CN101012222A - Method of synthesizing Itraconazole - Google Patents
Method of synthesizing Itraconazole Download PDFInfo
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- CN101012222A CN101012222A CN 200710056778 CN200710056778A CN101012222A CN 101012222 A CN101012222 A CN 101012222A CN 200710056778 CN200710056778 CN 200710056778 CN 200710056778 A CN200710056778 A CN 200710056778A CN 101012222 A CN101012222 A CN 101012222A
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Abstract
The invention discloses a synthesizing method of yiqukangpyrazole, which comprises the following steps: dissolving sulfonate in the organic solvent; blending with inorganic alkaline solution, antioxidant and quaternary phase-transfering catalyst according to certain rate; adding hydroxy material; heating to 50-110 deg.c; refluxing 5-20 h; cooling to 40deg.c; removing water phase; cooling to 20-30 deg.c; obtaining rough product.
Description
Technical field
The present invention relates to a kind of synthetic method of itraconazole, belong to pharmaceutical chemistry technical field.
Background technology
Itraconazole is a kind of triazole antifungal agent, has characteristics such as activity is strong, has a broad antifungal spectrum, curative ratio height because of it and is widely used.The synthesis technique more complicated of itraconazole comprises nine steps of main chain, three steps of side chain.The final step of its reaction is condensation reaction, promptly by 2,4-dihydro-4-[4-[4-(4-hydroxy phenyl)-1-piperazinyl] phenyl]-2-(1-methyl-propyl)-]-H-1,2, the 4-triazole-]-ketone (abbreviation hydroxylic species) and suitable-[2-(2,4 dichloro benzene base)-2-(1H-1,2,4-triazole-1-methyl)-1,3-dioxolane-4]-methanesulfonate ester (being called for short the methanesulfonate ester thing) condensation under alkaline condition gets the itraconazole crude product.
The process of this condensation reaction is as follows:
There is following deficiency in this reaction:
1, the yield of itraconazole crude product is lower, has only about 80%.
2, second-rate.Because side reaction is more in this reaction process, foreign matter content is higher, and the content of end product itraconazole crude product can only reach about 97%, thereby needs could obtain qualified elaboration through solvent is repeatedly refining.
Summary of the invention
The synthetic method that the purpose of this invention is to provide a kind of itraconazole of high-quality, high yield.
The object of the invention is achieved by following technical solution, and the synthesis step of condensation reaction comprises:
(1) the sulphonate thing is dissolved in the organic solvent, and mixes with inorganic base aqueous solution, antioxidant and quaternary ammonium salt-type phase transfer catalyst.
Wherein:
The mole ratio of mineral alkali and sulphonate thing is 10~20: 1; The mass ratio of organic solvent and sulphonate thing is 10~20: 1; The mass ratio of antioxidant and sulphonate thing is 0.005~0.05: 1; The mass ratio of quaternary ammonium salt-type phase transfer catalyst and sulphonate thing is 0.05~0.20: 1.
(2) add hydroxylic species.The mole ratio of hydroxylic species and sulphonate thing is 0.8~1.5: 1.
(3) be warming up to 50~110 ℃, back flow reaction 5~20 hours.
(4) be cooled to 40 ℃ afterwards, divide the phase of anhydrating.
(5) continue to be cooled to 20~30 ℃, filter the itraconazole crude product.
Described sulphonate thing is methanesulfonate ester thing, phenylbenzimidazole sulfonic acid ester thing or tolyl sulphonate thing.
Described organic solvent is benzene,toluene,xylene or their mixture.
Described mineral alkali is sodium hydroxide or potassium hydroxide.
Described antioxidant is hydrazine hydrate and hydrochloride, vitriol and/or their mixture;
Described quaternary ammonium salt-type phase transfer catalyst is benzyltriethylammoinium chloride (TEBA), Tetrabutyl amonium bromide (TBA).
In order to obtain better effect, the mass ratio of preferred organic solvent and sulfonic acid clarified butter thing is 13~17: 1, the mass ratio of antioxidant and sulphonate thing is 0.008~0.015: 1, the mass ratio of quaternary ammonium salt-type phase transfer catalyst and sulphonate thing is 0.08~0.12: 1, hydroxylic species and sulphonate thing mole ratio are 0.8~1.2: 1, and the reaction times is 6 hours.
More preferably the mass ratio of organic solvent and sulphonate thing is 15: 1, and the mass ratio of antioxidant and sulphonate thing is 0.01: 1, and quaternary ammonium salt-type phase transfer catalyst is 0.10: 1 with sulphonate amount ratio, and hydroxylic species and sulphonate thing mole ratio are 0.9: 1.Reaction process of the present invention is as follows:
Advantage of the present invention and characteristics are:
1, yield height.The yield of itraconazole crude product is brought up to more than 90% by original about 80%.
2, the quality of itraconazole crude product significantly improves, and content is brought up to more than 99% by about 97%, and foreign matter content drops to by about 2.5% and is lower than 1.0%.
3, greatly reduce the cost that obtains elaboration.Because yield improves, and reduced because of the refining cost that brings increases, the production cost of elaboration significantly reduces.
Following word/term used herein has following implication, and other has except the explanation:
Hydroxylic species: 2,4-dihydro-4-[4-[4-(4-hydroxy phenyl)-1-piperazinyl] phenyl]-2-(1-methyl-propyl)-]-H-1,2, the 4-triazole-]-ketone
Sulphonate thing: suitable-[2-(2,4 dichloro benzene base)-2-(1H-1,2,4-triazole-1-methyl)-1,3-dioxolane-4]-hydrocarbyl sulfonic ester
Embodiment
Further specify the present invention below in conjunction with embodiment, but do not limit the present invention.
Embodiment 1
In reaction flask, add 140 gram water, 45 gram sodium hydroxide, 180 gram toluene, 10 gram hydroxylic species, 12 gram methanesulfonate ester things and 0.1 gram hydrazine hydrate, 1.0 gram TEBA were warming up to 110 ℃ of back flow reaction 8 hours.Reaction is complete to be cooled to 40 ℃, tells alkali lye.Continue to be cooled to room temperature again, filter, get itraconazole crude product crystallization 17.2 grams.Yield 95.0%, foreign matter content are 0.60%.
Embodiment 2
In reaction flask, add 140 gram water, 45 gram sodium hydroxide, 180 gram toluene, 10 gram hydroxylic species, 12 gram methanesulfonate ester things and 0.2 gram hydrazine hydrate, 1.0 gram TEBA were warming up to 110 ℃ of back flow reaction 10 hours.According to embodiment 1 operation, get itraconazole crude product crystallization 16.8 grams, yield 93.0%, foreign matter content are 0.80%.
Embodiment 3
In reaction flask, add 140 gram water respectively, 47 gram potassium hydroxide, 180 gram toluene, 10 gram hydroxylic species, 12 gram methanesulfonate ester things and 0.1 gram hydrazine hydrate, 1.0 gram TEBA were warming up to 110 ℃ of back flow reaction 7 hours.According to embodiment 1 operation, get itraconazole crude product crystallization 17.1 grams, yield 95.0%, foreign matter content are 0.62%.
Embodiment 4
In reaction flask, add 140 gram water respectively, 40 gram sodium hydroxide, 180 gram toluene, 10 gram hydroxylic species, 13 gram p-methylphenyl sulphonate things and 0.1 gram hydrazine hydrate hydrochloride, 1.0 gram TEBA were warming up to 110 ℃ of back flow reaction 8 hours.According to embodiment 1 operation, get itraconazole crude product crystallization 16.5 grams, yield 91.5%, foreign matter content are 0.81%.
Embodiment 5
In reaction flask, add 140 gram water respectively, 45 gram sodium hydroxide, 180 gram dimethylbenzene, 10 gram hydroxylic species, 13 gram p-methylphenyl sulphonate things and 0.1 gram hydrazine hydrate vitriol, 1.0 gram TEBA were warming up to 110 ℃ of back flow reaction 12 hours.According to embodiment 1 operation, get itraconazole crude product crystallization 16.7 grams, yield 91.6%, foreign matter content are 0.74%.
Claims (10)
1. the synthetic method of an itraconazole, it is characterized in that: the synthesis step of the condensation reaction of its final step comprises:
1) the sulphonate thing is dissolved in the organic solvent, and mixes with inorganic base aqueous solution, antioxidant and quaternary ammonium salt-type phase transfer catalyst;
2) add hydroxylic species, the mole ratio of hydroxylic species and sulphonate thing is 0.8~1.5: 1;
3) be warming up to 50~110 ℃, back flow reaction 5~20 hours;
4) be cooled to 40 ℃ afterwards, divide the phase of anhydrating;
5) continue to be cooled to 20~30 ℃, filter the itraconazole crude product.
2, the synthetic method of itraconazole according to claim 1 is characterized in that:
The mole ratio of mineral alkali and sulphonate thing is 10~20: 1; The mass ratio of organic solvent and sulphonate thing is 10~20: 1; The mass ratio of antioxidant and sulphonate thing is 0.005~0.05: 1; The mass ratio of quaternary ammonium salt-type phase transfer catalyst and sulphonate thing is 0.05~0.20: 1.
3, the synthetic method of itraconazole according to claim 1 is characterized in that: described organic solvent is benzene,toluene,xylene or their mixture.
4, the synthetic method of itraconazole according to claim 1 is characterized in that: described mineral alkali is sodium hydroxide or potassium hydroxide.
5, the synthetic method of itraconazole according to claim 1 is characterized in that: oxygenant is hydrazine hydrate and hydrochloride, vitriol and/or their mixture.
6, the synthetic method of itraconazole according to claim 1 is characterized in that: described quaternary ammonium salt-type phase transfer catalyst is benzyltriethylammoinium chloride or Tetrabutyl amonium bromide.
7, the synthetic method of itraconazole according to claim 1 is characterized in that: the sulphonate thing is methanesulfonate ester, phenylbenzimidazole sulfonic acid ester or tolyl sulphonate thing.
8, the synthetic method of itraconazole according to claim 1, it is characterized in that: the mass ratio of organic solvent and sulphonate thing is 13~17: 1, the mass ratio of antioxidant and sulphonate thing is 0.008~0.015: 1, the mass ratio of quaternary ammonium salt-type phase transfer catalyst and sulphonate thing is 0.08~0.12: 1, and hydroxylic species and sulphonate thing mole ratio are 0.8~1.2: 1.
9, the synthetic method of itraconazole according to claim 1, it is characterized in that: the mass ratio of organic solvent and sulphonate thing is 15: 1, the mass ratio of antioxidant and sulphonate thing is 0.01: 1, quaternary ammonium salt-type phase transfer catalyst is 0.10: 1 with sulphonate amount ratio, and hydroxylic species and sulphonate thing mole ratio are 0.9: 1.
10, the synthetic method of itraconazole according to claim 1 is characterized in that: reflux time is 6 hours.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102351850A (en) * | 2009-01-14 | 2012-02-15 | 重庆华邦胜凯制药有限公司 | Method for refining itraconazole |
CN101775009B (en) * | 2009-01-14 | 2012-09-05 | 重庆华邦胜凯制药有限公司 | Composite method of itraconazole and refining method |
CN109293642A (en) * | 2018-09-29 | 2019-02-01 | 北京莱瑞森医药科技有限公司 | A kind of polishing purification method of Itraconazole |
-
2007
- 2007-02-13 CN CNB2007100567784A patent/CN100519556C/en active Active
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102351850A (en) * | 2009-01-14 | 2012-02-15 | 重庆华邦胜凯制药有限公司 | Method for refining itraconazole |
CN101775009B (en) * | 2009-01-14 | 2012-09-05 | 重庆华邦胜凯制药有限公司 | Composite method of itraconazole and refining method |
CN109293642A (en) * | 2018-09-29 | 2019-02-01 | 北京莱瑞森医药科技有限公司 | A kind of polishing purification method of Itraconazole |
CN109293642B (en) * | 2018-09-29 | 2020-07-03 | 北京莱瑞森医药科技有限公司 | Refining and purifying method of itraconazole |
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