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.