CN103360278B - Method for improving olsalazine sodium quality - Google Patents

Method for improving olsalazine sodium quality Download PDF

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Publication number
CN103360278B
CN103360278B CN201310333249.XA CN201310333249A CN103360278B CN 103360278 B CN103360278 B CN 103360278B CN 201310333249 A CN201310333249 A CN 201310333249A CN 103360278 B CN103360278 B CN 103360278B
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olsalazine sodium
crude product
olsalazine
product quality
quality
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CN103360278A (en
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周艳明
骆红宇
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SHANDONG CHUANCHENG PHARMACEUTICAL Co Ltd
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Abstract

The invention belongs to the field of drug chemosynthesis and relates to a method for improving olsalazine sodium quality. The method comprises the following steps of dissolving an olsalazine sodium crude product in a certain amount of water, adding an appropriate amount of a complexing agent into the solution, carrying out heating for dissolution and crystallization, and removing heavy metal ions. The method can improve olsalazine sodium appearance and realize heavy metal ion removal.

Description

A kind of method that improves Olsalazine sodium quality
Technical field
The invention belongs to the synthetic field of pharmaceutical chemistry, be specially a kind of method that improves Olsalazine sodium quality.
Background technology
Olsalazine sodium is also Olsalazine (Olsalazine), has another name called Olsalazine, Di Botan, is by the medicine of Phar ma ci A B company of Switzerland exploitation, goes on the market first in 1989 in Denmark.Olsalazine splits into 2 molecule 5-aminosalicylic acids and acts on colonic inflammation mucous membrane under colon bacteria effect, suppress prostaglandin(PG) synthetic, the formation of inflammation-inhibiting medium leukotriene, reduce the permeability of intestines parietal cell film, alleviate intestinal mucosa oedema, therefore it has anti-inflammatory, increases immunity of organisms, reduces the effects such as inflammatory mediator generation.The clinical long term maintenance treatment that is used for the treatment of acute and chronic ulcerative colitis, clone disease, Crohn disease and alleviation thereof.This product substitutes the sulfapyridine of non-activity in sulfasalazine with activeconstituents 5-aminosalicylic acid, connect the 5-aminosalicylic acid of 2 molecules by azo bond, and with sulfasalazine comparison, curative effect improves, adverse reaction rate reduces.
Due to the feature of Olsalazine sodium self structure, be very easy in process of production the heavy metal ion in complexing raw material or conversion unit, cause Olsalazine sodium heavy metal content severe overweight, Quality Down, and do not take effective process for purification for the heavy metal wherein containing at present, cause quality product decline, and clothes for patients with after there is negative influence.
Summary of the invention
Main purpose of the present invention is to provide a kind of method that improves Olsalazine sodium quality, the method is by Olsalazine sodium crude product heating for dissolving, adopt complexing agent to carry out complexing, then filtration washing, step is simple, easy to operate, make heavy metal content drop to the following (inspection (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law of 20ppm by 1000ppm, must not cross 20/1000000ths containing heavy metal), outward appearance becomes glassy yellow from green-yellow, thereby reaches the specification of quality described in pharmacopeia.
The refining Olsalazine sodium crude product of the present invention is diazonium salt and the wintergreen oil coupling of preparing with 5-aminosalicylic acid methyl esters, and gained azo makes with sodium hydroxide hydrolysis again.
Technical scheme of the present invention:
A method that improves Olsalazine sodium quality, comprises the following steps:
(1) Olsalazine sodium crude product is heated to 80-105 DEG C, is dissolved in appropriate pure water, amount of purified water used is 5-15 times of Olsalazine sodium crude product quality;
(2) after heating for dissolving, add the complexing agent of Olsalazine sodium crude product quality 1-10%, at 80-105 DEG C of insulation 10-50min;
(3) at 80-100 DEG C, filter, cooling crystallization, filters, and by methanol wash twice, is 10% of Olsalazine sodium crude product quality at every turn, obtains glassy yellow product.
Described complexing agent is removed the heavy metal ion in Olsalazine sodium crude product, and complexing agent used is the one in nitrilotriacetic acid(NTA) sodium (NTA), disodium EDTA (EDTA), tetrasodium salt of EDTA (EDTA), diethylenetriamine pentacarboxylic acid salt (DTPA).
Described complexing agent consumption is the 2-10% of Olsalazine sodium crude product quality.
Described complexing agent disodium EDTA or tetrasodium salt of EDTA consumption are the 2-3% of Olsalazine sodium crude product quality.
Described complexing agent nitrilotriacetic acid(NTA) sodium consumption is the 7-8% of Olsalazine sodium crude product quality.
Described complexing agent diethylenetriamine pentacarboxylic acid salt consumption is the 9-10% of Olsalazine sodium crude product quality.
In step (1), pure water consumption is 8-10 times of Olsalazine sodium crude product quality.
In step (1), pure water consumption is 11 times of Olsalazine sodium crude product quality.
In step (2), soaking time is 10-15 minute.
Described step (3) is to filter at 80-100 DEG C, is cooled to 0-5 DEG C, leaves standstill insulation extremely dry by rejection filter after 24 hours, and methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn, and filtrate is reclaimed; Filter cake is dried 4~6 hours at 60~65 DEG C, obtains product.
Beneficial effect of the present invention is:
Refine for the heavy metal in Olsalazine sodium crude product, successful, step is simple, make Olsalazine sodium crude product heavy metal content drop to the following (inspection (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law of 20ppm by 1000ppm, must not cross 20/1000000ths containing heavy metal), outward appearance becomes glassy yellow from green-yellow, thereby reaches the specification of quality described in pharmacopeia, and concrete data are shown in detection table 1.
In a word, the present invention possesses outstanding substantive distinguishing features and significant progressive.
table 1 Olsalazine sodium is processed front and back quality examination table
embodiment
Below by specific embodiment, technical scheme of the present invention is described in detail.
Following detection method is two annex VIII H first methods of Chinese Pharmacopoeia version in 2010.
embodiment 1
In reactor, add 44kg pure water, 4.0kg Olsalazine sodium crude product, heating makes its dissolving, add Olsalazine sodium crude product quality 3% disodium EDTA, stirring is warming up to 100 DEG C, is incubated 10~15 minutes, filtered while hot, filtrate is cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn.Filtrate is reclaimed.Filter cake is dried 4~6 hours at 60~65 DEG C, the qualified product 3.80kg obtaining, yield 95%.
Before refining, heavy metal content has exceeded 1000ppm, outward appearance green-yellow, refining rear detection heavy metal is 10ppm, outward appearance glassy yellow, reach the required standard of medicine (check (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law, must not cross 20/1000000ths containing heavy metal).
embodiment 2
In reactor, add 44kg pure water, 4.0kg Olsalazine sodium crude product, heating makes its dissolving, add Olsalazine sodium crude product quality 8% NTA, stirring is warming up to 105 DEG C, is incubated 10~15 minutes, filtered while hot, filtrate is cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn.Filtrate is reclaimed.Filter cake is dried 6 hours at 60 DEG C, the qualified product 3.84kg obtaining, yield 96%.
Before refining, heavy metal content has exceeded 1000ppm, outward appearance green-yellow, refining rear heavy metal 9ppm, the outward appearance glassy yellow of detecting, reach the required standard of medicine (check (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law, must not cross 20/1000000ths containing heavy metal).
embodiment 3
In reactor, add 44kg pure water, 4.0kg Olsalazine sodium crude product, heating makes its dissolving, add Olsalazine sodium crude product quality 10% DTPA, stirring is warming up to 80 DEG C, is incubated 10~15 minutes, filtered while hot, filtrate is cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn.Filtrate is reclaimed.Filter cake is dried 4 hours at 65 DEG C, the qualified product 3.82kg obtaining, yield 95.5%.
Before refining, heavy metal content has exceeded 1000ppm, outward appearance green-yellow, refining rear heavy metal 11ppm, the outward appearance glassy yellow of detecting, reach the required standard of medicine (check (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law, must not cross 20/1000000ths containing heavy metal).
embodiment 4
In reactor, add 20kg pure water, 4.0kg Olsalazine sodium crude product, be heated to 80 DEG C and make its dissolving, add Olsalazine sodium crude product quality 9% DTPA, stirring is warming up to 100 DEG C, is incubated 50 minutes, filtered while hot, filtrate is cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn.Filtrate is reclaimed.Filter cake is dried 4 hours at 65 DEG C, the qualified product 3.70kg obtaining, yield 92.5%.
Before refining, heavy metal content has exceeded 1000ppm, outward appearance green-yellow, refining rear heavy metal 11ppm, the outward appearance glassy yellow of detecting, reach the required standard of medicine (check (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law, must not cross 20/1000000ths containing heavy metal).
embodiment 5
In reactor, add 60kg pure water, 4.0kg Olsalazine sodium crude product, be heated to 100 DEG C and make its dissolving, add Olsalazine sodium crude product quality 2% tetrasodium salt of EDTA, stirring is warming up to 103 DEG C, is incubated 10 minutes, filtered while hot, filtrate is cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn.Filtrate is reclaimed.Filter cake is dried 5 hours at 63 DEG C, the qualified product 3.68kg obtaining, yield 92.0%.
Before refining, heavy metal content has exceeded 1000ppm, outward appearance green-yellow, refining rear heavy metal 11ppm, the outward appearance glassy yellow of detecting, reach the required standard of medicine (check (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law, must not cross 20/1000000ths containing heavy metal).
embodiment 6
In reactor, add 32kg pure water, 4.0kg Olsalazine sodium crude product, be heated to 100 DEG C and make its dissolving, add Olsalazine sodium crude product quality 1% disodium EDTA, stirring is warming up to 105 DEG C, is incubated 30 minutes, filtered while hot, filtrate is cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn.Filtrate is reclaimed.Filter cake is dried 5 hours at 63 DEG C, the qualified product 3.76kg obtaining, yield 94%.
Before refining, heavy metal content has exceeded 1000ppm, outward appearance green-yellow, refining rear heavy metal 11ppm, the outward appearance glassy yellow of detecting, reach the required standard of medicine (check (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law, must not cross 20/1000000ths containing heavy metal).
embodiment 7
In reactor, add 40kg pure water, 4.0kg Olsalazine sodium crude product, be heated to 80 DEG C and make its dissolving, add Olsalazine sodium crude product quality 9% DTPA, stirring is warming up to 90 DEG C, is incubated 20 minutes, filtered while hot, filtrate is cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn.Filtrate is reclaimed.Filter cake is dried 6 hours at 60 DEG C, the qualified product 3.82kg obtaining, yield 95.5%.
Before refining, heavy metal content has exceeded 1000ppm, outward appearance green-yellow, refining rear heavy metal 11ppm, the outward appearance glassy yellow of detecting, reach the required standard of medicine (check (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law, must not cross 20/1000000ths containing heavy metal).
embodiment 8
In reactor, add 44kg pure water, 4.0kg Olsalazine sodium crude product, be heated to 90 DEG C and make its dissolving, add Olsalazine sodium crude product quality 7% NTA, stirring is warming up to 105 DEG C, is incubated 15 minutes, filtered while hot, filtrate is cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn.Filtrate is reclaimed.Filter cake is dried 4 hours at 60 DEG C, the qualified product 3.84kg obtaining, yield 96%.
Before refining, heavy metal content has exceeded 1000ppm, outward appearance green-yellow, refining rear heavy metal 11ppm, the outward appearance glassy yellow of detecting, reach the required standard of medicine (check (two annex VIII H first methods of Chinese Pharmacopoeia version in 2010) in accordance with the law, must not cross 20/1000000ths containing heavy metal).
Detailed introduction to the embodiment of the present invention above, for one of ordinary skill in the art, according to the thought of the embodiment of the present invention, all will change in specific embodiments and applications, in sum, this description should not be construed as limitation of the present invention.

Claims (5)

1. a method that improves Olsalazine sodium quality, comprises the following steps:
(1) Olsalazine sodium crude product is heated to 80-105 DEG C, is dissolved in appropriate pure water, amount of purified water used is 5-15 times of Olsalazine sodium crude product quality;
(2) after heating for dissolving, add the complexing agent of Olsalazine sodium crude product quality 1-10%, at 80-105 DEG C of insulation 10-50min; Described complexing agent is the one in nitrilotriacetic acid(NTA) sodium, diethylenetriamine pentacarboxylic acid salt; Described complexing agent nitrilotriacetic acid(NTA) sodium consumption is the 7-8% of Olsalazine sodium crude product quality; Described complexing agent diethylenetriamine pentacarboxylic acid salt consumption is the 9-10% of Olsalazine sodium crude product quality;
(3) at 80-100 DEG C, filter, cooling crystallization, filters, and by methanol wash twice, is 10% of Olsalazine sodium crude product quality at every turn, obtains glassy yellow product.
2. the method for raising Olsalazine sodium quality according to claim 1, is characterized in that, in step (1), pure water consumption is 8-10 times of Olsalazine sodium crude product quality.
3. the method for raising Olsalazine sodium quality according to claim 1, is characterized in that, in step (1), pure water consumption is 11 times of Olsalazine sodium crude product quality.
4. the method for raising Olsalazine sodium quality according to claim 1, is characterized in that, in step (2), soaking time is 10-15 minute.
5. the method for raising Olsalazine sodium quality according to claim 1, it is characterized in that, described step (3) is to filter at 80-100 DEG C, be cooled to 0-5 DEG C, leave standstill insulation extremely dry by rejection filter after 24 hours, methanol wash twice for filter cake is 10% of Olsalazine sodium crude product quality at every turn, and filtrate is reclaimed; Filter cake is dried 4~6 hours at 60~65 DEG C, obtains product.
CN201310333249.XA 2013-08-02 2013-08-02 Method for improving olsalazine sodium quality Active CN103360278B (en)

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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101786964A (en) * 2010-03-16 2010-07-28 天津力生制药股份有限公司 Improved synthetic method of Olsalazine sodium

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101786964A (en) * 2010-03-16 2010-07-28 天津力生制药股份有限公司 Improved synthetic method of Olsalazine sodium

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
超声波作用下合成奥沙拉秦;陈小全;《超声波作用下合成奥沙拉秦》;20081231;第17卷;858-860 *
郑爱玲.络合滴定法.《化学基础与分析检验》.中国计量出版社,2003,136-138. *
陈小全.超声波作用下合成奥沙拉秦.《超声波作用下合成奥沙拉秦》.2008,第17卷858-860. *

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Inventor after: Zhou Yanming

Inventor after: Luo Hongyu

Inventor before: Liu Huaizhen

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Free format text: CORRECT: INVENTOR; FROM: LIU HUAIZHEN TO: ZHOU YANMING LUO HONGYU

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Effective date of registration: 20160629

Address after: 252022 north of the Mount Lu, Liaocheng economic and Technological Development Zone, Shandong

Patentee after: SHANDONG CHUANCHENG PHARMACEUTICAL CO., LTD.

Address before: 250132, Sichuan Province, Ji'nan Shandong high tech Zone martyrs Road No. 15, Sichuan Pharmaceutical Science and Technology Development Co., Ltd.

Patentee before: Liu Huaizhen