CN112094311B - Process for preparing dexamethasone sodium phosphate by one-step method - Google Patents

Process for preparing dexamethasone sodium phosphate by one-step method Download PDF

Info

Publication number
CN112094311B
CN112094311B CN202011112167.9A CN202011112167A CN112094311B CN 112094311 B CN112094311 B CN 112094311B CN 202011112167 A CN202011112167 A CN 202011112167A CN 112094311 B CN112094311 B CN 112094311B
Authority
CN
China
Prior art keywords
dexamethasone
sodium phosphate
hydrolysis
phase
sodium hydroxide
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
CN202011112167.9A
Other languages
Chinese (zh)
Other versions
CN112094311A (en
Inventor
王培文
刘伟
李娜
蒲飞飞
张恒
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.)
Xi'an Guokang Ruijin Pharmaceutical Co ltd
Original Assignee
Xi'an Guokang Ruijin Pharmaceutical 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 Xi'an Guokang Ruijin Pharmaceutical Co ltd filed Critical Xi'an Guokang Ruijin Pharmaceutical Co ltd
Priority to CN202011112167.9A priority Critical patent/CN112094311B/en
Publication of CN112094311A publication Critical patent/CN112094311A/en
Application granted granted Critical
Publication of CN112094311B publication Critical patent/CN112094311B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07JSTEROIDS
    • C07J51/00Normal steroids with unmodified cyclopenta(a)hydrophenanthrene skeleton not provided for in groups C07J1/00 - C07J43/00

Abstract

The invention provides a process for producing dexamethasone sodium phosphate by a one-step method, which comprises the following steps: the method is characterized in that dexamethasone is used as a starting raw material, and the dexamethasone is subjected to (1) pyrophosphoryl chloride esterification, (2) purified water hydrolysis, (3) toluene extraction and purification, sodium hydroxide alkalization treatment, (4) activated carbon decolorization, and (5) acetone crystallization to obtain a high-purity dexamethasone sodium phosphate product with high yield.

Description

Process for preparing dexamethasone sodium phosphate by one-step method
Technical Field
The invention relates to the technical field of medicines, and particularly relates to a preparation process for producing dexamethasone sodium phosphate by a one-step method.
Background
Dexamethasone sodium phosphate is called as fluorometholone sodium phosphate, has the chemical name of 1, 4-pregnadiene-9 alpha-fluoro-16 alpha-methyl-11 beta, 17 alpha, 21-triol-3, 20-diketone-21-phosphate disodium salt, belongs to adrenocortical hormone medicines, and is widely applied to the fields of anti-inflammation, antianaphylaxis, rheumatism resistance, immunosuppression and the like.
In the dexamethasone sodium phosphate product on the market at present, the production process must pass through a dexamethasone phosphate intermediate, CN104744543A and CN101397320A, and research on the synthesis process of dexamethasone sodium phosphate (periu) in the academic paper is to alkalize and acidify the dexamethasone phosphate and then alkalize the dexamethasone phosphate again to obtain a refined dexamethasone sodium phosphate product. In view of the situation, the dexamethasone phosphate intermediate liquid is directly subjected to extraction, alkalization sodium conversion and crystallization through technological innovation to obtain the product, and the batch production result shows that the product quality is stable, the process time is shortened, the use of equipment and a solvent is reduced, the production cost is greatly reduced, and the method has a good industrial application prospect.
Disclosure of Invention
The invention aims to provide a process for preparing dexamethasone sodium phosphate by a dexamethasone one-step method, the product obtained by the process has high yield, high purity and stable quality, the use of equipment and solvents is reduced, the method is simple and convenient, the production cost is greatly reduced, and the process is more suitable for industrial large-scale production.
The technical scheme adopted by the invention is as follows:
the method comprises the following operation steps:
esterification:
adding solvent anhydrous tetrahydrofuran into a reaction tank, adding raw material dexamethasone, cooling, dropwise adding pyrophosphoryl chloride, reacting for 1 hour, sampling and detecting dexamethasone residue (less than or equal to 1.0%, namely, the conversion rate is more than or equal to 99.0%);
(II) hydrolysis:
after the reaction liquid is detected to be qualified, adding purified water for hydrolysis;
(III) extraction and purification:
adding toluene after hydrolysis, standing for phase splitting, collecting an oil phase, dropwise adding a sodium hydroxide solution into the oil phase to adjust the pH value to 8-12, standing for phase splitting, and collecting a water phase;
(IV) decoloring:
adding activated carbon into the water phase, decoloring, and pumping the liquid into a clean area;
(V) crystallization:
after all the liquid is stirred, acetone is dripped for crystallization, crystal growth, centrifugation and drying are carried out, and dexamethasone sodium phosphate is obtained.
The reagents used in the invention are all the existing reagents, and since pyrophosphoryl chloride is decomposed into phosphoric acid and hydrochloric acid when meeting water, anhydrous tetrahydrofuran is required to be used for reducing the generation of byproducts. The method for preparing the dexamethasone sodium phosphate product has the advantages of high yield, high purity and simplicity, and is more suitable for industrial large-scale production.
The molar ratio of dexamethasone to pyrophosphoryl chloride in the step (I) is 1: 2-7, preferably 1: 3-6, more preferably 1: 4-5, most preferably 1: 5;
cooling to-50 to-60 ℃;
the reaction time of the step (I) is 1-4h, preferably 1-3h, more preferably 1-2h, and most preferably 1 h;
the volume ratio of the purified water added in the step (II) to the anhydrous tetrahydrofuran in the step (I) is 1:1-1:3, and the preferred volume ratio is 1: 2;
adding sodium hydroxide solution to adjust the pH to 8-12, preferably to 9-11, more preferably to 10, wherein the concentration of the added sodium hydroxide is 10% -40%;
the volume ratio of the toluene added in the step (III) to the purified water added in the step (II) is 0.5-4:1, preferably 1-3:1, and more preferably 1.5: 1;
and (4) the volume ratio of the acetone dropwise added in the step (five) to the sodium hydroxide solution dropwise added in the step (three) is 3:1, preferably 2:1, and most preferably 1: 1.
Detailed Description
The invention is further described below by way of examples, which are not intended to limit the present invention further. It will be understood by those skilled in the art that equivalent substitutions and corresponding modifications of the technical features of the present invention can be made and still fall within the scope of the present invention.
Example 1
Adding 2000ml of anhydrous tetrahydrofuran into a reaction tank, adding 392g (1.0mol) of dexamethasone, stirring and dispersing, cooling to-50 ℃, dropwise adding 755g (3.0mol) of pyrophosphoryl chloride, keeping the temperature unchanged, reacting for 1h after the addition is finished, sampling and detecting that the residue of dexamethasone is less than or equal to 1.0%, adding 1000ml of purified water for hydrolysis, slowly heating to room temperature, and fully stirring. Adding 1500ml of toluene after hydrolysis, standing for phase splitting, collecting an oil phase, dropwise adding a sodium hydroxide solution into the toluene oil phase to adjust the pH value to 10, standing for phase splitting, collecting a water phase, adding activated carbon into the water phase for decoloring for 30 minutes, filtering, completely pumping the liquid into a clean area, adding acetone with the same volume as that of the sodium hydroxide solution for crystallization, growing crystals, centrifuging, and drying to obtain 415g of dexamethasone sodium phosphate, wherein the yield is 80.4%, the purity is 99.0%, and the MP: 232 ℃ and 235 ℃.
Example 2
Adding 2000ml of anhydrous tetrahydrofuran into a reaction tank, adding 392g (1.0mol) of dexamethasone, stirring and dispersing, cooling to-50 ℃, dropwise adding 1007g (4.0mol) of pyrophosphoryl chloride, keeping the temperature unchanged, reacting for 1h after the addition is finished, sampling and detecting that the residue of dexamethasone is less than or equal to 1.0%, adding 1000ml of purified water for hydrolysis, slowly heating to room temperature, and fully stirring. Adding 1500ml of toluene after hydrolysis, standing for phase splitting, collecting an oil phase, dropwise adding a sodium hydroxide solution into the toluene oil phase to adjust the pH value to 10, standing for phase splitting, collecting a water phase, adding activated carbon into the water phase for decoloring for 30 minutes, filtering, completely pumping the liquid into a clean area, adding acetone with the same volume as that of the sodium hydroxide solution for crystallization, growing crystals, centrifuging and drying to obtain 445g of dexamethasone sodium phosphate, wherein the yield is 86.2%, the purity is 99.2%, and the MP: 232 ℃ and 235 ℃.
Example 3
Adding 2000ml of anhydrous tetrahydrofuran into a reaction tank, adding 392g (1.0mol) of dexamethasone, stirring and dispersing, cooling to-50 ℃, dropwise adding 1259g (5.0mol) of pyrophosphoryl chloride, keeping the temperature unchanged, reacting for 1h after the addition is finished, sampling and detecting that the dexamethasone residue is less than or equal to 1.0%, adding 1000ml of purified water for hydrolysis, slowly heating to room temperature, and fully stirring. Adding 1500ml of toluene after hydrolysis, standing for phase splitting, collecting an oil phase, dropwise adding a sodium hydroxide solution into the toluene oil phase to adjust the pH value to 10, standing for phase splitting, collecting a water phase, adding activated carbon into the water phase for decoloring for 30 minutes, filtering, completely pumping the liquid into a clean area, adding acetone with the same volume as that of the sodium hydroxide solution for crystallization, growing crystals, centrifuging and drying to obtain 482g of dexamethasone sodium phosphate, wherein the yield is 93.4%, the purity is 99.5%, and the MP: 233-.
Examples 5-10 the experiment of example 3 was repeated with the following equal volumes of solvent in place of toluene:
Figure BDA0002728955320000041
examples 5-10 the experiment of example 3 was repeated with equal volumes of solvent replacing toluene, but the product yield was lower when methylene chloride and xylene solvents were used, the product yield and purity were lower when ethyl acetate, petroleum ether and acetone solvents were used, and the separation was not possible by miscibility when ethanol was used as the solvent, as can be seen from the experimental results: in the technology for preparing dexamethasone sodium phosphate by a dexamethasone one-step method, only a toluene solvent can obtain a high-purity product with high yield.
Examples 11-15 the experiment of example 3 was repeated with varying amounts of toluene:
examples Toluene (ml) Yield of Purity of
11 500 81.7% 99.6%
12 1000 90.8% 99.4%
13 2000 93.9% 98.2%
14 2500 94.5% 98.0%
15 3000 95.9% 96.2%
Examples 11-15 the experiment of example 3 was repeated with the amount of toluene varied, and the yield was lower when the amount of toluene was 500ml, although the purity of the product was higher, and the yield and purity of the dexamethasone sodium phosphate product were higher when the amount of toluene was between 1000 and 3000ml, i.e. the volume ratio of toluene to purified water was 1-3:1, to achieve satisfactory results.
It will be apparent to those skilled in the art that various changes and modifications may be made in the present invention without departing from the spirit and scope of the invention. Thus, if such modifications and variations of the present invention fall within the scope of the claims of the present invention and their equivalents, the present invention is also intended to include such modifications and variations.

Claims (1)

1. The process for preparing dexamethasone sodium phosphate by using the one-step method is characterized by comprising the following operation steps:
esterification:
adding solvent anhydrous tetrahydrofuran into a reaction tank, adding raw material dexamethasone, cooling, dropwise adding pyrophosphoryl chloride, reacting for 1 hour, sampling and detecting that dexamethasone residue is less than or equal to 1.0 percent, namely the conversion rate is more than or equal to 99.0 percent;
(II) hydrolysis:
after the reaction liquid is detected to be qualified, adding purified water for hydrolysis;
(III) extraction and purification:
adding toluene after hydrolysis, standing for phase separation, collecting oil phase, adding sodium hydroxide solution dropwise into the oil phase to adjust pH to 10,
standing for phase separation, and collecting a water phase;
(IV) decoloring:
adding activated carbon into the water phase, decoloring, and pumping the liquid into a clean area;
(V) crystallization:
after all the liquid is stirred, dropwise adding acetone for crystallization, growing crystals, centrifuging and drying to obtain dexamethasone sodium phosphate;
wherein, the molar ratio of the dexamethasone and the pyrophosphoryl chloride in the step (I) is 1: 5, cooling to-50 to-60 ℃;
the volume ratio of the purified water added in the step (II) to the anhydrous tetrahydrofuran in the step (I) is 1: 2;
the concentration of the sodium hydroxide added in the step (III) is 10-40%, and the volume ratio of the toluene added in the step (III) to the purified water added in the step (II) is 1.5: 1;
the volume ratio of the acetone dripped in the step (five) to the sodium hydroxide solution dripped in the step (three) is 1:1,
the dexamethasone phosphate intermediate liquid is directly subjected to extraction, alkalization sodium conversion and crystallization to obtain the product, so that the use of equipment and a solvent is reduced, and the method is suitable for industrial large-scale production.
CN202011112167.9A 2020-10-16 2020-10-16 Process for preparing dexamethasone sodium phosphate by one-step method Active CN112094311B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011112167.9A CN112094311B (en) 2020-10-16 2020-10-16 Process for preparing dexamethasone sodium phosphate by one-step method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011112167.9A CN112094311B (en) 2020-10-16 2020-10-16 Process for preparing dexamethasone sodium phosphate by one-step method

Publications (2)

Publication Number Publication Date
CN112094311A CN112094311A (en) 2020-12-18
CN112094311B true CN112094311B (en) 2022-04-08

Family

ID=73784997

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011112167.9A Active CN112094311B (en) 2020-10-16 2020-10-16 Process for preparing dexamethasone sodium phosphate by one-step method

Country Status (1)

Country Link
CN (1) CN112094311B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115057904B (en) * 2022-07-11 2023-06-27 西安国康瑞金制药有限公司 Production process and production device of betamethasone
CN115178213B (en) * 2022-07-11 2023-06-27 西安国康瑞金制药有限公司 Preparation system and preparation process of dexamethasone sodium phosphate
CN115974958B (en) * 2023-01-17 2024-04-26 江苏联环药业股份有限公司 Method for improving clarity of dexamethasone sodium phosphate

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1706961A (en) * 2004-06-07 2005-12-14 西安益尔高科技股份有限公司 Dexamethasone hormone medicine intermediate and its prepn process
CN101397320A (en) * 2007-09-29 2009-04-01 天津天药药业股份有限公司 Method for preparing dexamethasone and series products thereof
CN101397319A (en) * 2007-09-29 2009-04-01 天津天药药业股份有限公司 Method for preparing betamethasone and series products thereof
CN103936809A (en) * 2014-04-03 2014-07-23 上海新华联制药有限公司 Improved preparation method of dexamethasone sodium phosphate intermediate
CN104744543A (en) * 2013-12-26 2015-07-01 重庆华邦制药有限公司 Preparation method of pregnenolone phosphate derivatives and their salts
CN105326787A (en) * 2015-11-10 2016-02-17 成都中牧生物药业有限公司 Technology for preparing dexamethasone sodium phosphate injection
CN109734766A (en) * 2019-01-07 2019-05-10 河南利华制药有限公司 A kind of preparation method of Inflamase intermediate
CN109988212A (en) * 2019-04-22 2019-07-09 河南利华制药有限公司 A kind of Inflamase production method
CN110964075A (en) * 2018-09-30 2020-04-07 天津药业研究院有限公司 Preparation method of betamethasone phosphate and sodium salt thereof

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1706961A (en) * 2004-06-07 2005-12-14 西安益尔高科技股份有限公司 Dexamethasone hormone medicine intermediate and its prepn process
CN101397320A (en) * 2007-09-29 2009-04-01 天津天药药业股份有限公司 Method for preparing dexamethasone and series products thereof
CN101397319A (en) * 2007-09-29 2009-04-01 天津天药药业股份有限公司 Method for preparing betamethasone and series products thereof
CN104744543A (en) * 2013-12-26 2015-07-01 重庆华邦制药有限公司 Preparation method of pregnenolone phosphate derivatives and their salts
CN103936809A (en) * 2014-04-03 2014-07-23 上海新华联制药有限公司 Improved preparation method of dexamethasone sodium phosphate intermediate
CN105326787A (en) * 2015-11-10 2016-02-17 成都中牧生物药业有限公司 Technology for preparing dexamethasone sodium phosphate injection
CN110964075A (en) * 2018-09-30 2020-04-07 天津药业研究院有限公司 Preparation method of betamethasone phosphate and sodium salt thereof
CN109734766A (en) * 2019-01-07 2019-05-10 河南利华制药有限公司 A kind of preparation method of Inflamase intermediate
CN109988212A (en) * 2019-04-22 2019-07-09 河南利华制药有限公司 A kind of Inflamase production method

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
周遂.地塞米松磷酸钠的合成工艺研究.《中国优秀博硕士学位论文全文数据库(硕士) 工程科技Ⅰ辑》.2012,(第07期),第B016-552页. *
地塞米松磷酸钠的合成工艺研究;周遂;《中国优秀博硕士学位论文全文数据库(硕士) 工程科技Ⅰ辑》;20120715(第07期);第B016-552页 *

Also Published As

Publication number Publication date
CN112094311A (en) 2020-12-18

Similar Documents

Publication Publication Date Title
CN112094311B (en) Process for preparing dexamethasone sodium phosphate by one-step method
JP4892915B2 (en) Epalrestat manufacturing method
CN109180749B (en) Method for preparing high-purity N-acetylneuraminic acid hydrate by using supersaturation crystallization method
CN101942001B (en) Purification method of loteprednol etabonate
CN109096129B (en) Preparation method of L-carnitine tartrate
CN109988183B (en) Environment-friendly preparation method of cefuroxime acid intermediate
CN1623987A (en) Novel processes for preparing torsemide
CN114276406B (en) Preparation method of intermediate of deoxomilpine
CN113527338B (en) Synthesis process of cefozopran hydrochloride
CN101870704A (en) Method for purifying cefotetan acid crude products
CN110606863B (en) Preparation method of N-acetylneuraminic acid dihydrate
JP4892821B2 (en) Epalrestat manufacturing method
CN106966916A (en) A kind of method that terramycin reduces tailing peak content
CN112125943A (en) Preparation method of high-purity 16 alpha-hydroxy prednisolone
CN112961197A (en) Chemical synthesis method of NMN
CN114213494B (en) Paramethosone acetate and preparation method of Paramethosone
CN106117075B (en) Novel ubenimex recrystallization method
CN108084064B (en) Novel preparation method of D- (-) -tartaric acid
CN115322239B (en) Method for recovering diketone from mandipropamid carbon loss ester mother liquor
CN111454214B (en) Synthetic method of 2-methoxy-1-pyrimidineethylamine hydrochloride
CN114957367B (en) Refining method for preparing testosterone by biological method
CN113149884B (en) Method for preparing 2, 4-dimethylpyrrole-3, 5-diformate in low-cost clean mode
CN110845354B (en) Preparation method of cilastatin sodium intermediate
CN115466217B (en) Method for recycling cyclic acid
CN114075258B (en) Preparation method of hydrocortisone

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant