CN101450960B - Abomacetin extraction by salting-out method - Google Patents

Abomacetin extraction by salting-out method Download PDF

Info

Publication number
CN101450960B
CN101450960B CN200710195544A CN200710195544A CN101450960B CN 101450960 B CN101450960 B CN 101450960B CN 200710195544 A CN200710195544 A CN 200710195544A CN 200710195544 A CN200710195544 A CN 200710195544A CN 101450960 B CN101450960 B CN 101450960B
Authority
CN
China
Prior art keywords
oxacyclotetradecane
erythromycin deriv
sodium
filtrating
erythrocin
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.)
Active
Application number
CN200710195544A
Other languages
Chinese (zh)
Other versions
CN101450960A (en
Inventor
潘贞德
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.)
Zhongnonghuawei Pharmaceutical Co., Ltd
Original Assignee
潘贞德
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 潘贞德 filed Critical 潘贞德
Priority to CN200710195544A priority Critical patent/CN101450960B/en
Publication of CN101450960A publication Critical patent/CN101450960A/en
Application granted granted Critical
Publication of CN101450960B publication Critical patent/CN101450960B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention discloses a method for extracting erythrocin form a fermentation filtrate or from an aqueous solution containing erythrocin by a salting-out. The method is that an adequate amount of sodium chloride or sodium sulfate or other salts are added in to the fermentation filtrate to reduce the solubility of the erythrocin to precipitate the erythrocin from the water liquid, or during extraction of the erythrocin with a hydrophobic organic solvent, an adequate amount of sodium chloride or sodium sulfate or other salts are added at the same time to improve the partition ratio of the erythrocin in the organic phrase. The method extracts the erythrocin from the fermentation filtrate, saves solvent media and improves the yield of the erythrocin.

Description

Abomacetin extraction by salting-out
Technical field
A kind of microbiotic process for extracting is about from ferment filtrate, extracting Oxacyclotetradecane,erythromycin deriv with salting-out process or from the aqueous solution that contains Oxacyclotetradecane,erythromycin deriv, extracting Oxacyclotetradecane,erythromycin deriv concretely.
Background technology
Oxacyclotetradecane,erythromycin deriv is a kind of macrolide antibiotics, has been widely used in clinical.The production of Oxacyclotetradecane,erythromycin deriv is divided into two and goes on foot greatly, and the one, by streptomyces erythreus fermentation synthesis of erythromycin; The 2nd, from fermented liquid, Oxacyclotetradecane,erythromycin deriv is extract.
The process for extracting of Oxacyclotetradecane,erythromycin deriv has solvent extraction, three kinds of ion exchange method and macroreticular resin absorbing methods (Gu Juefen chief editor, microbiotic, Shanghai science tech publishing house, September calendar year 2001 the 1st edition, the 217th~218 page).
The present invention extracts Oxacyclotetradecane,erythromycin deriv with salting-out process from ferment filtrate; The invention main points are following: the sodium-chlor or sodium sulfate or other salts that in ferment filtrate, add capacity; Readjust the distribution ferment filtrating PH to 7.5~11.5 then and (also can transfer PH earlier; The back adds salt), Oxacyclotetradecane,erythromycin deriv is just separated out from ferment filtrate, and its eduction rate can reach more than 95%; Adopt filtration or centrifugation method to collect the Oxacyclotetradecane,erythromycin deriv of separating out then.Also can in the system of above-mentioned " 1 ", add an amount of (be equivalent to ferment filtrate volume 5~50%) hydrophobic solvent (as: alcohols of ETHYLE ACETATE, butylacetate, Isoamyl Acetate FCC, pentyl acetate, 4-methyl-2 pentanone, 4~8 carbon); Because the existence of salt; Thereby reduced the solubleness of Oxacyclotetradecane,erythromycin deriv in water, improved the partition ratio (partition rate) of Oxacyclotetradecane,erythromycin deriv in organic phase.For example: with the butylacetate/butanols or the octanol cosolvent that are equivalent to ferment filtrate volume 8%, under the situation that the salt that capacity is arranged exists, through single extraction, the percentage extraction of Oxacyclotetradecane,erythromycin deriv can reach more than 97%; If under no salt added situation, the solvent with 15% (butylacetate/butanols or octanol) extraction, the percentage extraction that extracts Oxacyclotetradecane,erythromycin deriv through twice just can reach about 95%.
This shows that the outstanding advantage of abomacetin extraction by salting-out is: can reduce the solvent usage quantity and reach 1/2~2/3.
Summary of the invention
The invention relates to the process for extracting of Oxacyclotetradecane,erythromycin deriv, definite saying is to adopt salting-out process to extract Oxacyclotetradecane,erythromycin deriv.This method feature is: the adding weight ratio is 3~85% inorganic acid salt or organic acid salt in abomacetin fermentation filtrating; Oxacyclotetradecane,erythromycin deriv is separated out from ferment filtrate; Perhaps when adopting hydrophobic organic solvent from ferment filtrate, to extract Oxacyclotetradecane,erythromycin deriv; The adding weight ratio is 3~85% inorganic acid salt or organic acid salt in system, is partition ratio thereby can significantly improve the partition rate of Oxacyclotetradecane,erythromycin deriv in the hydrophobicity organic phase.The sufficient quantity that in abomacetin fermentation filtrating, adds inorganic acid salt or organic acid salt is 8~36% (W/V).
Inorganic acid salt and organic acid salt used among the present invention are: the organic acid salt of sylvite, sodium salt, ammonium salt, hydrochloride, vitriol, 2~8 carbon.Described sylvite comprises: Repone K, vitriolate of tartar, soluble tartrate; Described sodium salt comprises: sodium-chlor, sodium sulfate, sodium acetate, Sodium Propionate, Sodium propanecarboxylate, sodium tartrate, Seignette salt, sodium oxalate, fumaric acid sodium, Trisodium Citrate.
The Oxacyclotetradecane,erythromycin deriv process for extracting that the present invention selects is following: the adding weight percent is 10~35% sodium-chlor or sodium sulfate in ferment filtrate; Under agitation condition; Readjust the distribution ferment filtrating PH7.2~11; Treat that the Oxacyclotetradecane,erythromycin deriv eduction rate reaches 93% when above, get final product solid-liquid separation, obtain to contain the bullion of Oxacyclotetradecane,erythromycin deriv; Also can readjust the distribution ferment filtrating pH value earlier is 7.2~11, and then, the adding weight percent is 10~35% sodium-chlor or sodium sulfate.
Also can in ferment filtrate, add hydrophobic organic solvent, and to add weight percent simultaneously be 5~35% sodium-chlor or sodium sulfate, under agitation condition; Readjust the distribution ferment filtrating PH7.2~11, behind the thorough mixing, leave standstill or centrifugal; Abandon water, must contain the organic phase of Oxacyclotetradecane,erythromycin deriv.
In the present invention; When salting-out process combines with extraction process to use; Used hydrophobic organic solvent is: the alcohols of ETHYLE ACETATE, butylacetate, Isoamyl Acetate FCC, pentyl acetate, 4-methyl-2 pentanone, 4~8 carbon, and they can use separately, also can more than one form the cosolvent use; Usage quantity is 2~50% of a ferment filtrate amount, volume per-cent.
Embodiment
The following example is provided so that people can make much of the present invention, but this can not be interpreted as the restriction to claim scope of the present invention and core content.
Instance 1, get the ferment filtrate 1L that tires to 3321ug Oxacyclotetradecane,erythromycin deriv/ml, under agitation condition, add 300g sodium-chlor, transfer liquid PH8.2 with saturated aqueous sodium carbonate, stir after 5 minutes, suction filtration must contain the wet solids of Oxacyclotetradecane,erythromycin deriv.
The wet solids that will contain Oxacyclotetradecane,erythromycin deriv is all used dissolve with methanol, filtration, carries out HPLC and analyzes, and wherein containing Oxacyclotetradecane,erythromycin deriv is 3198mg, and yield is 96.3% (weight ratio).
Instance 2, get the ferment filtrate 1L that tires to 3321ug Oxacyclotetradecane,erythromycin deriv/ml, under agitation condition, add 200g sodium-chlor, transfer liquid PH8.2 with saturated aqueous sodium carbonate, stir after 5 minutes, suction filtration must contain the wet solids of Oxacyclotetradecane,erythromycin deriv.
The wet solids that will contain Oxacyclotetradecane,erythromycin deriv is all used dissolve with methanol, filtration, carries out HPLC and analyzes, and wherein containing Oxacyclotetradecane,erythromycin deriv is 3039mg, and yield is 91.5% (weight ratio).
Instance 3, get the ferment filtrate 1L that tires to 3321ug Oxacyclotetradecane,erythromycin deriv/ml, be heated to 35 ℃, under agitation condition, add 200g sodium sulfate, transfer liquid PH8.2 with saturated aqueous sodium carbonate, stir after 5 minutes, suction filtration must contain the wet solids of Oxacyclotetradecane,erythromycin deriv.
The wet solids that will contain Oxacyclotetradecane,erythromycin deriv is all used dissolve with methanol, filtration, carries out HPLC and analyzes, and wherein containing Oxacyclotetradecane,erythromycin deriv is 3231mg, and yield is 97.3% (weight ratio).
Instance 4,
Experimental group: get the ferment filtrate 1L that tires to 3321ug Oxacyclotetradecane,erythromycin deriv/ml, be heated to 35 ℃, under agitation condition; Add 80ml butylacetate/butanols cosolvent, add 300g sodium-chlor then, transfer liquid PH8.2 with saturated aqueous sodium carbonate; Stir after 5 minutes; Leave standstill, treat complete layering after, Oxacyclotetradecane,erythromycin deriv content is measured in water intaking mutually.
Control group: other gets the ferment filtrate 1L that tires to 3321ug Oxacyclotetradecane,erythromycin deriv/ml, is heated to 35 ℃, under agitation condition; Add 80ml butylacetate/butanols cosolvent; Transfer liquid PH8.2 with saturated aqueous sodium carbonate then, stir after 5 minutes, leave standstill; After treating complete layering, Oxacyclotetradecane,erythromycin deriv content is measured in water intaking mutually.
Experimental result:
Residual tiring is that 142ug/ml, percentage extraction are 96% in the experimental group water liquid;
Residual tiring is that 587ug/ml, percentage extraction are 82.3% in the control group water liquid.

Claims (2)

1. Oxacyclotetradecane,erythromycin deriv process for extracting; It is characterized in that in abomacetin fermentation filtrating, adding weight percent and be 10~35% sodium-chlor or sodium sulfate; Under agitation condition, readjust the distribution ferment filtrating PH 7.2~11, treat that the Oxacyclotetradecane,erythromycin deriv eduction rate reaches 93% when above; Carry out solid-liquid separation, can obtain to contain the bullion of Oxacyclotetradecane,erythromycin deriv; Also can readjust the distribution ferment filtrating pH value earlier is 7.2~11, adds weight percent then and be 10~35% sodium-chlor or sodium sulfate.
2. Oxacyclotetradecane,erythromycin deriv process for extracting is characterized in that in abomacetin fermentation filtrating, adding volume per-cent and is 2~50% hydrophobic organic solvent, and to add weight percent be 5~35% sodium-chlor or sodium sulfate; Under agitation condition; Readjust the distribution ferment filtrating PH 7.2~11, behind the thorough mixing, leave standstill phase-splitting or centrifugal phase-splitting; Abandon water, must contain the organic phase of Oxacyclotetradecane,erythromycin deriv; Above-described hydrophobic organic solvent is: the alcohols of ETHYLE ACETATE, butylacetate, Isoamyl Acetate FCC, pentyl acetate, 4-methyl-2 pentanone, 4~8 carbon.
CN200710195544A 2007-12-07 2007-12-07 Abomacetin extraction by salting-out method Active CN101450960B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200710195544A CN101450960B (en) 2007-12-07 2007-12-07 Abomacetin extraction by salting-out method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200710195544A CN101450960B (en) 2007-12-07 2007-12-07 Abomacetin extraction by salting-out method

Publications (2)

Publication Number Publication Date
CN101450960A CN101450960A (en) 2009-06-10
CN101450960B true CN101450960B (en) 2012-08-29

Family

ID=40733461

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200710195544A Active CN101450960B (en) 2007-12-07 2007-12-07 Abomacetin extraction by salting-out method

Country Status (1)

Country Link
CN (1) CN101450960B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103159812B (en) * 2011-12-08 2016-03-23 湖南中创化工股份有限公司 A kind of method extracting erythromycin from the erythromycin aqueous solution

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2881162A (en) * 1953-11-16 1959-04-07 Abbott Lab Recovery process

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2881162A (en) * 1953-11-16 1959-04-07 Abbott Lab Recovery process

Also Published As

Publication number Publication date
CN101450960A (en) 2009-06-10

Similar Documents

Publication Publication Date Title
US4886889A (en) Process for recovery of an amino acid from aqueous mixtures thereof
CN101381756B (en) Purification method of super tylosin
JP2009519245A (en) Purification method of echinocandin type compound
CN113648834B (en) Ceramic membrane and preparation method and application thereof
CN101619069A (en) Preparation method of cefotiam hexetil hydrochloride
CN101921302B (en) Purification technology of rokitamycin
CN102040638A (en) Method for preparing nonsolvent of high-purity natamycin
CN106188188B (en) A kind of preparation method of avermectin
CN101450960B (en) Abomacetin extraction by salting-out method
CN103275150A (en) Method for refining and preparing erythromycin thiocyanate
CN100513578C (en) Method for extracting natural beta-caroetne
CN101531694A (en) Method for extracting erythromycins by salting-out method
CN100402516C (en) Prepn process of mofe-til mycophenolate
CN1289609C (en) Method for preparing crystal of lycopene and concentrate
CN101580515B (en) Method for extracting and purifying staurosporin
CN101156664B (en) Method for distilling fucoidin from sea tangle caustic refining liquid
CN103012344B (en) Method of recovering lovastatin from lovastatin crystal mother liquor
CN101709072B (en) Method for efficiently extracting and purifying natamycin
CN103709219A (en) Tylosin extraction method
CN104341377B (en) The method reclaiming lovastatin from lovastatin crystalline mother solution
CN110540570A (en) method for separating and purifying fusidic acid through ion exchange resin
CN1470515A (en) Method for extracting tetrodotoxin from globefish livers
CN109651438A (en) A kind of preparation of modified oxidized magnesium and its application in L-Ascorbic Acid L-O-Phosphate
CN107937472A (en) A kind of method of straight-through synthesis Amoxicillin
CN107446965A (en) A kind of preparation method of ornithine hydrochloride

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: BEIJING AGRICHINA PHARMACEUTICAL CO., LTD.

Free format text: FORMER OWNER: PAN ZHENDE

Effective date: 20131127

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 100089 HAIDIAN, BEIJING TO: 100000 CHANGPING, BEIJING

TR01 Transfer of patent right

Effective date of registration: 20131127

Address after: 100000 Wang Zhuang Industrial Zone, Shahe Airport Road, Changping District, Beijing

Patentee after: BEIJING AGRICHINA PHARMACEUTICAL CO., LTD.

Address before: 100089 Beijing box 8956 Haidian District Wanliu spring Sinorama District Building 5 room 103

Patentee before: Pan Zhende

CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 102209, Changping District science and Technology Park, Beijing, No. 37, building 16, No. 2, building C2034

Patentee after: Beijing Zhongnonghuawei pharmaceutical Limited by Share Ltd

Address before: 100000 Wang Zhuang Industrial Zone, Shahe Airport Road, Changping District, Beijing

Patentee before: BEIJING AGRICHINA PHARMACEUTICAL CO., LTD.

PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Abomacetin extraction by salting-out method

Effective date of registration: 20180910

Granted publication date: 20120829

Pledgee: Huaxia Bank Beijing branch Wanliu Limited by Share Ltd

Pledgor: Beijing Zhongnonghuawei pharmaceutical Limited by Share Ltd

Registration number: 2018990000795

PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20191122

Granted publication date: 20120829

Pledgee: Huaxia Bank Beijing branch Wanliu Limited by Share Ltd

Pledgor: Beijing Zhongnonghuawei pharmaceutical Limited by Share Ltd

Registration number: 2018990000795

PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Abomacetin extraction by salting-out method

Effective date of registration: 20191128

Granted publication date: 20120829

Pledgee: Huaxia Bank Beijing branch Wanliu Limited by Share Ltd

Pledgor: Beijing Zhongnonghuawei pharmaceutical Limited by Share Ltd

Registration number: Y2019990000606

CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: 102209 C2034 2, 16 building, No. 37 Chao Yuan Road, Changping District science and Technology Park, Beijing.

Patentee after: Zhongnonghuawei Pharmaceutical Co., Ltd

Address before: 102209 C2034 2, 16 building, No. 37 Chao Yuan Road, Changping District science and Technology Park, Beijing.

Patentee before: Beijing Zhongnong Huawei Pharmaceutical Co.,Ltd.

PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20210531

Granted publication date: 20120829

Pledgee: Huaxia Bank Beijing branch Wanliu Limited by Share Ltd.

Pledgor: Beijing Zhongnong Huawei Pharmaceutical Co.,Ltd.

Registration number: Y2019990000606

PC01 Cancellation of the registration of the contract for pledge of patent right