CN102627633A - New method for purifying elubiol - Google Patents

New method for purifying elubiol Download PDF

Info

Publication number
CN102627633A
CN102627633A CN2012100758937A CN201210075893A CN102627633A CN 102627633 A CN102627633 A CN 102627633A CN 2012100758937 A CN2012100758937 A CN 2012100758937A CN 201210075893 A CN201210075893 A CN 201210075893A CN 102627633 A CN102627633 A CN 102627633A
Authority
CN
China
Prior art keywords
health azoles
new health
mixing solutions
elubiol
water
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
CN2012100758937A
Other languages
Chinese (zh)
Inventor
颜国和
林超成
曾灶兴
刘亚静
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.)
ZHEJIANG PEGENT CHEMICAL CO Ltd
Original Assignee
ZHEJIANG PEGENT CHEMICAL CO Ltd
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 ZHEJIANG PEGENT CHEMICAL CO Ltd filed Critical ZHEJIANG PEGENT CHEMICAL CO Ltd
Priority to CN2012100758937A priority Critical patent/CN102627633A/en
Publication of CN102627633A publication Critical patent/CN102627633A/en
Pending legal-status Critical Current

Links

Landscapes

  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

The invention discloses a new method for purifying elubiol. 2-methyl-2-pentanone which is used in present elubiol recrystallization has a high price, is not economic, and is detrimental to the human health because ketone chemicals are residual in products. The method of the invention comprises the following steps: 1, dissolving crude elubiol with a mixed solution of water and a low chain alkyl alcohol at 50-85DEG C; and 2, decoloring by adding active carbon to the elubiol-dissolved mixed solution, filtering to remove carbon, crystallizing by cooling to a certain temperature, filtering again, and drying. According to obtained fine elubiol, the content is above 99.0%, the HPLC purity is above 99.5%, and the melting point is between 127.6DEG C and 130DEG C. The method of the invention has the advantages of conciseness, low cost, good stability of the purified elubiol, and total molar yield of the reaction of 89-91%.

Description

New health azoles New Method of Purification
Technical field
The invention belongs to technical field of chemistry and chemical engineering, relate in particular to a kind of new health azoles New Method of Purification.
Background technology
New health azoles is the verivate of KETOKONAZOL (II), and chemistry is by name: cis-4-[4-[[2-(2,4 dichloro benzene base)-2-(1H-imidazoles-1-ylmethyl)-1,3-dioxolane-4-yl] methoxyl group] phenyl]-1-piperazine carboxylic acid ethyl ester (I), and structural formula is following:
Figure 2012100758937100002DEST_PATH_IMAGE002
New health azoles is the same with traditional imidazoles antimicrobial product KETOKONAZOL, is a kind of imidazoles New-type wide-spectrum antifungal products, can suppress the biosynthesizing of fungi ergosterol, and changes the composition of other lipoid substance of cytolemma.Candidiasis, Cryptococcus neoformans, Histoplasma capsulatum, Blastomyces dermatitidis and coccidioides immitis etc. all there is antagonistic action; But compare with KETOKONAZOL; The latter can not be used for personal care articles, and new health azoles is water-soluble better than KETOKONAZOL, is fit to the personal care articles field use; Listed European personal care articles use range in, market outlook are boundless.
Synthesizing of new health azoles; In U.S. Pat 4335125, with suitable-[2-(2,4 dichloro benzene base)-2-(1H-imidazoles-1-ylmethyl)-1; 3-dioxolane-4-yl] methyl alcohol p-toluenesulfonic esters (III; The active ester pattern) be raw material, get with 4-(4-hydroxy phenyl)-1-piperazine carboxylic acid ethyl ester (IV) condensation, specific as follows:
Figure 2012100758937100002DEST_PATH_IMAGE004
In US4335125, new health azoles is with 2-methyl-2 pentanone recrystallization, and the new health azoles fusing point that obtains is 112.2 ℃
In world patent WO93/18743, new health azoles is synthetic to be to be starting raw material with the KETOKONAZOL, and after hydrolysis, acidylate, refining and commentaries on classics crystal formation obtains the new health azoles of I type, and is specific as follows:
Figure 2012100758937100002DEST_PATH_IMAGE006
Its purification is with 2-methyl-2 pentanone crystallization, and reaction is 84.9% with crystallization yield, and the back makes the transition to the I type with acetone, and the yield of transition is 82.1%, obtains the total recovery 69.7% of I type, 127.6 ℃ of the new health azoles fusing points of I type.
In WO93/18743, also mentioned the I type and the II type proterties of new health azoles, the DSC maximum peak of dystectic I type is at 127.6 ℃, and the DSC maximum peak of low-melting II type is at 110.9 ℃, the I type is more stable than II type, preferentially is used for the makeup that human body is used.
In above-mentioned two patents, recrystallization is all used 2-methyl-2 pentanone, and not only price is high, uneconomical, and the ketone chemical residues is disadvantageous to HUMAN HEALTH in product.
In Chinese patent prospectus CN101665490A; Mention and use re-crystallizing in ethyl acetate; Recrystallization yield 69.8% 84.5%; Use ETHYLE ACETATE organism recrystallization, but yield is not high, and does not mention the fusing point of product.
Summary of the invention
The objective of the invention is deficiency, a kind of new health azoles New Method of Purification is provided to prior art.
The technical solution adopted for the present invention to solve the technical problems step is following:
Step (1). the mixing solutions of water and low paraffinic hydrocarbons alcohol; Temperature be 50
Figure 221209DEST_PATH_IMAGE008
85 ℃ of new health azoles bullions of dissolving down, in the mixing solutions ratio of water and low paraffinic hydrocarbons alcohol be 3/7
Figure 6763DEST_PATH_IMAGE008
1/19;
Low paraffinic hydrocarbons alcohol in the described step (1) comprises methyl alcohol, ethanol, propyl alcohol, Virahol; The mixing solutions of described water and low paraffinic hydrocarbons alcohol and new health azoles bullion weight ratio be 10/1
Figure 869677DEST_PATH_IMAGE008
2/1;
Step (2). in the mixing solutions that has dissolved new health azoles bullion; Add activated carbon decolorizing; After filtering de-carbon, be cooled to-5
Figure 93985DEST_PATH_IMAGE008
15 ℃ of crystallizations; And then filter and drying; The new health azoles elaboration content that obtains is more than 99.0%; HPLC purity is more than 99.5%, fusing point 127.6
Figure 358744DEST_PATH_IMAGE008
between 130 ℃;
As preferably; The temperature of the new health azoles of the dissolving bullion described in the step (1) be 75
Figure 580778DEST_PATH_IMAGE008
80 ℃; Low paraffinic hydrocarbons alcohol is ethanol; In the mixing solutions water and alcoholic acid ratio be 1/1
Figure 930988DEST_PATH_IMAGE008
3/17, water and alcoholic acid mixing solutions and new health azoles bullion weight ratio be preferred 4/1
Figure 693407DEST_PATH_IMAGE008
3/1;
As preferably, the Tc described in the step (2) be 0
Figure 2012100758937100002DEST_PATH_IMAGE010
5 ℃.
Preferred as further; Low paraffinic hydrocarbons alcohol described in the step (1) is ethanol, in the mixing solutions water and alcoholic acid ratio be 3/7
Figure 628652DEST_PATH_IMAGE008
1/4.
Beneficial effect of the present invention is following:
With the present invention's new health azoles of purifying; The product purity that method is succinct, with low cost, the back of purifying obtains is more than 99.5%; Content is more than 99.0%; Fusing point 127.6-130 ℃, the good stability of products that obtains, and react total molar yield 89
Figure 21587DEST_PATH_IMAGE010
91%.
Embodiment
Below in conjunction with embodiment the present invention is described further.
Embodiment 1
Step (1). water and alcoholic acid mixing solutions are 50 ℃ of new health azoles bullions of dissolving down in temperature, and water and alcoholic acid ratio are 3:7 in the mixing solutions,
Described water and alcoholic acid mixing solutions and new health azoles bullion weight ratio be 10:1;
Step (2). in the mixing solutions that has dissolved new health azoles bullion, add activated carbon decolorizing, behind the filtration de-carbon, be cooled to-5 ℃ of post crystallizations; And then filter and drying; The new health azoles elaboration content that obtains is 99.3%; HPLC purity is 99.7%, fusing point 127.6
Figure 859093DEST_PATH_IMAGE008
129 ℃.
Embodiment 2
Step (1). water and alcoholic acid mixing solutions are 75 ℃ of new health azoles bullions of dissolving down in temperature, and water and alcoholic acid ratio are 3:10 in the mixing solutions;
Described water and alcoholic acid mixing solutions and new health azoles bullion weight ratio be 7:2;
Step (2). in the mixing solutions that has dissolved new health azoles bullion, add activated carbon decolorizing, behind the filtration de-carbon, be cooled to 3 ℃ of post crystallizations; And then filter and drying; The new health azoles elaboration content that obtains is 99.8%; HPLC purity is 99.9%, fusing point 128.5 130 ℃.
Embodiment 3
Step (1). water and alcoholic acid mixing solutions are 85 ℃ of new health azoles bullions of dissolving down in temperature, and water and alcoholic acid ratio are 1:19 in the mixing solutions;
Described water and alcoholic acid mixing solutions and new health azoles bullion weight ratio be 2:1;
Step (2). in the mixing solutions that has dissolved new health azoles bullion, add activated carbon decolorizing, behind the filtration de-carbon, be cooled to 5 ℃ of post crystallizations; And then filter and drying; The new health azoles elaboration content that obtains is 99.1%; HPLC purity is 99.6%, fusing point 128 129 ℃.
Embodiment 4
Step (1). the mixing solutions of water and methyl alcohol is 85 ℃ of new health azoles bullions of dissolving down in temperature, and the ratio of water and methyl alcohol is 1:4 in the mixing solutions;
The mixing solutions of described water and methyl alcohol and new health azoles bullion weight ratio be 2:1;
Step (2). in the mixing solutions that has dissolved new health azoles bullion, add activated carbon decolorizing, behind the filtration de-carbon, be cooled to 15 ℃ of post crystallizations; And then filter and drying; The new health azoles elaboration content that obtains is 99.1%; HPLC purity is 99.6%, fusing point 128
Figure 835249DEST_PATH_IMAGE008
129 ℃.
Embodiment 5
Step (1). in reaction kettle, drop into 10% hydrochloric acid of 100KG KETOKONAZOL and 110KG, reacted 20 hours down, be cooled to room temperature at 85 ℃; The toluene that adds 400L then slowly adds 50% sodium hydroxide solution of 96.5KG again, separates out crystalline solid, and is centrifugal, with 40KG water washing filter also, dry, oven dry, the 92.1KG hydrolyzate, HPLC purity is more than 99.5%, yield 100%.
Step (2). the 92.1KG hydrolyzate that step (1) is obtained drops in the reaction kettle; Drop into 520KG methylene dichloride and 36KG salt of wormwood again, drip the 25KG Vinyl chloroformate under the room temperature, stirring reaction is 3 hours then; Add water 300KG; Organic phase is got in layering, and underpressure distillation is reclaimed methylene dichloride to doing De Xinkang azoles bullion.
Step (3). the new health azoles bullion that will obtain, add in the 400KG water-ethanol mixing solutions (weight ratio 25:75), be heated to 75 ℃ and dissolve clear; After adding the carbon filtration, cooling, crystallization; Filter, drain, oven dry; Get the new health azoles of 95.6KG, HPLC purity 99.6%, chemistry titration content 99.4%; 128.5 ℃ of fusing points 127.6
Figure 160051DEST_PATH_IMAGE008
, total recovery 90.5%.

Claims (4)

1. new health azoles New Method of Purification is characterized in that, comprises the steps:
Step (1). the mixing solutions of water and low paraffinic hydrocarbons alcohol; Temperature be 50
Figure 2012100758937100001DEST_PATH_IMAGE002
85 ℃ of new health azoles bullions of dissolving down, in the mixing solutions ratio of water and low paraffinic hydrocarbons alcohol be 3/7
Figure 818717DEST_PATH_IMAGE002
1/19;
Low paraffinic hydrocarbons alcohol in the described step (1) comprises methyl alcohol, ethanol, propyl alcohol, Virahol; The mixing solutions of described water and low paraffinic hydrocarbons alcohol and new health azoles bullion weight ratio be 1/10
Figure 912575DEST_PATH_IMAGE002
2/1;
Step (2). in the mixing solutions that has dissolved new health azoles bullion; Add activated carbon decolorizing; After filtering de-carbon, be cooled to-5
Figure 647313DEST_PATH_IMAGE002
15 ℃ of crystallizations; And then filter and drying; The new health azoles elaboration content that obtains is more than 99.0%; HPLC purity is more than 99.5%, fusing point 127.6
Figure 196761DEST_PATH_IMAGE002
between 130 ℃.
2. new health azoles New Method of Purification according to claim 1; The temperature that it is characterized in that the new health azoles of the dissolving bullion described in the step (1) be 75
Figure 307937DEST_PATH_IMAGE002
80 ℃; Low paraffinic hydrocarbons alcohol is ethanol; In the mixing solutions water and alcoholic acid ratio be 1/1
Figure 318618DEST_PATH_IMAGE002
3/17;, water and alcoholic acid mixing solutions and new health azoles bullion weight ratio be preferred 4/1
Figure 224257DEST_PATH_IMAGE002
3/1.
3. new health azoles New Method of Purification according to claim 1; It is characterized in that the low paraffinic hydrocarbons alcohol described in the step (1) is ethanol, in the mixing solutions water and alcoholic acid ratio be 3/7
Figure 258072DEST_PATH_IMAGE002
1/4.
4. new health azoles New Method of Purification according to claim 1, it is characterized in that the Tc described in the step (2) be 0
Figure 2012100758937100001DEST_PATH_IMAGE004
5 ℃.
CN2012100758937A 2012-03-21 2012-03-21 New method for purifying elubiol Pending CN102627633A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012100758937A CN102627633A (en) 2012-03-21 2012-03-21 New method for purifying elubiol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012100758937A CN102627633A (en) 2012-03-21 2012-03-21 New method for purifying elubiol

Publications (1)

Publication Number Publication Date
CN102627633A true CN102627633A (en) 2012-08-08

Family

ID=46586054

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012100758937A Pending CN102627633A (en) 2012-03-21 2012-03-21 New method for purifying elubiol

Country Status (1)

Country Link
CN (1) CN102627633A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4144346A (en) * 1977-01-31 1979-03-13 Janssen Pharmaceutica N.V. Novel 1-(1,3-dioxolan-2-ylmethyl)-1H-imidazoles
WO1993018743A1 (en) * 1992-03-20 1993-09-30 Janssen Pharmaceutica N.V. Agent for regulating the greasiness of the skin
CN101665490A (en) * 2008-09-01 2010-03-10 浙江东亚药业有限公司 Method for preparing ketoconazole derivatives
CN102070620A (en) * 2011-01-25 2011-05-25 南京白敬宇制药有限责任公司 Preparation method of antibacterial ester

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4144346A (en) * 1977-01-31 1979-03-13 Janssen Pharmaceutica N.V. Novel 1-(1,3-dioxolan-2-ylmethyl)-1H-imidazoles
WO1993018743A1 (en) * 1992-03-20 1993-09-30 Janssen Pharmaceutica N.V. Agent for regulating the greasiness of the skin
CN101665490A (en) * 2008-09-01 2010-03-10 浙江东亚药业有限公司 Method for preparing ketoconazole derivatives
CN102070620A (en) * 2011-01-25 2011-05-25 南京白敬宇制药有限责任公司 Preparation method of antibacterial ester

Similar Documents

Publication Publication Date Title
CN104230803B (en) Preparation method of hydroxychloroquine sulfate
CN101941969B (en) Preparation method of moxifloxacin hydrochloride
CN101531640B (en) Preparation method of Quizalofop-p-ethyl with high optical content
CN107216289B (en) Preparation method of edaravone
EP3395813A1 (en) Voriconazole intermediate and voriconazole synthesis method
CN102190628A (en) Preparation method of 5-fluoro-6-ethyl-4-hydroxypyrimidine intermediate and Voriconazole
CN103936671A (en) Preparation method for montelukast sodium intermediate
CN102617542A (en) Method for preparing and purifying olmesartan intermediate
CN104860872A (en) Bis-(3R,4R)-1-benzyl-N,4-dimethyl piperidin-3-amine L-di-p-toluyl tartrate synthesis method
CN104356111A (en) Method for preparing dabigatran etexilate hydrolysis impurities
CN101671292B (en) Synthetic method of fexofenadine hydrochloride
CN101747210A (en) Method for preparing alpha-(di-n-butylaminomethyl)-2,7-dichloro-4-fluorenemethanol and the hydrochloride thereof
CN102627633A (en) New method for purifying elubiol
CN104774161A (en) Peptide and protein pegylation agent synthesis method
CN103965058B (en) A kind of production technology of memantine
CN105085396A (en) Intermediate for preparing bedaquiline, preparation method therefor and application thereof
CN103922925B (en) A kind of production technique of Fenofibric Acid
CN101914055A (en) Reductive preparation method of imide
CN104628518A (en) Method for synthesizing repaglinide key intermediate
CN104761599A (en) Preparation method of 5,4'-dihydroxy flavone-7-O-D-glucuronic acid
CN107488178B (en) Preparation method of high-purity pralatrexate intermediate
CN101823986A (en) Preparation method for tert-butyl carbazate
CN105418507A (en) Preparation method for 1-(3-methyl-1-phenyl-1H-pyrazole-5-yl)piperazine
CN101928278A (en) (S)-4-[(4-chlorphenyl)(pyridine-2-yl)methoxyl]piperidinehydroxyphenpropionate and application thereof
CN107304194A (en) The method for preparing Dapagliflozin

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20120808