Disclosure of Invention
The invention aims to provide a method for preparing high-purity (-) -coriolide primary alcohol triethylsilane and preparing (-) benzoyl coriolide from the (-) -coriolide primary alcohol triethylsilane with high selectivity, convenient operation and easy industrialization and high yield.
In a first aspect, the present invention provides a method for preparing a compound of formula 3 in high purity, the method comprising performing the method shown in the following scheme:
in the formula, R is triethylchlorosilane;
the method comprises the following steps: protecting primary alcohol of (-) -coriolide shown in a formula 4 with triethylchlorosilane in dichloromethane in the presence of diisopropylethylamine to obtain a compound shown in a formula 3;
wherein the mol ratio of (-) -coriolide shown in the formula 4 to triethylchlorosilane is 1-1.5,
the mol ratio of the (-) -coriolide shown in the formula 4 to the diisopropylethylamine is 1.5-3;
the volume/mass (ml/g) of the dichloromethane and the (-) -coriolide shown in the formula 4 is 3-10;
the reaction temperature is 20-30 ℃.
In a specific embodiment, the ratio of (-) -coriolide of formula 4 to triethylchlorosilane is 1.1.
The formula 5 is (-) -Corey Lactone primary alcohol and secondary alcohol double-protected disubstituted impurity.
In a second aspect, the present invention provides a method for preparing a high purity benzoylcoriolide of formula 1, comprising performing the method as shown in the following scheme:
in the formula, R is triethylchlorosilane;
wherein the method comprises the steps of:
a. protecting primary alcohol of (-) -coriolide shown in a formula 4 by using triethylchlorosilane in dichloromethane in the presence of diisopropylethylamine in a solvent to obtain a compound shown in a formula 3;
b. carrying out esterification reaction on the compound shown in the formula 3 and benzoic acid to obtain (-) -benzoyl colactone shown in a formula 2 with protected primary alcohol; and
c. removing the primary alcohol protecting group of the (-) -benzoyl colactone shown in the formula 2 to obtain the (-) -benzoyl colactone shown in the formula 1;
in the step a, the first step is carried out,
the mol ratio of the (-) -coriolide shown in the formula 4 to the triethylchlorosilane is 1 to 1.5,
the mol ratio of the (-) -coriolide shown in the formula 4 to the diisopropylethylamine is 1.5-3;
the volume/mass (ml/g) of the dichloromethane and the (-) -coriolide shown in the formula 4 is 3-10;
the reaction temperature is 20-30 ℃.
In a specific embodiment, in step a, the ratio of (-) -coriolide of formula 4 to triethylchlorosilane is 1.1.
It is to be understood that within the scope of the present invention, the above-described features of the present invention and those specifically described below (e.g., in the examples) may be combined with each other to form new or preferred embodiments. Not to be reiterated herein, but to the extent of space.
Detailed Description
The inventor has conducted extensive and intensive studies and unexpectedly found that a specific protecting group can be used for protecting the primary alcohol of (-) -Corey Lactone with high selectivity, then the primary alcohol is reacted with benzoic acid to obtain the (-) -Corey Lactone benzoate protected by the primary alcohol, and finally the primary alcohol protecting group is selectively removed to obtain the (-) -Corey Lactone benzoate. The invention has good reaction selectivity, easy crystallization and purification of the product and high purity; the reaction yield is high, and the cost is greatly reduced; convenient operation and easy industrialization. The present invention has been completed based on this finding.
Method of the invention
The invention provides a method for preparing (-) -Corey Lactone benzoate with high purity and high yield. From (-) -Corey Lactone, the (-) -Corey Lactone benzoate protected by primary alcohol is obtained by high-selectivity single protection of the primary alcohol, then the esterification reaction of the secondary alcohol and benzoic acid, and then the silicon-based protection of the primary alcohol is selectively removed, thus obtaining the (-) -Corey Lactone benzoate. The invention has good reaction selectivity, easy crystallization and purification of the product and high purity; the reaction yield is high, and the cost is greatly reduced; can adopt a one-pot method, is convenient to operate and is easy to industrialize.
Wherein the structure of (-) -Corey Lactone is shown as follows;
(-)-Corey Lactone
the technical scheme for preparing the high-purity primary alcohol protected (-) -Corey Lactone provided by the invention is as follows:
reacting (-) -Corey Lactone in a solvent S1, a base B1 and a protective agent C1 at a certain reaction temperature T1 to obtain high-purity primary alcohol protected (-) -Corey Lactone;
wherein the temperature T1 is 0-50 ℃, most preferably 20-30 ℃;
wherein the solvent S1 is one of dichloromethane, trichloromethane, 1, 2-dichloroethane, acetonitrile, DMF or THF; most preferably dichloromethane;
the volume/mass (ml/g) of the solvent S1 and (-) -Corey Lactone is 1:1-50ml/g, preferably 3-10 ml/g;
the alkali B1 is one of triethylamine, diisopropylethylamine, pyridine, imidazole or N-methylmorpholine; wherein the reaction yield of the diisopropylethylamine is highest, the disubstituted impurity is minimum, and the most preferable is diisopropylethylamine;
the molar ratio of (-) -Corey Lactone to the alkali B1 is 1-5, preferably 1: 1.5-3;
the protective agent C1 is one of trimethylchlorosilane, triethylchlorosilane, tert-butyldimethylchlorosilane and tert-butyldiphenylchlorosilane; the reaction effect of the triethylchlorosilane is best, the disubstituted impurity is minimum, the yield is highest, and the triethylchlorosilane is most preferred;
according to the charging proportion of the (-) -Corey Lactone and the protective agent, the double-substituted impurities are increased when the dosage of the protective agent is increased, the amount is small, the reaction is incomplete, the yield is low, and the optimal dosage is 1-1.5 eq.
The invention has the advantages that:
the method of the invention has the following advantages:
1. good selectivity, convenient operation and easy industrialization;
2. can prepare high-purity primary alcohol protected (-) -Corey Lactone; and
3. the yield of the prepared (-) benzoyl coriolide is high.
The technical solution of the present invention will be further described with reference to the following specific embodiments, but the following embodiments are not intended to limit the present invention, and all of the various application methods adopted according to the principles and technical means of the present invention belong to the scope of the present invention. The experimental procedures, in which specific conditions are not noted in the following examples, are generally carried out under conventional conditions or conditions recommended by the manufacturers. Unless otherwise indicated, percentages and parts are by weight.
Example 1
Based on the reaction scheme shown above, the inventors examined the preparation of primary alcohol-protected (-) -Corey Lactone using trimethylchlorosilane, triethylchlorosilane, t-butyldimethylchlorosilane or t-butyldiphenylchlorosilane.
Table 1.
Serial number
|
Protecting group
|
Yield of
|
1
|
Trimethylchlorosilane
|
96%
|
2
|
Triethylchlorosilane
|
89%
|
3
|
Tert-butyldimethylsilyl chloride
|
87%
|
4
|
Tert-butyldiphenylchlorosilane
|
82% |
As a result, it was found that trimethylchlorosilane yield was the highest and activity was the best.
Example 2
In this example, the inventors further examined possible impurities (i.e., primary alcohol, secondary alcohol disubstituted impurities) resulting from protection of the primary hydroxyl group by trimethylchlorosilane, triethylchlorosilane, t-butyldimethylchlorosilane, or t-butyldiphenylchlorosilane.
Table 2.
Serial number
|
Protecting group
|
Yield of(%)
|
Disubstituted impurity (%)
|
1
|
Trimethylchlorosilane
|
96%
|
7.5%
|
2
|
Triethylchlorosilane
|
89%
|
6.0%
|
3
|
Tert-butyldimethylsilyl chloride
|
87%
|
6.5%
|
4
|
Tert-butyldiphenylchlorosilane
|
82%
|
7.0% |
The inventors have found that although the protection of the primary hydroxyl groups with triethylchlorosilane, t-butyldimethylchlorosilane or t-butyldiphenylchlorosilane yields slightly lower impurities than trimethylchlorosilane, there is no substantial difference. The use of chlorotrimethylsilane seems to be the best choice, considering that the yield and activity of chlorotrimethylsilane are far superior to those of chlorotriethylsilane, tert-butyldimethylchlorosilane or tert-butyldiphenylchlorosilane.
Example 3
In this example, the inventors have also investigated specific process conditions for preparing primary alcohol-protected (-) -Corey Lactone from trimethylchlorosilane, triethylchlorosilane, t-butyldimethylchlorosilane or t-butyldiphenylchlorosilane.
As a result, the inventors have unexpectedly found that the yields and the impurity cases at specific molar ratios in the presence of each base in each solvent at each reaction temperature examined using trimethylchlorosilane, t-butyldimethylchlorosilane or t-butyldiphenylchlorosilane are similar to those of examples 1 and 2.
If the preparation of primary alcohol-protected (-) -Corey Lactone with triethylchlorosilane in the presence of a specific base, diisopropylethylamine, in a specific solvent, at a specific reaction temperature and a specific molar ratio, the secondary alcohol disubstituted impurities generated by the preparation of the primary alcohol-protected (-) -Corey Lactone with triethylchlorosilane are far lower than those generated by the preparation of trimethylchlorosilane, t-butyldimethylchlorosilane or t-butyldiphenylchlorosilane, high purity of the primary alcohol-protected (-) -Corey Lactone can be prepared. The specific data are shown in the following table:
TABLE 3 reaction of triethylchlorosilane in different bases (triethylamine, diisopropylethylamine, pyridine, DBU, imidazole or N-methylmorpholine).
Serial number
|
Alkali
|
Yield (%)
|
Disubstituted impurity (%)
|
1
|
Triethylamine
|
91%
|
2.2%
|
2
|
Diisopropylethylamine
|
92%
|
0.8%
|
3
|
Pyridine compound
|
81%
|
1.5%
|
4
|
DBU
|
88%
|
1.3%
|
5
|
Imidazole
|
85%
|
2.0%
|
6
|
N-methylmorpholine
|
70%
|
2.2% |
According to the results in table 3, the specific base used was not regularly reproducible for the formation of disubstituted impurities, of which diisopropylethylamine works best.
Table 4 reactivity of triethylchlorosilane with diisopropylethylamine in different solvents.
Serial number
|
Solvent(s)
|
Yield (%)
|
Disubstituted impurity (%)
|
1
|
Methylene dichloride
|
92%
|
0.8
|
2
|
Acetonitrile
|
75%
|
2.5
|
3
|
DMF
|
85%
|
1.5
|
4
|
THF
|
80%
|
2.9 |
According to the results in Table 4, the effect of the specific solvent used on the yield and the formation of disubstituted impurities is not regularly reproducible, with the best results being obtained when dichloromethane is used as solvent.
TABLE 5 reactivity of triethylchlorosilane with diisopropylethylamine at different temperatures.
Serial number
|
Solvent(s)
|
Yield (%)
|
Disubstituted impurity (%)
|
1
|
0℃~10℃
|
82%
|
0.5%
|
2
|
10℃-20℃
|
86%
|
0.8%
|
3
|
20℃~30℃
|
92%
|
0.6%
|
4
|
40℃-50℃
|
80%
|
3.5% |
According to the results in table 5, the specific reaction temperature of triethylchlorosilane and diisopropylethylamine has no regular and recyclable effect on yield and generation of disubstituted impurities, wherein the comprehensive effect of the reaction of triethylchlorosilane and diisopropylethylamine at 20-30 ℃ is the best.
TABLE 6 reaction of (-) -coriolide with triethylchlorosilane in different molar ratios
Serial number
|
Molar ratio of (-) -coriolide to triethylchlorosilane
|
Yield (%)
|
Disubstituted impurity (%)
|
1
|
0.8
|
78%
|
0.9%
|
2
|
1.1
|
92%
|
0.3%
|
3
|
1.3
|
86%
|
0.7%
|
4
|
1.8
|
83%
|
3.3% |
TABLE 7 reaction of (-) -Coriolis lactone with diisopropylethylamine in different molar ratios
Serial number
|
Molar ratio of (-) -coriolide to diisopropylethylamine
|
Yield (%)
|
Disubstituted impurity (%)
|
1
|
1.2
|
82%
|
0.7%
|
2
|
1.6
|
87%
|
0.5%
|
3
|
2.5
|
91%
|
0.4%
|
4
|
3.4
|
80%
|
1.1% |
TABLE 8 reaction of methylene chloride with (-) -coriolide at different volume/mass ratios (ml/g)
Based on the above examples, the present inventors have unexpectedly discovered that primary alcohol protected (-) -Corey Lactone can be prepared in high yields with minimal secondary impurities by reacting triethylchlorosilane in combination with diisopropylethylamine in a specific solvent, dichloromethane, at 20 ℃ to 30 ℃.
Example 6: laboratory-Scale preparation of benzoylcorinolide
17.2g (1eq) of (-) -Corey Lactone is put into a 500ml three-mouth bottle, 100ml of dichloromethane is added, stirring and mixing are carried out, 34.1ml (2.5eq) of diisopropylethylamine is added at room temperature, stirring is carried out, the temperature is reduced to 20 ℃, 16.6g (1.1eq) of triethylchlorosilane is slowly added dropwise, the temperature is kept for 20-30 ℃ for reaction for 2 hours, 18.3g (1.5eq) of benzoic acid is added, 26.9g (1.5eq) of EDCI and 0.7g of DMAP (0.1eq) are added, the mixture is kept for reaction for 20 hours at room temperature, 150ml (4.1eq) of 10% hydrochloric acid is added, the mixture is kept for reaction for 6-12 hours under stirring, layering is carried out, anhydrous sodium sulfate is added into a dichloromethane layer for drying, filtering is carried out, filtrate is evaporated to dryness, 50ml of petroleum ether is added for crystallization, 23.8g of (-) -Corey Lactone tonoate is obtained, the yield is 86%, the purity is 99.5.
Purity detection HPLC method: a chromatographic column: ZORBAX SB-C184.6mm 150mm,5 um; mobile phase A: 0.1% phosphoric acid water, mobile phase B: acetonitrile, gradient elution as follows; column temperature: 25 ℃; detection wavelength: 230 nm; flow rate: 1.0 ml/min; sample introduction amount: 5 μ l.
ee detection HPLC method: a chromatographic column: CHIRALPAK AD-H, 250 x 4.6mm, 5 um; mobile phase: n-hexane: ethanol 70: 30; flow rate: 0.5 ml/min; column temperature: 25 ℃; detection wavelength: 230 nm; sample introduction amount: 5 mu l of the solution; operating time: and (4) 40 min.
Example 7: pilot scale production of benzoylcorinolide
172g (1eq) of (-) -Corey Lactone is put into a 5000ml three-mouth bottle, 1000ml of dichloromethane is added, the mixture is stirred and mixed, 341ml (2.5eq) of diisopropylethylamine is added at room temperature, the temperature is reduced to 20 ℃ under stirring, 165.8g (1.1eq) of triethylchlorosilane is slowly added dropwise, the temperature is kept at 20-30 ℃ for reaction for 2 hours, 183g (1.5eq) of benzoic acid is added, 269g (1.5eq) of EDCI and 7g of DMAP (0.1eq) are added, the reaction is carried out at room temperature for 20 hours, 10% of 1500ml (4.1eq) of hydrochloric acid is added, the reaction is carried out for 6-12 hours under heat preservation and stirring, layers are separated, the dichloromethane layer is added with anhydrous sodium sulfate for drying, the filtration is carried out, the filtrate is evaporated to dryness, 500ml of petroleum ether is added for crystallization, 242.3g of (-) -Corey Lacey Lactone benzoate is obtained, the yield is 87.7%, the purity is 99..
Example 8: production scale preparation of benzoylcorinolide
17.2kg of (-) -Corey Lactone is put into a 500L reaction kettle, 130kg of dichloromethane is added, stirring and mixing are carried out, 25.3kg of diisopropylethylamine is added at room temperature, the temperature is reduced to 20 ℃ under stirring, 16.6kg (1.1eq) of triethylchlorosilane is slowly dripped, the temperature is kept for 20-30 ℃ for reaction for 2 hours, 18.3kg of benzoic acid is added, 26.9kg of EDCI and 0.7kg of DMAP are added, the reaction is carried out at room temperature for 20 hours, the cooling is carried out for 10 ℃, 150kg of 10% hydrochloric acid is added, the reaction is carried out for 6-12 hours under heat preservation and stirring, layering is carried out, anhydrous sodium sulfate is added into a dichloromethane layer for drying, filtering is carried out, filtrate is evaporated to dryness, 50L of petroleum ether is added for crystallization, and 24kg of (-) -Corey Lactone benzoate is obtained, the yield is 86.9%, the.
Example 9: preparation and structure confirmation of (-) -Corey Lactone primary alcohol triethylsilane
Putting 1.72g (1eq) (-) -Corey Lactone into a 50ml three-necked bottle, adding 20ml dichloromethane, stirring and mixing, adding 3.4ml (2.5eq) of diisopropylethylamine at room temperature, cooling to 20 ℃, slowly adding 1.66g (1.1eq) of triethylchlorosilane dropwise, keeping the temperature at 20-30 ℃ for reaction for 2 hours, pouring the reaction liquid into 20ml of ice water, separating an aqueous layer, drying with anhydrous sodium sulfate, filtering, evaporating the filtrate to dryness, and performing column chromatography separation and purification (petroleum ether elution) to obtain 2.63g of (-) -Corey Lactone primary alcohol triethylsilane, wherein the yield is 92% and the GC is 98.7%.
GC/MS(EI):257(M-CH2CH3)。
1H-NMR(CDCl3,400MHZ):δ0.50-0.65[m,6H,Si(CH2CH3)3];0,90-1.01[m,9H,Si(CH2CH3)3);1.9-2.85(m,6H);3.5-3.8(m,2H,CH2OSi);4.12(dd,1H);4.89(ddd,1H)。
GC (area normalization): a chromatographic column: DB-1; 60m 0.25mm 1.0 μm; nitrogen flow rate: 30.0 cm/sec; column temperature: maintaining at 290 deg.C for 40 min; sample inlet temperature: 250 ℃; FID detector temperature: 300 ℃; hydrogen flow rate: 40 ml/min; air flow rate: 400 ml/min; the split ratio is as follows: 50: 1; sample introduction amount: 1.0. mu.l.
Example 10: preparation and structure confirmation of disubstituted impurity ((-) -Corey Lactone primary alcohol and secondary alcohol double protection)
(-) -Corey Lactone (2.0g,11.62mmol) and dried pyridine (20.0ml) are put into a 50ml three-necked bottle, triethylchlorosilane (4.0g,26.72mmol) is added at room temperature, the temperature is raised to 60 ℃, stirring is carried out for one hour, 40ml of water is added into reaction liquid for dilution, 50ml of dichloromethane is extracted, anhydrous sodium sulfate is added into extract liquid for drying, filtering is carried out, filtrate is evaporated to dryness, and the obtained oily substance is purified by column chromatography (eluent: n-hexane, ethyl acetate, 7:3) to obtain 4.3g of colorless oily product (disubstituted impurity), the yield is 93%, and GC is 99.45%.
MS(Q-TOF micro ESI+):423(M+Na),823(2M+Na)
1H-NMR(CDCl3,400MHZ):δ0.50-0.65[m,12H,2Si(CH2CH3)3];0,90-1.01[m,18H,2Si(CH2CH3)3);1.86-2.81(m,6H);3.48(m,2H,CH2OSi);4.10(dd,1H);4.90(ddd,1H)。
GC (area normalization): a chromatographic column: DB-1 column (60m 0.25mm 1.0 m); nitrogen flow rate: 30.0 cm/sec; column temperature: maintaining at 290 deg.C for 40 min; sample inlet temperature: 250 ℃; FID detector temperature: 300 ℃; hydrogen flow rate: 40 ml/min; air flow rate: 400 ml/min; air flow rate: 400 ml/min; the split ratio is as follows: 50: 1; sample introduction amount: 1.0. mu.l.
All documents referred to herein are incorporated by reference into this application as if each were individually incorporated by reference. Furthermore, it should be understood that various changes and modifications of the present invention can be made by those skilled in the art after reading the above teachings of the present invention, and these equivalents also fall within the scope of the present invention as defined by the appended claims.