Patent Application
20160096860
This invention relates to a preparation method for a pharmaceutical compound, specifically, a preparation method of trihydroxyethyl rutoside.
Troxerutin, also called Venoruton, is mainly composed of 7,3′,4′-trihydroxyethyl rutoside (abbreviated as “trihydroxyethyl rutoside” thereafter). The formula is C33H42O19, CAS No. is 7085-55-4, molecular weight is 742.69, and the chemical structure is as below:
Troxerutin is a kind of anticoagulant and thrombolytic drug. Generally, it can be synthesized by reacting rutin with ethylene oxide in methanol and water as medium in the presence of a basic catalyst. Currently, active pharmaceutical ingredient of troxerutin is available on the market, sold at different purities such as 60%, 80% and 88%.
Trihydroxyethyl rutoside is the active ingredient in troxerutin. The higher its content is in troxerutin, the higher the quality of the drug. However, the current technical approach for preparing troxerutin with high purity is far from ideal.
The products of troxerutin on the market include injection formulation, oral solution and capsule. Especially for injection, the non-ideal purity of troxerutin produced by current technologies may pose great risk to clinical applications. Actually, injecting such a drug may lead to high prevalence of adverse effects, particularly allergic reactions. Improving the purity of troxerutin, specifically, the purity of the active ingredient trihydroxyethyl rutoside, therefore, has been studied by a great number of researchers.
The exiting preparation method of troxerutin utilizes a one-step reaction, i.e., direct hydroxyethylation of rutin to complete the reaction. Different hydroxyethylation techniques are based on utilizing different hydroxyethylation agents, reaction media, catalysts, reaction parameters, etc. The following are examples.
1. In Patent BG2888B1, trihydroxyethyl rutoside with purity of 85.8% was prepared using water as solvent, ammonium water as catalyst, and ethylene oxide as hydroxyethylation agent.
2. In Patent CN1331697 (US6855697), trihydroxyethyl rutoside with purity of 92% was prepared by using water as solvent, alkaline metal as catalyst, and ethylene oxide as hydroxyethylation agent, and by controlling the recrystallization condition.
3. In Patent US3420815, troxerutin with chromatographic purity of 87.4%, content of 85.3% and melting point of 181-183° C. was prepared by using sodium hydroxide as catalyst.
4. In Patent CN1554353, trihydroxyethyl rutoside with content of 90% was prepared by using organic solvents (methanol and ethanol) as solvent and pyridine as catalyst.
5. In Patent CN1814613, trihydroxyethyl rutoside with content of 85% was prepared by using resin to control the pH value of the reaction solution.
One of the difficulties in preparing trihydroxyethyl rutoside is that rutin has four active hydroxyl groups, all of which can be hydroxyethylated, resulting in a mixture of products. Another difficulty is that natural rutin is mixed with impurities having highly similar structures, making purification difficult. It is challenging to obtain rutin with high purity by using conventional methods. Patent CN200810007927.2 discloses a method for purifying rutin by using complex reverse chromatography, which only gives gram-scale rutin with purity of 98%. In fact, commercially available rutin with low purity is always used as raw materials to prepare troxerutin. The impurities in the raw materials also undergo hydroxyethylation reaction, generating impurities with highly similar properties as trihydroxyethyl rutoside, and such impurities are hard to be removed. Actually, the preparation of trihydroxyethyl rutoside with high purity is highly challenging. Except for the chromatographic method of Jun Li et al. [2004, “Separation of troxerutin as reference substance by preparative liquid chromatography”, Chinese Journal of Pharmaceuticals, 35(5), 285-287] which is capable of preparing trihydroxyethyl rutoside with a purity of 99% as reference substance, no other reports of preparing trihydroxyethyl rutoside with a purity higher than 98% by using conventional methods can be found. Even though a product with a purity of 99% is claimed on the market, the preparation method is not disclosed, and the product is not available. The purity of reference substance prepared by current methods, even after multiple recrystallizations, is only 96-97%.
In order to solve the problem, this invention provides a preparation method of troxerutin with low content of impurities. Specifically, this method provides troxerutin containing less than 2% of non-troxerutin derivatives and greater than 98% of trihydroxyethyl rutoside. The essence of this invention relies on a two-step reaction to synthesize trihydroxyethyl rutoside with purification of the intermediate, whereby obtaining high-purity product.
This invention discloses a new preparation method of troxerutin, including
It was discovered that 7-monohydroxyethyl rutoside, as an intermediate for preparing troxerutin, is significantly different in properties in comparison to other impurities contained in the raw materials. Therefore, 7-monohydroxyethyl rutoside can be prepared with a purity of greater than 98%. Comparing with current technologies, this invention can use conventional purification methods, especially recrystallization method. No special expensive equipments or expensive separation chromatographic column is needed. This method thus greatly saves cost for manufacture and makes it possible for industrial production of trihydroxyethyl rutoside. Using conventional method is impossible to obtain trihydroxyethyl rutoside with high purity due to the similarities in properties between the impurities and the final product, even if recrystallization of the final product is performed repeatedly.
The synthetic approach in this invention can be illustrated as below:
The following are illustrative examples only and are not meant to limit the scope of this invention.
In the present method, the preparation of 7-monohydroxyethyl rutoside in step (1) can utilize the technology in U.S. Pat. No. 4,153,788, such as using borax to protect the hydroxyl groups at the 5, 3′, and 4′ positions. Alternatively, preparing 7-monohydroxyethyl rutoside from rutin can also employ the technology in U.S. Pat. No. 3,430,815, i.e., synthesis in organic solvents.
During the preparation, hydroxyl protecting agent is used to protect the hydroxyl groups of rutin. Then, hydroxyethylation agent is added to the solvent to perform the reaction, wherein rutin can be purchased on the market, the hydroxyl protecting agent is borax, the hydroxyethylation agent is ethylene oxide, the reaction solvent is selected from water, methanol and ethanol, the reaction temperature is 30-50° C., the reaction time is 4-12 h, the reaction solution is let stand after reaction is complete, optionally at low temperature, the solution is made acidic if necessarily, and the resulting precipitate can be used for the next step after filtration.
The purification of 7-monohydroxyethyl rutoside in step (2) can use any industrially available method such as recrystallization, wherein 7-monohydroxyethyl rutoside is purified to a purity of greater than 95%, preferably greater than 98%, most preferably greater than 99%, and the purified product is used for further reaction.
The solvent for recrystallization is selected from water, methanol, ethanol, isopropanol and a mixture thereof. The recrystallization step includes dissolution, crystallization and filtration.
The preparation of trihydroxyethyl rutoside from purified 7-monohydroxyethyl rutoside in step (3) can utilize conventional hydroxyethylation approaches such as hydroxyethylation of 7-monohydroxyethyl rutoside by using ethylene oxide as hydroxyethylation agent. After reaction, the reaction product is passed through cation exchange resin and anion exchange resin to remove salts, or through macroporous resin to remove impurities. Then step (4) is performed.
In the process, a hydroxyethylation agent is added to react with 7-monohydroxyethyl rutoside, which is dissolved or dispersed in a solvent, wherein the hydroxyethylation agent is ethylene oxide, the reaction solvent is selected from water, methanol, ethanol, pyridine, and a mixture thereof, the reaction temperature is 50-80° C., the reaction time is 3-8 hours, the solution is let stand after reaction is complete, optionally at low temperature, the solution is made acidic if necessarily, and the resulting solution can be used for the next step.
Said cation exchange resins are selected from strong acidic polystyrene cationic exchange resins such as 007X7(732), 001X12, 001X1 and 001X16, said anion exchange resins are selected from strong basic polystyrene anion exchange resins such as 201X4(711) and 201X7(717). The method of passing the product through resins can be performed as follows: passing the solution through a column of resins, or adding the resins to the reaction solution, stirring the mixture, and then separating the crude product solution.
Said macroporous resins selected from D101, D201, DAB-8 and D301 can be used for purification in conventional manners, i.e., passing the filtered aqueous solution of the reaction product through a resin column, washing the column with purified water, and further washing with organic solvents of various concentrations in a gradient manner, wherein the organic solvent is ethanol, resulting in a product solution of crude trihydroxyethyl rutoside. The solution of crude product can be subjected to recrystallization after concentration and drying.
The purification step (4) utilizes recrystallization to prepare purified trihydroxyethyl rutoside, wherein the solvent for recrystallization is selected from water, methanol, ethanol, isopropanol and a mixture thereof, and the recrystallization step includes dissolution, crystallization and filtration.
Unless otherwise indicated, all the ratios and percentages are weight percentage values, and chromatographic purity refers to the results obtained according to the troxerutin analysis method in European Pharmacopoeia 7.0. Detailed preparation examples can be found in the examples below.
The advantages of this invention include the following.
Based on known reports, preparing highly pure trihydroxyethyl rutoside with purity greater than 98% is only possible using preparative chromatographic method, which is extremely expensive, strictly restrained within laboratory research, impossible for large-scale manufacture and wide application. The method disclosed in this invention takes a simpler method to obtain trihydroxyethyl rutoside with high purity, the cost is low and feasibility is great.
In comparison with current methods, this invention will greatly decrease cost. Especially for trihydroxyethyl rutoside, the cost is significantly decreased. The relevant experimental data are as follows.
The method in U.S. Pat. No. 3,420,815: according to this method, it is impossible to obtain trihydroxyethyl rutoside with a purity of 98%. The chromatographic purity of the product is 87.4% and the content is 84.2%. The color is dark yellow. Melting point is 178-182 ° C. The cost is 400-500 Chinese Yuan per kilogram. With preparative chromatographic separation, trihydroxyethyl rutoside with a purity of 99% can be obtained. The cost, however, increases dramatically to 5,000-10,000 Chinese Yuan per gram.
In addition, the relevant data for comparison with the published preparation methods are as follows.
The method in U.S. Pat. No. 6,855,697: according to this method, it is impossible to obtain trihydroxyethyl rutoside with a purity of 98%. The chromatographic purity of the product is 92.1% and the content is 90.3%. The color is yellow. Melting point is 179-183 ° C. The cost is 500-800 Chinese Yuan per kilogram. With preparative chromatographic separation, trihydroxyethyl rutoside with a purity of 99% can be obtained. The cost, however, increases dramatically to 5,000-10,000 Chinese Yuan per gram.
This invention provides a preparation of trihydroxyethyl rutoside with purity of 98%. Its color is light yellow, melting point is 185-187° C. and the cost is around 2,000-3,000 Chinese Yuan per kilogram.
The invention provides a preparation of trihydroxyethyl rutoside with purity of 99%. Its color is light yellow, melting point is 186-188° C. and the cost is around 3,000-5,000 Chinese Yuan per kilogram.
The products after step (1) and after purification in this invention are analyzed with results as below:
According to the table above, it can be seen that the physicochemical property of 7-monohydroxyethyl rutoside is significantly different from the impurities 1-7 in the reaction. The effects of purification are significant
In order to prove the superiority of this invention, a comparison to the latest technology is also made.
Trihydroxyethyl rutoside is prepared by the method disclosed in U.S. Pat. No. 6,855,697. After reaction, the trihydroxyethyl rutoside in the reaction solution is purified by the following steps.
The solution containing trihydroxyethyl rutoside is passed through cation exchange resin 732, anion exchange resin 717 to remove salts, then concentrated under reduced pressure, and further spray-dried. With 8,000 ml of methanol added, the solid is heated to dissolve. After active charcoal for refinement of injection is added, the solution is heated at reflux for 30 min, and filtered while hot. The filtrate is let stand at room temperature for 6 h to allow crystallization. After filtration, the solid is dried at 40-50° C. and trihydroxyethyl rutoside is finally obtained, in which the content of trihydroxyethyl rutoside is tested to be 88.2%. The obtained solid was recrystallized from a 20-fold amount of methanol, and dried. The content of trihydroxyethyl rutoside is 90.6%.
The solution containing trihydroxyethyl rutoside is passed through cation exchange resin 732, anion exchange resin 711 to remove salts, then concentrated under reduced pressure, and further spray-dried. With 7,000 ml of methanol-water (37:3) added, the solid is heated to dissolve. After active charcoal for refinement of injection is added, the solution is heated at reflux for 30 min, and filtered while hot. The filtrate is let stand at room temperature for 6 h to allow crystallization. After filtration, the solid is dried at 40-50 ° C. and trihydroxyethyl rutoside is finally obtained, in which the content of trihydroxyethyl rutoside is tested to be 90.1%. The obtained solid was recrystallized from a 20-fold amount of methanol-water (37:3), and dried. The content of trihydroxyethyl rutoside is 91.6%.
The solution containing trihydroxyethyl rutoside is passed through cation exchange resin 001X14, anion exchange resin 717 to remove salts, then concentrated under reduced pressure, and further spray-dried. With 9000 ml of methanol-isopropanol (95:5) added, the solid is heated to dissolve. After active charcoal for refinement of injection is added, the solution is heated at reflux for 30 min, and filtered while hot. The filtrate is let stand at room temperature for 6 h to allow crystallization. After filtration, the solid is dried at 40-50° C. and trihydroxyethyl rutoside is finally obtained, in which the content of trihydroxyethyl rutoside is tested to be 91.7%. The obtained solid was recrystallized from a 20-fold amount of methanol-isopropanol (95:5), and dried. The content of trihydroxyethyl rutoside is 92.4%.
Trihydroxyethyl rutoside is prepared by the method disclosed in this invention. After reaction, the trihydroxyethyl rutoside in the reaction solution is purified by the following steps.
The solution containing trihydroxyethyl rutoside is passed through cation exchange resin 732, anion exchange resin 717 to remove salts, then concentrated under reduced pressure, and further spray-dried. With 8,000 ml methanol added, the solid is heated to dissolve. After active charcoal for refinement of injection is added and the solution is heated at reflux for 30 min, filtered while hot. The filtrate is then precipitated at room temperature for 6 h. After filtration, the solid is dried at 40-50° C., and trihydroxyethyl rutoside is finally obtained, in which the content of trihydroxyethyl rutoside is tested to be 92.4%. The obtained solid was recrystallized from a 20-fold amount of methanol, and dried. The content of trihydroxyethyl rutoside is 98.2%.
The solution containing trihydroxyethyl rutoside is passed through cation exchange resin 732, anion exchange resin 711 to remove salts, then concentrated under reduced pressure, and further spray-dried. With 7,000 ml methanol-water (37:3) added, the solid is heated to dissolve. After active charcoal for refinement of injection is added and the solution is heated at reflux for 30 min, filtered while hot. The filtrate is then precipitated at room temperature for 6 h. After filtration, the solid is dried at 40-50° C. and trihydroxyethyl rutoside is finally obtained, in which the content of trihydroxyethyl rutoside is tested to be 93.5%. The obtained solid was recrystallized from a 20-fold amount of methanol-water (37:3), refined and dried. The content of trihydroxyethyl rutoside is 98.3%.
The solution containing trihydroxyethyl rutoside is passed through cation exchange resin 001X14, anion exchange resin 717 to remove salts, then concentrated under reduced pressure, and further spray-dried. After 9,000 ml methanol-isopropanol (95:5) added, the solid is heated to dissolve. After active charcoal for refinement of injection is added, the solution is heated at reflux for 30 min, and filtered while hot. The filtrate is then precipitated at room temperature for 6 h. After filtration, the solid is dried at 40-50° C. and trihydroxyethyl rutoside is finally obtained, in which the content of trihydroxyethyl rutoside is tested to be 95.8%. The obtained solid was recrystallized from a 20-fold amount of methanol-isopropanol (95:5), and dried. The content of trihydroxyethyl rutoside is 98.6%.
It can be seen from the comparison above that through the same purification method, the present preparation method gave much better result.
Based on existing technology such as the method in U.S. Pat. No. 6,855,697, the purity of trihydroxyethyl rutoside is 91.3%. Much purer product could not be obtained even by repeated recrystallization from a 20˜25-fold amount of methanol-isopropanol (95:51. as shown below:
1. 328 g (0.86 mol) Borax (Na2B4O7.10H2O) is added into 2,500 ml deionized water, and dissolve with stirring. 605 g (0.82 mol) rutin is added and dissolve with stirring at 40-45° C. Clear and transparent solution of rutin-borax complex is obtained. Under 40-45° C., with stirring, 88 g (2.0 mol) ethylene oxide is gradually introduced into the reaction solution followed by a reaction for about 6 h. The reaction is complete based on
HPLC analysis. The pH value of the solution is adjusted to 2.0 by using 5N HCl and further let stand for 12 h at 3-5° C. After filtration, the solid cake is obtained, in which contains 504 g 7-monohydroxyethyl rutoside and the yield is 95%.
2. 1,460 g 7-monohydroxyethyl rutoside obtained from 1 above is added into 4,750 ml deionized water and heated to 60° C. with stirring. When full dissolution reached, the solution is filtrated and the filtrate stands at 3-5° C. for overnight. The predicated solid is obtained by filtration and further dried at 40-50° C. for 12 h. 450g 7-monohydroxyethyl rutoside is obtained. The content by anhydrous count is 98.3%. The chromatographic purity is 98.6%. The yield is 89.3% and the total yield is 84.8%.
3. 490 g (0.7mol) 7-monohydroxyethyl rutoside obtained from 2 above and 5.6 g sodium hydroxide are added into 1,880 ml deionized water, heated to and kept at 75-80° C. with stirring. 92 g (2.1 mol) ethylene oxide is gradually introduced into the reaction solution followed by a reaction reacting for 5-6 h. When the fraction of trihydroxyethyl rutoside reaches 75%-78% based on HPLC analysis, the supply of ethylene oxide is stopped. At the same time, nitrogen is introduced into the reaction and the temperature is rapidly lowered down. When the temperature is lower than 40° C., the pH value is adjusted to 5.0±0.2 by using 3N HCl. The reaction solution is respectively passing through cation exchange resin column 732 and anion exchange resin column 717, followed by concentration under reduced pressure, and spray-dried. Solid powder of 520 g is obtained. The content of trihydroxyethyl rutoside is 92.3%. The melting point is 180-183° C. The yield is 98% and the total yield is 83.1%.
4. 500 g solid powder as obtained from 3 above is added into 10,000 ml methanol. After an addition of 1.0 g active charcoal for refinement of injection, the solution is heated at reflux for 30 min, and filtered while hot. After a natural crystallization of filtrate at room temperature for 6 h, the solid is obtained by filtration and further dried at 40-50° C. 410 g of trihydroxyethyl rutoside is obtained. The content is 96.8%. The yield is 82% and the total yield is 68.1%.
5. 410 g of the solid powder obtained from 4 above is added into 9,500 ml methanol. The solid is heated for dissolve. The solution is heated at reflux for 30 min and filtrated while hot. The filtrate gets through a natural precipitation of crystal at room temperature for 6 h. The solid is obtained after filtration and further dried at 40-50° C. under vacuum. 338 g of trihydroxyethyl rutoside is finally obtained. The content is 98.2%. The chromatographic purity is 98.4%. The melting point is 184-186° C. The yield is 82.5% and the total yield is 56%.
1. 164 g (0.43 mol) Borax (Na2B4O7.10H2O) and 12 g (0.3 mol) sodium hydroxide are added into 2,000 ml deionized water, and dissolve with stirring. With an addition of 605 g (0.82 mol) rutin, the solution is heated to and kept at 40-45° C. On the condition of stirring, 88 g (2.0 mol) ethylene oxide is gradually introduced into the reaction solution followed by a reaction for about 12 h. The reaction is complete based on HPLC analysis. The pH value of the solution is adjusted to 2.0 by using 5N HCl and further let stand for 12 h at 3-5° C. After filtration, the solid cake is obtained, in which contains 510 g of 7-mono hydroxyethyl rutoside and the yield is 96%.
2. 510 g 7-monohydroxyethyl rutoside obtained from 1 above (total weight is 1,450 g containing 940 g water) is added into 2,000 ml deionized water and heated to 40 ° C. under stirring. Saturated sodium bicarbonate solution is dropwise added until solid is fully dissolved. The solution is filtrated and the pH value of the filtrate is adjusted to 4.0 by using 0.1 N HCl. The filtrate is let stand at 3-5° C. for overnight. The solid is obtained by filtration and further dried at 40-50° C. for 12h. 433 g 7-monohydroxyethyl rutoside (total weight 470 g) is obtained. The content by anhydrous count is 98.6%. The chromatographic purity is 98.8%. The yield is 85% and the total yield is 81.6%.
3. 433 g (0.67mo1) 7-monohydroxyethyl rutoside obtained from 2 above and 5.6 g ammonium water are added into 1,880 ml deionized water, heated to and kept at 75-80° C. with stirring. 92 g (2.1 mol) ethylene oxide is gradually introduced into the reaction solution followed by a reaction for 5-6 h. When the fraction of trihydroxyethyl rutoside reaches 75-78% based on HPLC analysis, the supply of ethylene oxide is stopped. At the same time, nitrogen is introduced into the reaction and the temperature is rapidly lowered down. When the temperature is lower than 40° C., the reaction solution is directly loaded onto the pre-treated macroporous resin D101 for purification, in which a total weight of 20 kg resin is used. When the loading is finished, deionized water is used for washing until the eluent is neutral and the chloride detection by silver nitrate is negative. Then 60% ethanol is used for washing until the eluent is colorless. Eluent is collected and concentrated to 2500 ml under reduced pressure. 465 g solid powder is obtained after spray drying. The content of trihydroxyethyl rutoside is 92%. The yield is 86% and the total yield is 70.2%
4. 465 g solid powder as obtained from 3 above is added into 8000 ml methanol and heated to dissolve. After an addition of 1.0 g active charcoal for refinement of injection and a refluxed for 30 min, the solution is filtered while hot. After crystal precipitation of filtrate at room temperature for 6 h, the solid is obtained by filtration and further drying at 40-50° C. The content is 97.2%. The yield is 82% and the total yield is 57.6%.
5. 381 g of the solid powder obtained from 4 above is added into 10500 ml methanol, and heated for dissolve. The solution is heated at reflux for 30 min and filtered while hot. The filtrate is let stand for a natural precipitation of crystal at room temperature for 6 h. The solid is obtained after filtration and further dried at 40-50° C. under vacuum. 314 g of trihydroxyethyl rutoside is finally obtained. The content is 98.3%. The chromatographic purity is 98.3%. The melting point is 184-186° C. The yield is 82.5% and the total yield is 47.5%.
1. 328 g (0.86 mol) Borax (Na2B4O7.10H2O) is added into 2,000 ml deionized water, and dissolve with stirring. 605g (0.82 mol) rutin is added and dissolved at 40-45° C. with stirring. Clear and transparent solution of rutin-borax complex is obtained. 88 g (2.0 mol) ethylene oxide is gradually introduced into reaction solution. After a reaction for about 12 h, the reaction is complete based on HPLC analysis. The reaction solution is directly loaded onto the pre-treated macroporous resin D101 for purification, in which a total weight of 25 kg resin is used. When the loading is finished, deionized water is used for washing until the eluent is neutral. The column is firstly washed by 10% ethanol, further washed by 10,000 ml 60% ethanol and finally washed by 90% ethanol. The eluent from 60% ethanol washing is collected and concentrated under reduced pressure until no smell of alcohol. The solution is diluted with water to a volume of 12,000 ml and stands at 3-5° C. for overnight. After filtration, the solid cake is further washed by icy water. 473 g trihydroxyethyl rutoside (total weight of 1,440 g) is obtained. The content by anhydrous count is 99.3%.The chromatographic purity is 99.3%. The yield is 89.3%.
2. 1,440 g solid containing water obtained from 1 above is added into 4,750 ml deionized water and heated to 60° C. under stirring. After full dissolution, the solution is filtered. Then, the solution is filtered and the pH value of the filtrate is adjusted to 2.0 by using 3N HCl. The filtrate is let stand at 3-5° C. for overnight. The solid is obtained by filtration and further dried at 40-50° C. for 12h. 463 g of 7-monohydroxyethyl rutoside (containing 8% water) is obtained. The content by anhydrous count is 99.5%. The chromatographic purity is 99.5%. The yield is 90.1% and the total yield is 80.5%.
3. 463 g (0.71 mol) 7-monohydroxyethyl rutoside obtained from 2 above and 5.6 g sodium hydroxide are added into 1,880 ml deionized water, heated to and kept at 75-80° C. with stirring. 92 g (2.1 mol) ethylene oxide is gradually introduced into the reaction solution followed by a reaction for 5-6 h. When the fraction of trihydroxyethyl rutoside based on HPLC analysis reaches 75%-78%, the supply of ethylene oxide is stopped. At the same time, nitrogen is introduced into the reaction and the temperature is rapidly lowered down. When the temperature is lower than 40° C., the pH value is adjusted to 5.0±0.2 by using 3N HCl. The reaction solution is respectively passed through cation exchange resin column 732 and anion exchange resin column 717 to remove salts, followed by concentration under reduced pressure, and spray-dried. Solid powder of 531 g is obtained. The content of trihydroxyethyl rutoside is 85%. The melting point is 180-183° C. The yield is 85% and the total yield is 68.4%.
4. 465 g solid powder as obtained from 3 above is added into 8,000 ml methanol and heated to dissolve. After an addition of 1.0 g active charcoal for refinement of injection, the solution is heated at reflux for 30 min, and filtered while hot. After a natural precipitation of crystal precipitation at room temperature for 6 h, the solid is obtained by filtration and further drying at 40-50° C. 531 g of trihydroxyethyl rutoside is obtained. The content is 95.8%. The yield is 82% and the total yield is 56%.
5. 435 g of the solid powder obtained from 4 above is added into 10,500 ml methanol, and heated to dissolve. The solution is heated at reflux for 30 min, and filtrated while hot. After a natural crystal precipitation at room temperature for 6 h, the solid is obtained after filtration and further dried at 40-50 ° C. under vacuum. Finally, 354 g trihydroxyethyl rutoside is obtained. The content is 98.4%. The chromatographic purity is 98.4%. The melting point is 184-186° C. The yield is 81.5% and the total yield is 45.6%.
1. The preparation of 7-monohydroxyethyl rutoside is the same as descried in EXAMPLE 1.
2. 510 g (0.71 mol) 7-monohydroxyethyl rutoside obtained from 1 above and 5.6 g sodium hydroxide are added into the mixture solution of 1,000 ml deionized water and 800 ml ethanol. The solution is heated to and kept at 70-75° C. under stirring. 92 g (2.1 mol) ethylene oxide is gradually introduced into reaction solution followed by a reaction for 10-13 h. When the fraction of trihydroxyethyl rutoside reaches 75-78% based on HPLC analysis, the supply of ethylene oxide is stopped. At the same time, nitrogen is introduced into the reaction and the temperature is rapidly lowered down. When the temperature is lower than 40° C., the pH value is adjusted to 5.0±0.2 by using 3N HCl. The ethanol is recycled by vacuum distillation. The reaction solution is respectively passed through cation exchange resin column 732 and anion exchange resin column 717 to remove salts, followed by spray drying. Solid powder of 480 g is obtained. The content of trihydroxyethyl rutoside is 93.4%. The melting point is 181-184° C. The yield is 85%.
3. The obtained solid from 2 above was recrystallized according to the method in EXAMPLE 1 by using methanol. 323 g of trihydroxyethyl rutoside is obtained. The chromatographic purity is 98.6%. The melting point is 185-186° C. The total yield is 53.5%.
1. The preparation of 7-monohydroxyethyl rutoside is the same as descried in EXAMPLE 1.
2. 510 g (0.71 mol) 7-monohydroxyethyl rutoside and 5.6 g sodium hydroxide are added into the mixture solution of 1,000 ml deionized water and 800 ml methanol.
The solution heated to and kept at 60-70° C. under stirring. 92 g (2.1 mol) ethylene oxide is gradually introduced into reaction solution followed by a reaction for 10-13 h. When the fraction of trihydroxyethyl rutoside reaches 75-78% based on HPLC analysis, the supply of ethylene oxide is stopped. At the same time, nitrogen is introduced into the reaction and the temperature is rapidly lowered down. When the temperature is lower than 40° C., the pH value is adjusted to 5.0±0.2 by using 3N HCl. The reaction solution is respectively passed through cation exchange resin column 732 and anion exchange resin column 717 to remove salts. The methanol is recycled by vacuum distillation. 474 g of solid powder of is obtained after spray drying. The content of trihydroxyethyl rutoside is 94.5%. The melting point is 181-184° C. The yield is 84%.
3. The solid as obtained from 2 above was recrystallized according to the method 1 in EXAMPLE 2 by using methanol. 317 g of trihydroxyethyl rutoside is obtained. The chromatographic purity is 98.7%. The melting point is 185-186° C. The total yield is 52.5%
1. The preparation of 7-monohydroxyethyl rutoside is the same as descried in EXAMPLE 1.
2. Within a 5,000 ml autoclave, 510 g (0.71 mol) 7-monohydroxyethyl rutoside, 10 ml trimethylamine, 2,000 ml methanol, and 132 g (3.0 mol) ethylene oxide at last are added. Once the addition is finished, the autoclave is sealed immediately and heated to and kept at 75-80° C. under stirring followed by a reaction for 2-3h. When the temperature is lower than 40° C. and the pressure is released, the reaction solution is filtrated. The filtrated solution is respectively passed through the cation exchange resin 732 column and the anion exchange resin 717 column. The pH value of the solution is adjusted to 5.0±0.2 by using 5N HCl. The filtrate is let stand for 6-8 h at room temperature. Crystal is obtained after filtration and the solid cake of 380 g is obtained.
3. The solid cake obtained from 2 above is re-dissolved in a 20-fold amount of hot methanol. The solution is heated at flux for 30 min and filtered. The filtrate is let stand for 6-8 h at room temperature. After filtration, the crystal is dried under vacuum at 40-50° C. The content of trihydroxyethyl rutoside is 98.1%. The melting point is 185-186° C. The yield is 58%.
1. The preparation of 7-monohydroxyethyl rutoside is the same as descried in EXAMPLE 1.
2. Within a 5,000 ml autoclave, 510 g (0.71 mol) 7-monohydroxyethyl rutoside, 10 ml diethylamine, 2,000 ml methanol, and 132 g (3.0 mol) ethylene oxide as the last are added. Once the addition is finished, the autoclave is sealed immediately and heated to and kept at 75-80° C. under stirring followed by a reaction for 2-3h. When the temperature is lower than 40° C. and the pressure is released, the reaction solution is filtered. The filtrate is respectively passed through the cation exchange resin 732 column and the anion exchange resin 717 column. The pH value of the solution is adjusted to 5.0±0.2 by using 5N HCl. The filtrate is let stand for 6-8 h at room temperature. Crystal is obtained after filtration and a solid cake of 375 g is obtained.
3. The solid cake obtained from 2 above is re-dissolved in a 20-fold amount of hot methanol-isopropanol (37:3). The solution is heated at reflux for 30 min, and filtered. The filtrate is let stand for 6-8 h at room temperature. Crystal is obtained after filtration followed by vacuum drying at 40-50° C. A solid powder of 302 g is obtained. The content of trihydroxyethyl rutoside is 98.3%. The melting point is 184-186° C. The yield is 57%.
1. The preparation of 7-monohydroxyethyl rutoside is the same as descried in EXAMPLE 1.
2. Within a 5,000 ml autoclave, 510 g (0.71 mol) 7-monohydroxyethyl rutoside, 30 ml ammonium water, 2,000 ml methanol, and 154 g (3.5 mol) ethylene oxide are added. Once the addition is finished, the autoclave is sealed immediately and heated to and kept at 75-80° C. with stirring followed by a reaction for 2-3 h. When the temperature is lower than 40° C. and the pressure is released, the reaction solution can be filtered.
The filtrated solution respectively passes through the cation exchange resin 732 column and the anion exchange resin 717 column. The pH value of the solution is adjusted to 5.0±0.2 by using 5N HCl. The filtrate is let stand for 6-8 h at room temperature. Crystal is obtained after filtration and 360 g of solid cake is obtained.
3. The solid cake obtained from 2 above is re-dissolved in a 20-fold amount of hot methanol. The solution is heated at reflux for 30 min and is filtrated. The filtrate is let stand for 6-8 h at room temperature. Crystal is obtained after filtration followed by vacuum drying at 40-50° C. 290 g of solid powder is obtained. The content of trihydroxyethyl rutoside is 98.2%. The melting point is 184-186° C. The yield is 55%.
1. The preparation of 7-monohydroxyethyl rutoside is the same as descried in EXAMPLE 1.
2. Within a 5,000 ml autoclave, 510 g (0.71 mol) 7-monohydroxyethyl rutoside, 10 ml pyridine, 1,600 ml methanol, 400 ml methanol and 154 g (3.5 mol) ethylene oxide as the last are added. Once the addition is finished, the autoclave is sealed immediately and heated to and kept at 75-80° C. under stirring followed by a reaction for 2-3 h. When the temperature is lower than 40° C. and the pressure is released, the reaction solution is filtered. The filtrate is respectively passed through the cation exchange resin 732 column and the anion exchange resin 717 column. The pH value of the solution is adjusted to 5.0±0.2 by using 5N HCl. The filtrate is let stand for 6-8 h at room temperature. Crystal is obtained after filtration and 420 g of solid cake is obtained.
3. The solid cake obtained from 2 above is re-dissolved in a 20-fold amount of methanol-ethanol (95:5) and heated to dissolve. The solution is heated at reflux for 30 min and filtrated. The filtrate is let stand for 6-8 h at room temperature. Crystal is obtained after filtration followed by a vacuum drying at 40-50° C. The 336 g of solid powder is obtained. The content of trihydroxyethyl rutoside is 98.2%. The melting point is 184-186° C. The yield is 64%.
1. The preparation of 7-monohydroxyethyl rutoside is the same as descried in EXAMPLE 1.
2. Within a 5,000 ml autoclave, 510 g (0.71 mol) 7-monohydroxyethyl rutoside, 10 ml pyridine, 2,000 ml methanol, and 154 g (3.5 mol) ethylene oxide as the last are added. Once the addition is finished, the autoclave is sealed immediately and heated to and kept at 75-80° C. with stirring followed by a reaction for 2-3h. When the temperature is lower than 40° C. and the pressure is released, the pH value of the solution is adjusted to 5.0±0.2 by using 5N HCl. The filtrate stands for 6-8 h at room temperature. Crystal is obtained after filtration and 410 g of solid cake is obtained.
3. The solid cake obtained from 2 above is re-dissolved in a 20-fold amount of methanol and heated to dissolve. The solution is heated at reflux for 30 min and filtrated. The filtrate is let stand for 6-8 h at room temperature. Crystal is obtained after filtration followed by vacuum drying at 40-50° C. A solid powder of 310 g is obtained. The content of trihydroxyethyl rutoside is 98.3%. The melting point is 184-186° C. The yield is 61%.
1. 100 g trihydroxyethyl rutoside with a purity of 98.7% as obtained from EXAMPLE 5 is added into 3,000 ml methanol-ethanol. The solution is heated at reflux for 30 min, and filtrated. After filtration, the crystal is dried under vacuum at 40-50° C. 80.2 g of trihydroxyethyl rutoside is obtained. The chromatographic purity is 98.8%. The content is 98.8%. The melting point is 186-188° C.
2. 80 g trihydroxyethyl rutoside with a purity of 98.8% as obtained above is added into 2,400 ml methanol-isopropanol (95:5). The solution is heated at reflux for 30 min, and filtrated while hot. The filtrate is let stand for 6-8 h at room temperature. After filtration, the crystal is dried under vacuum g at 40-50° C. 64.3 g trihydroxyethyl rutoside is obtained. The chromatographic purity is 99.2%. The content is 99.2%. The melting point is 187-189° C.
| Number | Date | Country | Kind |
|---|---|---|---|
| 201310188451.8 | May 2013 | CN | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CN2014/078322 | 5/23/2014 | WO | 00 |
