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CN111153862B - A kind of refining method of Recinade - Google Patents

A kind of refining method of Recinade Download PDF

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Publication number
CN111153862B
CN111153862B CN202010059448.6A CN202010059448A CN111153862B CN 111153862 B CN111153862 B CN 111153862B CN 202010059448 A CN202010059448 A CN 202010059448A CN 111153862 B CN111153862 B CN 111153862B
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hexane
ethyl acetate
mixed solvent
stirring
crude
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CN111153862A (en
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夏中宁
吴进
张丽杰
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Beijing Xin Kai Yuan Pharmaceutical Technology Co ltd Hainan Branch
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Beijing Xin Kai Yuan Pharmaceutical Technology Co ltd Hainan Branch
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    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D249/00Heterocyclic compounds containing five-membered rings having three nitrogen atoms as the only ring hetero atoms
    • C07D249/02Heterocyclic compounds containing five-membered rings having three nitrogen atoms as the only ring hetero atoms not condensed with other rings
    • C07D249/081,2,4-Triazoles; Hydrogenated 1,2,4-triazoles
    • C07D249/101,2,4-Triazoles; Hydrogenated 1,2,4-triazoles with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
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Abstract

本发明涉及一种雷西纳德的精制方法,包括以下步骤:将雷西纳德粗品加入到加热至沸的溶剂中,加热至溶解,加入活性炭,过滤,滴加正己烷,缓慢降温至35~45℃析晶1~2h,再缓慢降温至0~10℃析晶2~3h,过滤,减压干燥,得到高纯度的成品。与现有方法相比,本发明所述方法精制效果好,精制过程所用到的溶剂较普通,工业化操作简单,精制目标产物收率和纯度高,适合工业化大生产。

Figure 202010059448

The invention relates to a method for purifying resinard, which comprises the following steps: adding crude resinad into a solvent heated to boiling, heating to dissolving, adding activated carbon, filtering, adding n-hexane dropwise, and slowly cooling to 35 ℃ Crystallize at ~45 °C for 1 ~ 2 hours, then slowly cool down to 0 ~ 10 °C for crystallization for 2 ~ 3 hours, filter, and dry under reduced pressure to obtain high-purity finished products. Compared with the existing method, the method of the invention has good refining effect, common solvent used in the refining process, simple industrial operation, high yield and high purity of the refining target product, and is suitable for large-scale industrial production.

Figure 202010059448

Description

Raisinard refining method
Technical Field
The invention relates to a refining method of Resinard, belonging to the technical field of medicines.
Background
Gout is a crystal-related arthropathy caused by precipitation of mono-sodiuurate, and is directly related to hyperuricemia caused by purine metabolic disturbance and reduced uric acid excretion. Rassinard (Lesinured) is an oral drug for promoting uric acid excretion, which can treat gout patients with hyperuricemia by inhibiting uric acid transporter URAT of renal proximal convoluted tubule, and the drug has a trade name of Zurampic in the United states, Rassinard is the first approved inhibitor of urate reabsorption transporter (URAT1) in the world, and the dosage form is an oral tablet, and the specification is 200 mg. The recommended dose is 200mg once a day in combination with allopurinol or febuxostat. Chemical name of Ravinard: 2- [ [ 5-bromo-4- (4-cyclopropyl-1-naphthalenyl) -4H-1,2, 4-triazol-3-yl ] thio ] acetic acid of the formula:
Figure BDA0002373959500000011
the original patent CN104736522A discloses that 1-cyclopropyl naphthalene-4-yl isothiocyanate (2) is used as a starting material, cyclizing with formyl hydrazine to obtain 4- (1-cyclopropyl naphthalene-4-yl) -4H-1,2, 4-triazole-thiol (3), and then nucleophilic substitution is carried out on the methyl bromoacetate to obtain 2- (4- (1-cyclopropyl naphthalene-4-yl) -4H-1,2, 4-triazole-3-yl sulfenyl) methyl acetate (4), NBS bromination is carried out to obtain 2- (5-bromine-4- (1-cyclopropyl naphthalene-4-yl) -4H-1,2, 4-triazole-3-yl sulfenyl) methyl acetate (5), and then hydrolysis is carried out to obtain the Raschindyle (1).
The synthetic route is as follows:
Figure BDA0002373959500000021
through a plurality of tests, the crude product compound (1) of the Racinidde synthesized by the method has low purity, and the impurities are mainly two: respectively as impurity A and impurity B
Figure BDA0002373959500000022
Impurity A: the residual compound 4 is hydrolyzed.
Impurity B: the chloride contained in NBS reacts with compound 4, and the generated chloride impurity is further hydrolyzed.
According to patent CN104736522A example 2A, compound 5 is synthesized, tetrahydrofuran is used as a solvent, NBS is used as a brominating agent, compound 4 has large residue, the content is about 3-10%, and the content of chlorinated impurities is 0.1-1.0%.
Disclosure of Invention
In view of the defects of the prior art, the invention aims to provide a method for refining a crude product of Raschild, which removes or controls impurities in the crude product within a certain range and improves the product quality.
The technical scheme adopted by the invention is as follows:
a method for refining Raschindde comprises the following steps:
adding the crude product of Racinidde into an organic solvent, heating to dissolve, adding activated carbon, filtering, dropwise adding n-hexane, cooling to 35-45 ℃ for crystallization for 1-2 h, cooling to 0-10 ℃ for crystallization for 2-3 h, filtering, and drying under reduced pressure to obtain a high-purity finished product.
Preferably, the organic solvent is one or more of ethyl acetate, isopropanol, n-hexane and dichloromethane.
Preferably, the organic solvent is a mixed solvent of ethyl acetate and n-hexane, a mixed solvent of ethyl acetate and isopropanol, and a mixed solvent of dichloromethane and n-hexane.
Preferably, the volume ratio of the ethyl acetate to the n-hexane in the mixed solvent of the ethyl acetate and the n-hexane is 1.0: (0.1 to 1.0); the volume ratio of ethyl acetate to isopropanol in the mixed solvent of ethyl acetate and isopropanol is 1.0 (0.1-0.5); the volume ratio of the dichloromethane to the n-hexane in the mixed solvent of the dichloromethane and the n-hexane is 1.0: (1-5).
More preferably, the volume ratio of ethyl acetate to n-hexane in the mixed solvent of ethyl acetate and n-hexane is 1.0: 0.2; the volume ratio of ethyl acetate to isopropanol in the mixed solvent of ethyl acetate and isopropanol is 1.0: 0.3; the volume ratio of the dichloromethane to the n-hexane in the mixed solvent of the dichloromethane and the n-hexane is 1.0: 1.5.
preferably, the feeding ratio of the crude Raxinard product to the organic solvent is 1 g: (10-60) ml.
Preferably, the feeding ratio of the crude Raxinard product to the n-hexane is 1 g: (5-20) ml.
Preferably, the dissolving temperature is 35-80 ℃.
Preferably, the feed ratio of the activated carbon to the crude product of Racinade is that of the crude product of Racinade: activated carbon 1 g: 0.1 g.
Compared with the prior art, the invention has the beneficial effects that:
the refining effect is good, the target product is refined, the yield and the purity are high, and the impurities A and B in the refined product are obviously reduced compared with the impurities A and B before refining, so that the quality of the finished product Racinidde is ensured; the refining process is simple, and the used solvent is common. Easy recovery, greatly simplifies the industrial operation, and is suitable for industrial production.
Drawings
FIG. 1 is an HPLC chromatogram of crude product
FIG. 2 is an HPLC chromatogram of the purification of example 2
FIG. 3 is an HPLC chromatogram of example 3
Detailed Description
The present invention will be described in further detail with reference to the following detailed description and accompanying drawings.
The experimental methods used in the examples of the present invention are all conventional methods unless otherwise specified.
The materials, reagents and the like used in the examples of the present invention can be obtained commercially without specific description.
The crude product of Raxinard in the embodiment of the invention is synthesized by the method of reference CN 104736522A. The method comprises the following specific steps:
adding 160.0g of intermediate 4 and 1.28L of tetrahydrofuran into a 5L three-neck flask, starting stirring, heating to 35-42.0 ℃, and stirring until the intermediate 4 and the tetrahydrofuran are dissolved; cooling to 27-32 ℃, adding 148.0g of NBS, and reacting for 3.0-4.0 h; cooling to 5 ℃, adding 800ml of toluene and 800ml of purified water, stirring and separating liquid, washing an organic phase with 800ml of 3% sodium bisulfite solution and 800ml of 5% sodium bicarbonate solution respectively, standing and separating liquid, collecting the organic phase, adding 580ml of 1mol/L sodium hydroxide into the organic phase, reacting for 2 hours, separating liquid, collecting a water phase, concentrating, cooling and crystallizing, filtering, and washing with water to obtain a wet product; adding 720ml of purified water into the wet product, heating to 35 ℃, stirring for dissolving, adding 1.6L of ethyl acetate, adjusting the pH value of the system to be 2-4 by using 24% hydrobromic acid, stirring for 30min, separating liquid, washing the organic phase once by using 320ml of purified water, concentrating the organic phase until solid is separated out, keeping the temperature at 38-42 ℃, continuously stirring for crystallization for 3-4 h, slowly cooling to 5-10 ℃, stirring for 2h, filtering, washing, and drying under reduced pressure and vacuum to obtain 123.0g of crude product of Ravinard. Purity 95.12%, impurity a: 4.22 percent; impurity B: 0.24 percent.
In the embodiment of the invention, the method for measuring the Ravinard purity and the content of each impurity adopts an HPLC method, and the main test conditions are as follows:
a chromatographic column: kromasil C184.6X 150mm, 5 μm
Mobile phase: a: 0.02mol/L potassium dihydrogen phosphate (adjusted to pH 3.0 with phosphoric acid) B: methanol
The gradient elution procedure was as follows:
time (minutes) Mobile phase A (%) Mobile phase B (%)
0 90 10
5 90 10
15 70 30
35 45 55
80 15 85
95 15 85
97 90 10
107 90 10
Column temperature: 35 deg.C
Detection wavelength: 226nm
Diluent agent: acetonitrile
Sample concentration: 0.5mg/ml
Flow rate: 1.0ml/min
Sample introduction amount: 5 μ l
Example 1
Taking 10.0g of crude Raxinard product, adding300ml of ethyl acetateHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,150ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and drying under vacuum at 50 ℃ for 6-8 h to obtain 8.1g of a white solid, namely high-purity Ravinard, wherein the yield is 81.0% (weight after purification/Ravinard crude product multiplied by 100%), the purity (in terms of peak area) is 99.95%, and the impurity A: not detected; impurity B:0.05 percent.
Example 2
Taking 10.0g of crude Raxinard product, adding250ml of ethyl acetateHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and drying under vacuum at 50 ℃ for 6-8 h under reduced pressure to obtain 8.6g of white solid, namely high-purity Ravinard, wherein the yield is 86.0%, the purity is 99.96%, and the impurity A: not detected; 0.04 percent of impurity B
Example 3
Taking 10.0g of crude Raxinard product, adding200ml of ethyl acetate and 60ml of isopropanolHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.4g of white solid, namely high-purity Ravinard, wherein the yield is 84.0%, and the purity is 99.94%; impurity A: not detected; 0.06 percent of impurity B.
Example 4
Taking 10.0g of crude Raxinard product, adding200ml of methylene chlorideHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,filter with filter element200ml of n-hexane was added dropwise to the solutionStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.3g of white solid, namely high-purity Ravinard, wherein the yield is 83.0%, and the purity is 99.98%; impurity A: not detected; 0.02 percent of impurity B.
Example 5
Taking 10.0g of crude Raxinard product, adding250ml of ethyl acetateHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,75ml of n-hexane was added dropwise to the filtrate,maintaining the temperature at 35-45 ℃, stirring for crystallization for 1-2 h, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying at 50 ℃ for 6-8 h to obtain 8.6g of white solid, namely high-purity Ravinard, wherein the yield is 86.0%, and the purity is 99.95%; impurity A: not detected; 0.05 percent of impurity B.
Example 6
Taking 10.0g of crude Raxinard product, adding200ml of ethyl acetate and 20ml of isopropanolHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.4g of white solid, namely high-purity Ravinard, wherein the yield is 84.0%, and the purity is 99.97%; impurity A: not detected; 0.03 percent of impurity B.
Example 7
Taking 10.0g of crude Raxinard product, adding200ml of ethyl acetate and 100ml of isopropanolHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.2g of white solid, namely high-purity Ravinard, wherein the yield is 82.0%, and the purity is 99.95%; impurity A: not detected; 0.05 percent of impurity B.
Example 8
Taking 10.0g of crude Raxinard product, adding200ml of ethyl acetateAnd 20ml of n-hexaneHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.4g of white solid, namely high-purity Ravinard, wherein the yield is 84.0%, and the purity is 99.97%; impurity A: not detected; 0.03 percent of impurity B.
Example 9
Taking 10.0g of crude Raxinard product, adding200ml of ethyl acetate and 100ml of n-hexaneHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.3g of white solid, namely high-purity Ravinard, wherein the yield is 83.0%, and the purity is 99.93%; impurity A: not detected; 0.07 percent of impurity B.
Example 10
Taking 10.0g of crude Raxinard product, adding200ml of ethyl acetate and 40ml of n-hexaneHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.7g of white solid, namely high-purity Ravinard, wherein the yield is 87.0%, and the purity is 99.93%; impurity A: not detected; 0.07 percent of impurity B.
Example 11
Taking 10.0g of crude Raxinard product, adding100ml of methylene chloride and 100ml of n-hexaneHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.2g of white solid, namely high-purity Ravinard, wherein the yield is 82.0%, and the purity is 99.94%; impurity A: not detected; 0.0 part of impurity B6%。
Example 12
Taking 10.0g of crude Raxinard product, adding100ml of methylene chloride and 150ml of n-hexaneHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.9g of white solid, namely high-purity Ravinard, wherein the yield is 89.0%, and the purity is 99.97%; impurity A: not detected; 0.03 percent of impurity B.
Example 13
Taking 10.0g of crude Raxinard product, adding100ml of methylene chloride and 500ml of n-hexaneHeating to dissolve at 35-80 deg.C, adding 1.0g of activated carbon, stirring for 10-15 min, filtering,50ml of n-hexane was added dropwise to the filtrateStirring and crystallizing for 1-2 h at the temperature of 35-45 ℃, slowly cooling to 0-10 ℃, stirring for 2-3 h, performing suction filtration, and performing vacuum reduced pressure drying for 6-8 h at the temperature of 50 ℃ to obtain 8.3g of white solid, namely high-purity Ravinard, wherein the yield is 83.0%, and the purity is 99.93%; impurity A: not detected; 0.07 percent of impurity B.
The foregoing is a more detailed description of the present invention that is presented in conjunction with specific embodiments, and the practice of the invention is not to be considered limited to those descriptions. It will be apparent to those skilled in the art that a number of simple derivations or substitutions can be made without departing from the inventive concept.

Claims (9)

1.一种雷西纳德的精制方法,其特征在于,包括以下步骤:1. a refining method of Recinade, is characterized in that, comprises the following steps: 将雷西纳德粗品加入到有机溶剂中,加热至溶解,加入活性炭,过滤,滴加正己烷,降温至35~45℃析晶1~2h,再降温至0~10℃析晶2~3h,过滤,减压干燥,得到高纯度的成品。Add the crude Recinade to the organic solvent, heat until dissolved, add activated carbon, filter, dropwise add n-hexane, cool to 35-45 °C for crystallization for 1-2 hours, and then cool to 0-10 °C for crystallization for 2-3 hours , filtered, and dried under reduced pressure to obtain a high-purity finished product. 2.根据权利要求1所述雷西纳德的精制方法,其特征在于,所述有机溶剂为乙酸乙酯、异丙醇、正己烷、二氯甲烷中的一种或者多种。2. The method for refining Recinad according to claim 1, wherein the organic solvent is one or more of ethyl acetate, isopropanol, n-hexane and methylene chloride. 3.根据权利要求2所述雷西纳德的精制方法,其特征在于,所述有机溶剂为乙酸乙酯和正己烷混合溶剂,乙酸乙酯和异丙醇混合溶剂、二氯甲烷和正己烷混合溶剂。3. the refining method of Recinad according to claim 2, is characterized in that, described organic solvent is ethyl acetate and n-hexane mixed solvent, ethyl acetate and Virahol mixed solvent, dichloromethane and n-hexane mixed solvent. 4.根据权利要求3所述雷西纳德的精制方法,其特征在于,乙酸乙酯和正己烷混合溶剂中乙酸乙酯和正己烷的体积比为1.0:(0.1~1.0);乙酸乙酯和异丙醇混合溶剂中乙酸乙酯和异丙醇的体积比为1.0:(0.1~0.5);二氯甲烷和正己烷混合溶剂中二氯甲烷和正己烷的体积比为1.0:(1.0~5.0)。4. the refining method of Recinad according to claim 3, is characterized in that, in ethyl acetate and n-hexane mixed solvent, the volume ratio of ethyl acetate and n-hexane is 1.0: (0.1~1.0); The volume ratio of ethyl acetate and isopropanol in the mixed solvent with isopropanol is 1.0:(0.1~0.5); the volume ratio of dichloromethane and n-hexane in the mixed solvent of dichloromethane and n-hexane is 1.0:(1.0~0.5) 5.0). 5.根据权利要求4所述雷西纳德的精制方法,其特征在于,乙酸乙酯和正己烷混合溶剂中乙酸乙酯和正己烷的体积比为1.0:0.2;乙酸乙酯和异丙醇混合溶剂中乙酸乙酯和异丙醇的体积比为1.0:0.3;二氯甲烷和正己烷混合溶剂中二氯甲烷和正己烷的体积比为1.0:1.5。5. the refining method of Recinade according to claim 4, is characterized in that, in ethyl acetate and n-hexane mixed solvent, the volume ratio of ethyl acetate and n-hexane is 1.0: 0.2; Ethyl acetate and Virahol The volume ratio of ethyl acetate and isopropanol in the mixed solvent is 1.0:0.3; the volume ratio of dichloromethane and n-hexane in the mixed solvent of dichloromethane and n-hexane is 1.0:1.5. 6.根据权利要求1所述雷西纳德的精制方法,其特征在于,所述雷西纳德粗品与所述有机溶剂的投料比为1g:(10~60)ml。6 . The method for purifying Recinade according to claim 1 , wherein the charging ratio of the crude Recinade to the organic solvent is 1 g: (10-60) ml. 7 . 7.根据权利要求1所述雷西纳德的精制方法,其特征在于,所述雷西纳德粗品与所述正己烷的投料比为1g:(5~20)ml。7 . The method for purifying Resinard according to claim 1 , wherein the feeding ratio of the crude Resinad to the n-hexane is 1 g: (5-20) ml. 8 . 8.根据权利要求1所述雷西纳德的精制方法,其特征在于,溶解温度为35~80℃。8 . The method for purifying Recinade according to claim 1 , wherein the dissolution temperature is 35-80° C. 9 . 9.根据权利要求1所述雷西纳德的精制方法,其特征在于,活性炭与雷西纳德粗品的投料比为雷西纳德粗品:活性炭=1g:0.1g。9 . The refining method of Resinard according to claim 1 , wherein the charging ratio of the activated carbon to the Resinad crude product is the Resinad crude product: activated carbon=1 g: 0.1 g. 10 .
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