extraction krestin is that manyzoned polypore sporophore is added water boil a few hours, leachate is filtered the back concentrate, and adds an amount of ethanol then, and the krestin precipitation is separated out, and the washing with alcohol after drying use in centrifugalize, gets the former powder of krestin.Because the leachate volume is very big, need to consume a large amount of energy in concentration process when adopting this technology, the operating time is also longer; The former powder of krestin can not long term store.
The present invention has provided the new technology that a kind of krestin extracts, and its objective is and has reduced energy resource consumption.Simultaneously owing to can obtain the krestin complex in producing the former powder craft process of krestin, this complex is comparatively stable, is convenient to store, thereby makes the problem that the former powder of krestin can not long term store obtain solution.
The present invention is achieved in that
1. the manyzoned polypore sporophore water is rinsed well, added certain water gaging then, heated and boiled 5 hours, the leaching leachate adds water boil 5 hours again in the sporophore, so repeat 1~2 time.
2. leachate is merged, add hydrogen calcium hydride or calcium oxide, consumption is 3~30% of a manyzoned polypore sporophore, makes krestin form complex and precipitates and separate out.In addition, the mixture of also available calcium chloride of calcium hydroxide and sodium hydroxide replaces, and the calcium chloride consumption is 4.5~45% of a manyzoned polypore sporophore.
3. leaching precipitate adds hydrochloric acid, consumption with in and calcium hydroxide be as the criterion, make the precipitate dissolving.
4. in above-mentioned solution, add 1~3 times of amount ethanol, the krestin precipitation is separated out.
5. leaching krestin precipitation with washing with alcohol, drying, promptly gets Powdered krestin.
Adopt this technological advantage to be:
1. leachate does not need to concentrate, thereby can reduce a large amount of energy consumptions.
2. can obtain more stable krestin complex as intermediate, be convenient to store.
Embodiment 1.
With 400 gram manyzoned polypore sporophores, the washing back adds suitable quantity of water (the sporophore submergence is got final product), heated and boiled 5 hours, and the leaching leachate adds water boil 5 hours again in the sporophore; Twice leachate merged, add calcium hydroxide 15 grams, make krestin form complex and precipitate and separate out; The leaching precipitate adds 62 milliliters of 6 equivalent hydrochloric acid, makes the precipitate dissolving; Add 2 times of volume ethanol in the gained solution, make the krestin precipitation separate out 1 and filter; Reuse washing with alcohol after drying promptly gets krestin.
Embodiment 2.
As described in the embodiment 1., add water boil with 200 gram manyzoned polypore sporophores, add calcium chloride 11.3 grams and 81 milliliters of mixture that are mixed with of 10% sodium hydroxide in the leachate, the leaching precipitate, add 6 equivalent hydrochloric acid and make resolution of precipitate for 31 milliliters, all the other technical processs are identical with embodiment 1, promptly get krestin.

Claims (1)

1, a kind of polysaccharide-k extracting new process, its technology is:
A rinses the manyzoned polypore sporophore water well.Add certain water gaging then, heated and boiled 5 hours, the leaching leachate adds water boil 5 hours again in the sporophore, so repeat 1~2 time;
B merges leachate, adds calcium hydroxide or calcium oxide, and consumption is a manyzoned polypore sporophore 3~30%, make krestin form complex and precipitate and separate out, in addition, the mixture of also available calcium chloride of calcium hydroxide and sodium hydroxide replaces, and the calcium chloride consumption is 4.5~45% of a manyzoned polypore sporophore;
C leaching precipitate adds hydrochloric acid, consumption with in and sodium hydroxide be as the criterion, make the precipitate dissolving;
D adds 1~3 times of amount ethanol in above-mentioned solution, the krestin precipitation is separated out;
E leaching krestin precipitation with washing with alcohol, drying, promptly gets Powdered krestin.
CN 90102310 1990-04-20 1990-04-20 A kind of polysaccharide-k extracting new process Pending CN1047805A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 90102310 CN1047805A (en) 1990-04-20 1990-04-20 A kind of polysaccharide-k extracting new process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 90102310 CN1047805A (en) 1990-04-20 1990-04-20 A kind of polysaccharide-k extracting new process

Publications (1)

Publication Number Publication Date
CN1047805A true CN1047805A (en) 1990-12-19

Family

ID=4877458

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 90102310 Pending CN1047805A (en) 1990-04-20 1990-04-20 A kind of polysaccharide-k extracting new process

Country Status (1)

Country Link
CN (1) CN1047805A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101181052B (en) * 2007-12-14 2010-12-01 广东省微生物研究所 Method for preparing coriolan
CN101249259B (en) * 2008-03-04 2011-07-27 上海师范大学 High content and high activity oral polysaccharide-peptide and preparing method and application of the same
CN102964459A (en) * 2012-11-02 2013-03-13 华南理工大学 Lentinan calcium complex, and preparation method and application thereof
CN103070172A (en) * 2012-12-27 2013-05-01 陕西恒田化工有限公司 Trametes versicolor glucan water agent and preparation method thereof
CN104231104A (en) * 2014-09-19 2014-12-24 中山安荞生物科技有限公司 Extraction method of polysaccharides in coriolus versicolor
CN104387486A (en) * 2014-11-11 2015-03-04 罗宇 High-yield preparation method of coriolus versicolor polysaccharide

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101181052B (en) * 2007-12-14 2010-12-01 广东省微生物研究所 Method for preparing coriolan
CN101249259B (en) * 2008-03-04 2011-07-27 上海师范大学 High content and high activity oral polysaccharide-peptide and preparing method and application of the same
CN102964459A (en) * 2012-11-02 2013-03-13 华南理工大学 Lentinan calcium complex, and preparation method and application thereof
CN103070172A (en) * 2012-12-27 2013-05-01 陕西恒田化工有限公司 Trametes versicolor glucan water agent and preparation method thereof
CN104231104A (en) * 2014-09-19 2014-12-24 中山安荞生物科技有限公司 Extraction method of polysaccharides in coriolus versicolor
CN104387486A (en) * 2014-11-11 2015-03-04 罗宇 High-yield preparation method of coriolus versicolor polysaccharide

Similar Documents

Publication Publication Date Title
CN101830948B (en) Method for preparing tea saponin by using tea seed degreased dreg
CN101864002B (en) Method for extracting sodium heparin
CN103408473B (en) A kind of method extracting natural taurine from scallop splanchna
CN1047805A (en) A kind of polysaccharide-k extracting new process
CN102432479B (en) Method for extracting L-valine from L-valine fermentation liquid
CN102875697A (en) Process for efficiently extracting liquaemin by utilizing porcine small intestines
CN115676877A (en) Silica gel modified metatitanic acid type lithium ion sieve precursor and preparation method thereof
CN109534472A (en) A kind of recycling and reuse method of polishing powder from rare earth waste material
CN103483403A (en) Circulating extraction method for extracting and purifying hesperidin from orange residues
CN103193861A (en) Method for extracting protein from waste liquid generated from production of sodium heparin
CN103520256B (en) A kind of preparation method of high-purity gynostemma pentaphylla total saponin for veterinary drug
CN108042470A (en) Sea cucumber extract nourishes facial mask and its preparation method
CN109097606B (en) Separation process for co-producing pure dysprosium and pure thulium by fractional extraction
CN102080133B (en) Method for saving water and reducing acid/alkali specific consumption in xylose production
CN110064378A (en) A kind of high absorption property chitosan magnetic carbon ball and its preparation method and application
CN1054788A (en) One step leaching grouts extract grease and tea saponin technology
CN102772452A (en) Method for producing ultra-low-acid ginkgo leaf extract
CN110078843A (en) The preparation method and application of carboxymethyl panax japonicus polysaccharides
CN101875685A (en) Lysimachia foenum-graecum hance saponin extract having more than or equal to 30 percent of saponin and extraction process thereof
CN110521861A (en) A kind of Radix Glycyrrhizae Thick many candies extract preparation and application as feed addictive
CN216363556U (en) Oyster juice concentration and extraction system
CN1067404C (en) Method for extraction water soluble polyose of spirulina
CN108950252A (en) A kind of separation method of fractional extraction coproducing pure samarium and pure terbium
CN1071672A (en) Produce the method for natural pigment with the tea cake
CN216737954U (en) Ternary precursor wastewater treatment and recycling system

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication