CN116751188A - Synthesis method of process impurities generated by voriconazole key intermediate - Google Patents

Synthesis method of process impurities generated by voriconazole key intermediate Download PDF

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Publication number
CN116751188A
CN116751188A CN202310757349.9A CN202310757349A CN116751188A CN 116751188 A CN116751188 A CN 116751188A CN 202310757349 A CN202310757349 A CN 202310757349A CN 116751188 A CN116751188 A CN 116751188A
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voriconazole
impurity
starting material
bromosuccinimide
synthesis method
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王浩
姜根华
霍志甲
石亮亮
姚志雄
张静
张�杰
王丽红
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Tianjin Lisheng Pharmaceutical Co ltd
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Tianjin Lisheng Pharmaceutical Co ltd
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Abstract

The invention discloses a synthesis method of a process impurity D generated by a voriconazole key intermediate, which comprises the following steps: reacting the starting material A, N-bromosuccinimide and azodiisobutyronitrile in dichloromethane, quenching by sodium sulfite aqueous solution, extracting, and distilling to obtain an intermediate B; the intermediate B, the initial raw material C, zinc powder and iodine are reacted in tetrahydrofuran solvent, quenched by glacial acetic acid, extracted, alkali regulated and column chromatography to obtain the compound D. The purity of the synthesized process impurity D can reach more than 95%, and the process impurity D can be used as an impurity reference substance when relevant substances of voriconazole intermediates, bulk drugs and preparations are detected, so that stricter quality control of voriconazole is realized.

Description

Synthesis method of process impurities generated by voriconazole key intermediate
Technical Field
The invention belongs to the technical field of pharmaceutical chemistry synthesis, and particularly relates to a synthesis method of process impurities in the process of producing a key intermediate of voriconazole.
Background
Voriconazole (Voriconazole) is a second generation triazole antifungal agent developed by the american-type scion company, marketed in the united states in 2002, and is mainly used clinically for treating acute or chronic deep fungal infections, and has the trade name Vfend. Compared with the traditional fungus medicines, the voriconazole as the fluconazole derivative has wider antibacterial spectrum, better safety, and good curative effect on oral administration and injection, especially invasive aspergillus infiltration infection, and is mainly used for treating candida diseases, deep subcutaneous tissue candida infection and candida infection of abdomen, kidney, bladder wall and wounds. The voriconazole has been a new market with the characteristic of high efficiency and low toxicity, and has great economic value and market prospect, so that the synthesis process of the voriconazole is necessary to be optimized, which is more beneficial to industrialized production and has better economic benefit.
There is a great deal of technical accumulation for the production and preparation of voriconazole. The invention discloses a synthesis process of voriconazole with the publication number of CN 113354625A; the publication number is CN111440152A, and the publication number is Voriconazole preparation method; the publication number is CN106632267A, and the publication number is Voriconazole synthesis method; the publication No. CN104884450A, entitled "method for preparing voriconazole and analogues thereof", discloses various preparation processes of voriconazole. The main synthetic route is as follows: 4-chloro-6-ethyl-5-fluoropyrimidine is used as a raw material to prepare voriconazole; wherein the reaction equation is as follows:
in the production of voriconazole according to the disclosed preparation process, it was found that a distinct impurity peak appears during the production of the intermediate 2 condensate and that this impurity is derivatised in the final voriconazole product. The impurities will have an impact on quality. At present, no effective synthesis method for the process impurity D in the synthesis process of the voriconazole intermediate condensate is reported so far, the impurity is researched by the patent with application number 202211660126.4 of the company, and the impurity is prepared by a high-pressure liquid chromatography method, but the high-pressure liquid chromatography is needed by adopting the liquid phase preparation method, so that the cost is high, and the impurity amount is low. In order to solve the problems of the prior art, a method for synthesizing the groceries is developed, which can use conventional synthesis equipment, adopts a simple process, has easily controlled preparation conditions, and is suitable for industrial production. The method for synthesizing the impurity can effectively help us to determine the mode for effectively removing the impurity, improves the purity of the voriconazole condensate from 90.3% to 97.6%, and greatly improves the purity of the voriconazole intermediate, thereby improving the quality of the voriconazole finished product.
Disclosure of Invention
Aiming at the technical problems in the prior art, the invention provides a synthesis method of voriconazole intermediate impurities, which can synthesize the impurities stably, with high yield and high purity, and can be used as an impurity reference substance for strictly and accurately controlling the quality of voriconazole in the preparation process. Therefore, the invention provides a simple synthesis method for synthesizing process impurities.
In order to achieve the above object, the present invention provides the following technical solutions:
the synthesis method of the process impurity D generated by the voriconazole key intermediate is characterized by comprising the following steps of:
(1) Reacting the initial raw materials A, N-bromosuccinimide and azodiisobutyronitrile in dichloromethane at the reaction temperature of 30-50 ℃ for 10-12 hours, quenching with sodium sulfite aqueous solution, extracting, and distilling to obtain an intermediate B; the starting material a: the molar ratio of N-bromosuccinimide is 1:1.0- -1.5
(2) Reacting the intermediate B obtained in the step 1) with the initial raw material C, zinc powder and iodine in tetrahydrofuran solvent, quenching with glacial acetic acid, extracting, regulating alkali, and performing column chromatography to obtain a compound D; the starting material C: the ratio of zinc powder is 1: 1-5.5;
the process impurity D is mainly in the voriconazole condensate, and can be used as a reference substance for voriconazole quality research.
The invention also discloses application of the process impurity D generated by the voriconazole condensate in preparing a control sample and controlling the quality of the voriconazole condensate, and experimental results prove that: the impurity D monomer is taken in proper amount, a solution of 0.5mg/ml is prepared by a diluent, the purity of the main peak is 97.6 percent calculated by an area normalization method according to the detection method of relevant substances of voriconazole condensate. The high-quality voriconazole raw material and the preparation can better meet the continuously and rapidly growing demands of antifungal drugs in the domestic market, are more beneficial to industrial production, and generate good economic benefit.
The beneficial effects of the process impurities generated in the process of producing voriconazole condensate disclosed by the invention are as follows:
(1) The invention provides a novel synthesis method of voriconazole impurities, and the structure is confirmed, so that the content of the impurities in voriconazole can be accurately and quantitatively analyzed, the accurate control of the content of the impurities in the production process is facilitated, and a research basis is provided for monitoring the production quality and improving the production process level; the preparation method of the invention can synthesize the impurity stably, with high yield and high purity, and provides a contrast basis for intensive study of the quality of raw materials and preparations.
(2) Since the voriconazole intermediate condensate can generate about 10% of impurity D during the production process, the purification by the subsequent prior art confirms that the impurity can be derived or transferred to the voriconazole finished product in the subsequent step, affecting the quality of the product. The derivative of the detected impurity D can be effectively controlled below 0.1% in the voriconazole finished product, and meets the requirements of the existing pharmacopoeia quality standard. Therefore, the preparation and structure of the impurity have great guiding significance for quality control and curative effect of voriconazole mass production.
(3) The process impurity D generated by the voriconazole key intermediate can be used for preparing a reference sample and controlling the quality of the voriconazole condensate.
The invention is described in more detail below:
the synthesis route of the synthesis method of the voriconazole condensate process impurity D disclosed by the invention is as follows:
(1) Reacting the initial raw materials A, N-bromosuccinimide and azodiisobutyronitrile in dichloromethane at the reaction temperature of 30-50 ℃ for 10-12 hours, quenching with sodium sulfite aqueous solution, extracting, and distilling to obtain an intermediate B; the starting material a: the molar ratio of N-bromosuccinimide is 1:1.0 to 1.5;
(2) Reacting the intermediate B obtained in the step 1) with the initial raw material C, zinc powder and iodine in tetrahydrofuran solvent, quenching with glacial acetic acid, extracting, regulating alkali, and performing column chromatography to obtain a compound D; the starting material C: the ratio of zinc powder is 1: 1-5.5;
in the synthesis method of the present invention, the starting material a is preferably: the ratio of N-bromosuccinimide is 1:1.2.
in the synthesis method of the invention, the ratio of the starting raw material C to zinc powder is preferably 1:2.5.
in the synthesis method of the present invention, the reaction condition temperature in step 1) is preferably 35 ℃ for 10 hours.
Drawings
FIG. 1 is a nuclear magnetic hydrogen spectrum of process impurity D;
FIG. 2 is a nuclear magnetic carbon spectrum of process impurity D;
fig. 3 is a mass spectrum of process impurity D positive ions.
Detailed Description
For the sake of simplicity and clarity, descriptions of well-known techniques are omitted appropriately below to avoid those unnecessary detail from affecting the description of the present solution. The following describes a further embodiment of the process for the synthesis of the process impurity D produced in the production of voriconazole according to the invention, in particular the starting materials A and C which can be synthesized by the process provided in CN104884450A or are commercially available; intermediate B, N-bromosuccinimide, azobisisobutyronitrile, and zinc powder, iodine, and the like used are commercially available.
Example 1
A synthetic method of a process impurity D generated in the production of a key intermediate of voriconazole, comprising the following steps:
1) 51.5g (0.321 mol) of the starting material A,400ml of methylene chloride, 68.6g (0.385 mol) of N-bromosuccinimide and 1.58g (0.010 mol) of azobisisobutyronitrile were each put into a 500ml three-necked flask equipped with a thermometer and mechanically stirred, and reacted at a temperature of 35℃for 10 hours, after the completion of the reaction, the aqueous sodium sulfite solution was quenched, washed with water twice, and distilled under reduced pressure to remove methylene chloride to obtain a crude product, and then 62.3g of intermediate B was obtained by column chromatography in a yield of 81.1% and a content of 95.3%.
2) To a 500ml three-necked flask equipped with a thermometer under nitrogen atmosphere and mechanically stirred, 28.2 g (0.434 mol) of zinc powder and 87.0ml of tetrahydrofuran were added, a solution of 19.36g (0.077 mol) of iodine in 58.0ml of tetrahydrofuran was slowly added at 20℃and reacted for 0.5 hour, 51.5g (0.215 mol) of intermediate B was weighed, 38.73g (0.174 mol) of starting material C was dissolved in 190ml of tetrahydrofuran, and the mixture was dropped into the reaction flask at a temperature of 10℃or below. A289 ml aqueous solution of 48.2g glacial acetic acid was added dropwise thereto at a temperature of 10℃or below, followed by stirring for 0.5 hours. The reaction solution was filtered, and after concentrating the filtrate, 289ml of dichloromethane was extracted with petroleum ether/ethyl acetate=1: column chromatography on 1 column gave 26.5g of impurity D in 82.0% yield with a content of 99.72%.
As shown in fig. 1 1 H NMR(DMSO-d 6 )8.968(s,1H),8.880(s,1H),8.256(d,1H),7.630(d,1H),
7.290(dt,1H),7.086-7.203(m,1H),6.944-6.898(td,1H),5.997(s,1H),5.048(m,1H),4.821(d,1H),4.297-4.382(q,2H), 1.677(t,3H),1.104-1.150(dd,3H).
As shown in fig. 2 13 C NMR(DMSO-d 6 ) The method comprises the steps of carrying out a first treatment on the surface of the MS as shown in fig. 3: [ M+H ]] + =508.1.
The synthetic process impurity D with high efficiency and high quality can be synthesized according to the formula. The impurity in the reaction process is less, the reaction is quick, the purification is simple, and the synthetic process impurity D is easy to obtain.
Example 2
1) 51.5g (0.321 mol) of the starting material A,400ml methylene chloride, 74.23g (0.417 mol) of N-bromosuccinimide and 1.58g (0.010 mol) of azodiisobutyronitrile are respectively added into a 500ml three-necked flask equipped with a thermometer and mechanically stirred, the reaction is carried out for 12 hours at the temperature of 45 ℃, after the reaction is finished, the aqueous solution of sodium sulfite is quenched, the reaction is washed twice, the methylene chloride is removed by reduced pressure distillation to obtain a crude product, and 61.8g of intermediate B is obtained by column chromatography, the yield is 80.5%, and the content is 92.1%.
2) 33.93g (0.522 mol) of zinc powder and 87.0ml of tetrahydrofuran are added into a 500-ml three-necked flask which is mechanically stirred under the protection of nitrogen, 19.36g (0.077 mol) of iodine and 58.0ml of tetrahydrofuran solution are slowly added at 20 ℃ to react for 0.5 hour, 51.5g (0.215 mol) of intermediate B and 38.73g (0.174 mol) of initial raw material C are weighed and dissolved in 190ml of tetrahydrofuran, the temperature is controlled to be lower than 10 ℃,289ml of aqueous solution of glacial acetic acid is controlled to be lower than 10 ℃, and stirring is carried out for 0.5 hour. The reaction solution was filtered, and after concentrating the filtrate, 289ml of dichloromethane was extracted with petroleum ether/ethyl acetate=1: column chromatography on 1 column gave 21.2g of impurity D, yield 65.6% and content 96.5%.
Example 3
Octadecylsilane chemically bonded silica is used as filler (Kromasil 100-5-C18,4.6mm×250mm,5 μm or chromatographic column with equivalent efficacy); gradient elution was performed according to Table 1 with 0.02mol/L ammonium formate solution (containing 0.1% formic acid) as mobile phase A and acetonitrile as mobile phase B; the flow rate is 0.8ml per minute; the column temperature is 30 ℃; the detection wavelength is 256nm; the temperature of the sample chamber is 5 ℃; the sample volume was 10. Mu.l. Under the chromatographic conditions, the voriconazole condensate peaks for about 29 minutes and impurity D peaks for about 34 minutes.
The impurity monomer is taken in proper amount, a solution of 0.5mg/ml is prepared by a diluent, the purity of the main peak is 97.6 percent calculated by an area normalization method according to the detection method of relevant substances of voriconazole condensate. No peak was observed at 34 minutes. For further verification, the test solution was added to the voriconazole condensate sample solution as a mixed solution for HPLC measurement, and a peak was found at 34 minutes, which confirmed by a chromatogram that the voriconazole condensate sample had no target impurity peak.
TABLE 1 gradient elution procedure
After the preferred embodiments have been described in detail, those skilled in the art will readily appreciate that various changes and modifications may be made therein without departing from the spirit and scope of the present invention as defined in the appended claims. And the invention is not limited to the example embodiments illustrated in the specification.

Claims (4)

1. The synthesis method of the process impurity D generated by the voriconazole key intermediate is characterized by comprising the following steps of:
1) Reacting the initial raw materials A, N-bromosuccinimide and azodiisobutyronitrile in dichloromethane at the reaction temperature of 30-50 ℃ for 10-12 hours, quenching with sodium sulfite aqueous solution, extracting, and distilling to obtain an intermediate B; the starting material a: the molar ratio of N-bromosuccinimide is 1:1.0 to 1.5;
reacting the intermediate B obtained in the step 1) with the initial raw material C, zinc powder and iodine in tetrahydrofuran solvent, quenching with glacial acetic acid, extracting, regulating alkali, and performing column chromatography to obtain a compound D; the starting material C: the ratio of zinc powder is 1: 1-5.5;
2. a process for the synthesis of process impurities derived from key intermediates of voriconazole according to claim 1, wherein step 1) is performed starting material a: the ratio of N-bromosuccinimide is 1:1.2.
3. the method for synthesizing process impurities generated by key intermediates of voriconazole according to claim 1, wherein the reaction temperature in step 1) is 35 ℃ for 10 hours.
4. A process for the synthesis of process impurities derived from key intermediates of voriconazole according to claim 1, wherein step 2) is performed starting material C: the ratio of zinc powder is 1:1- -2.5.
CN202310757349.9A 2023-06-26 2023-06-26 Synthesis method of process impurities generated by voriconazole key intermediate Pending CN116751188A (en)

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