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.
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.