Method for refining chiral alcohol
阅读说明：本技术 手性醇的精制方法 (Method for refining chiral alcohol ) 是由 徐亮 李彦雄 蒙发明 孙悦晋 陈清华 于 2020-12-23 设计创作，主要内容包括：本发明涉及式(I)所示手性醇的精制方法,包括以下步骤：提供式(I)所示手性醇的粗品；采用精制溶剂对所述式(I)所示手性醇的粗品进行精制,制得式(I)所示手性醇的精制品；其中,所述精制溶剂选自乙醚、正庚烷和甲基叔丁基醚、异丙醚中至少一种；上述手性醇的精制方法,能够在保证手性醇的产率的基础上,将工艺杂质的残留量控制在0.3％以下。且该精制方法简单,无需特殊仪器设备,也无需特殊操作技巧,故特别适用于工业生产应用。(The invention relates to a refining method of chiral alcohol shown in formula (I), which comprises the following steps: providing a crude product of chiral alcohol shown in formula (I); refining the crude chiral alcohol shown in the formula (I) by using a refining solvent to obtain a refined product of the chiral alcohol shown in the formula (I); wherein the refined solvent is at least one selected from diethyl ether, n-heptane, methyl tert-butyl ether and isopropyl ether;)
1. A method for refining chiral alcohol shown in formula (I) is characterized by comprising the following steps:
providing a crude product of chiral alcohol shown in formula (I);
refining the crude chiral alcohol shown in the formula (I) by using a refining solvent to obtain a refined product of the chiral alcohol shown in the formula (I); wherein the refined solvent is at least one selected from diethyl ether, n-heptane, methyl tert-butyl ether and isopropyl ether;
R1and R2Each independently selected from: halogen, cyano, nitro, C substituted by halogen1-4Alkyl, C substituted by cyano1-4Alkyl or C substituted by nitro1-4An alkyl group;
R3is C1-8An alkyl group.
2. The purification process according to claim 1, wherein R is1And R2Are all trifluoromethyl; r3Is methyl.
3. The purification process according to claim 2, wherein the purification solvent is selected from isopropyl ethers.
4. The purification process according to any one of claims 1 to 3, wherein 0.1 to 5mL of the purification solvent is added per 1g of the crude chiral alcohol represented by the formula (I).
5. The purification process according to any one of claims 1 to 3, wherein in the purification step, the crude chiral alcohol represented by the formula (I) is recrystallized by cooling crystallization using the purification solvent.
6. The refining process of claim 5, wherein the step of refining comprises the steps of:
mixing the crude product of chiral alcohol shown in formula (I) with refined solvent, and dissolving at 50-60 deg.C;
cooling to 0-5 deg.C, standing, separating crystal, collecting crystal, and drying to obtain refined product of chiral alcohol shown in formula (I).
7. The refining method according to any one of claims 1 to 3, characterized in that the crude chiral alcohol represented by the formula (I) contains 0.01 to 10 mass% of impurities.
8. A purification method according to any one of claims 1 to 3, wherein the step of providing a crude product of the chiral alcohol represented by the formula (I) comprises the steps of:
providing a compound represented by formula (II);
and (3) carrying out asymmetric catalytic hydrogenation on the compound with the structure shown in the formula (II) to obtain a crude product of the chiral alcohol shown in the formula (I).
9. The refining method according to claim 8, wherein the catalyst used in the asymmetric catalytic hydrogenation reaction is a high-molecular-weight polymeric bis-ruthenium-bisphosphine catalyst.
10. The purification method according to claim 8, wherein the structure is represented by the following formula (A):
r is a high molecular polymer;
m is a transition metal;
x, Y are each independently a halogen radical;
represents a bisphosphine ligand;
R4is H or C1-8An alkyl group.
Technical Field
The invention relates to the technical field of compound purification, in particular to a refining method of chiral alcohol.
Background
Chiral alcohol-containing intermediates, such as aprepitant intermediates, are currently used in many drug syntheses. The intermediate is prepared by asymmetric reduction of raw materials containing ketone group to obtain chiral alcohol compound containing target chiral center. Among them, the above-mentioned type of reaction usually adopts asymmetric catalytic hydrogenation method, but at present most of the catalysts adopted by asymmetric catalytic hydrogenation method have low stereoselectivity, low product conversion rate and low crude product purity. Based on this, this department has developed a series of solid phase catalyst, improves the stereoselectivity of reaction on the one hand, and on the other hand, reduces the metallic impurity that remains in the product, reduces the follow-up purification degree of difficulty. However, in the research of the technicians, even if a high-efficiency catalyst is adopted, the conventional solvent washing or recrystallization treatment method is adopted, the raw material residue still reaches more than 0.9%, the residue of other impurities also reaches more than 0.5%, and after the purity is improved to a certain degree, even if the purification is carried out for many times, the purity improvement effect is still not obvious, the requirement that the impurity residue is below 0.5% cannot be met, and the yield is greatly reduced due to the purification treatment for many times, so that the requirement of modern industrial production cannot be met.
Disclosure of Invention
Therefore, it is necessary to provide a method for refining chiral alcohol to improve the purity of chiral alcohol on the basis of ensuring the yield of chiral alcohol.
A method for refining chiral alcohol shown in formula (I) comprises the following steps:
providing a crude product of chiral alcohol shown in formula (I);
refining the crude chiral alcohol shown in the formula (I) by using a refining solvent to obtain a refined product of the chiral alcohol shown in the formula (I); wherein the refined solvent is at least one selected from diethyl ether, n-heptane, methyl tert-butyl ether and isopropyl ether;
R1and R2Each independently selected from: halogen, cyano, nitro, halogen substituted C1-4Alkyl, cyano-substituted C1-4Alkyl or nitro substituted C1-4An alkyl group;
R3is C1-8An alkyl group.
In one embodiment, R1And R2Are all trifluoromethyl; r3Is methyl.
In one embodiment, the refining solvent is selected from isopropyl ether.
In one embodiment, 0.1-5mL of the refined solvent is added per 1g of the crude chiral alcohol of formula (I).
In one embodiment, in the refining step, the crude chiral alcohol shown in formula (I) is recrystallized by using the refining solvent and cooling crystallization.
In one embodiment, the refining step comprises the steps of:
mixing the crude product of chiral alcohol shown in formula (I) with refined solvent, and dissolving at 50-60 deg.C;
cooling to 0-5 deg.C, standing, separating crystal, collecting crystal, and drying to obtain refined product of chiral alcohol shown in formula (I).
In one embodiment, in the crude product of the chiral alcohol shown in the formula (I), the impurity content is 0.01-10% by mass.
In one embodiment, the step of providing the crude chiral alcohol of formula (I) comprises the following steps:
providing a compound represented by formula (II);
and (3) carrying out asymmetric catalytic hydrogenation on the compound with the structure shown in the formula (II) to obtain a crude product of the chiral alcohol shown in the formula (I).
In one embodiment, in the asymmetric catalytic hydrogenation reaction, the catalyst used is a polymeric bis (ruthenium bis (phosphonitrogen)) catalyst.
In one embodiment, the catalyst used in the asymmetric catalytic hydrogenation reaction has a structure represented by the following formula (a):
r is a high molecular polymer;
m is a transition metal;
x, Y are each independently a halogen radical;
n is an integer of 12 to 65;
represents a bisphosphine ligand;
R4is H or C1-8An alkyl group.
In one embodiment, the catalyst used in the asymmetric catalytic hydrogenation reaction has a structure represented by the following formula (C):
n is 12, 14, 15 or 16.
Has the advantages that:
the skilled person in the present application finds in the study: the main impurities affecting the purity of the final product are the compound shown in the formula (II) and/or the enantiomer of the intermediate shown in the formula (I), and the enantiomer is similar to the intermediate shown in the formula (I), so that the compound and the intermediate are difficult to separate by the traditional method, and the purity of the final product cannot meet the requirement. Based on this, through a lot of research, the present inventors have effectively improved the purity of the compound represented by formula (I) by purifying the crude product of the compound represented by formula (I) with the above-mentioned refined solvent, and can control the residual amount of process impurities to be below 0.3% while maintaining the product to have a higher yield. The refining method is simple, does not need special instruments and equipment, does not need special operation skills, and is particularly suitable for industrial production application.
Detailed Description
In order that the invention may be more fully understood, a more particular description of the invention will now be rendered by reference to specific embodiments thereof that are illustrated in the appended drawings. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
Term(s) for
Unless otherwise stated or contradicted, terms or phrases used herein have the following meanings:
the term "alkyl" refers to a saturated hydrocarbon containing a primary (normal) carbon atom, or a secondary carbon atom, or a tertiary carbon atom, or a quaternary carbon atom, or a combination thereof. Phrases containing the term, e.g., "C1-8The "alkyl group" means an alkyl group having 1 to 8 carbon atoms and "C1-6The "alkyl group" means an alkyl group having 1 to 6 carbon atoms and "C1-4The alkyl group means an alkyl group having 1 to 4 carbon atoms. Suitable examples include, but are not limited to: methyl (Me, -CH)3) Ethyl (Et-CH)2CH3) 1-propyl (n-Pr, n-propyl, -CH)2CH2CH3) 2-propyl (i-Pr, i-propyl, -CH (CH)3)2) 1-butyl (n-Bu, n-butyl, -CH)2CH2CH2CH3) 2-methyl-1-propyl (i-Bu, i-butyl, -CH)2CH(CH3)2) 2-butyl (s-Bu, s-butyl, -CH (CH)3)CH2CH3) 2-methyl-2-propyl (t-Bu, t-butyl, -C (CH)3)3) 1-pentyl (n-pentyl, -CH)2CH2CH2CH2CH3) 2-pentyl (-CH (CH3) CH2CH2CH3), 3-pentyl (-CH (CH)2CH3)2) 2-methyl-2-butyl (-C (CH)3)2CH2CH3) 3-methyl-2-Butyl (-CH (CH)3)CH(CH3)2) 3-methyl-1-butyl (-CH)2CH2CH(CH3)2) 2-methyl-1-butyl (-CH)2CH(CH3)CH2CH3) 1-hexyl (-CH)2CH2CH2CH2CH2CH3) 2-hexyl (-CH (CH)3)CH2CH2CH2CH3) 3-hexyl (-CH (CH)2CH3)(CH2CH2CH3) 2-methyl-2-pentyl (-C (CH))3)2CH2CH2CH3) 3-methyl-2-pentyl (-CH (CH)3)CH(CH3)CH2CH3) 4-methyl-2-pentyl (-CH (CH)3)CH2CH(CH3)2) 3-methyl-3-pentyl (-C (CH)3)(CH2CH3)2) 2-methyl-3-pentyl (-CH (CH)2CH3)CH(CH3)2) 2, 3-dimethyl-2-butyl (-C (CH)3)2CH(CH3)2) 3, 3-dimethyl-2-butyl (-CH (CH)3)C(CH3)3And octyl (- (CH)2)7CH3)。
The term "cycloalkyl" refers to a non-aromatic hydrocarbon containing ring carbon atoms and may be a monocycloalkyl, or spirocycloalkyl, or bridged cycloalkyl. Phrases encompassing this term, such as "3-8 membered cycloalkyl" refer to cycloalkyl groups containing 3 to 8 carbon atoms. Suitable examples include, but are not limited to: cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl and cycloheptyl. In addition, "cycloalkyl" may also contain one or more double bonds, and representative examples of cycloalkyl groups containing a double bond include cyclopentenyl, cyclohexenyl, cyclohexadienyl, and cyclobutadienyl.
"aryl" refers to an aromatic hydrocarbon group derived by removing one hydrogen atom from the aromatic ring compound and may be a monocyclic aryl group, or a fused ring aryl group, or a polycyclic aryl group, at least one of which is an aromatic ring system for polycyclic ring species. For example, "5-10 membered aryl" refers to aryl groups containing 5 to 10 ring atoms. Suitable examples include, but are not limited to: benzene, biphenyl, naphthalene, anthracene, phenanthrene, perylene, triphenylene, and derivatives thereof.
"heteroaryl" means that on the basis of an aryl at least one carbon atom is replaced by a non-carbon atom which may be a N atom, an O atom, an S atom, etc. For example, "5-10 membered heteroaryl" refers to heteroaryl groups containing 5 to 10 ring atoms. Suitable examples include, but are not limited to: furan, benzofuran, thiophene, benzothiophene, pyrrole, pyrazole, triazole, imidazole, oxazole, oxadiazole, thiazole, tetrazole, indole, carbazole, pyrroloimidazole, pyrrolopyrrole, thienopyrrole, thienothiophene, furopyrrole, furofuran, thienofuran, benzisoxazole, benzisothiazole, benzimidazole, pyridine, pyrazine, pyridazine, pyrimidine, triazine, quinoline, isoquinoline, phthalazine, quinoxaline, phenanthridine, primadine, quinazoline, and quinazolinone.
In the present invention, when the number of substituents is not specified, it is to be understood that there may be an optional number of substituents substituted, for example, fluorine atom-substituted methyl groups including monofluoromethyl group, difluoromethyl group and trifluoromethyl group.
Detailed explanation
An embodiment of the present invention provides a method for refining chiral alcohol, including the steps of:
s101: providing a crude product of a compound shown in a formula (I);
R1and R2Each independently selected from: halogen, cyano, nitro, halogen substituted C1-4Alkyl, cyano-substituted C1-4Alkyl or nitro substituted C1-4An alkyl group;
R3is C1-8An alkyl group.
Further, R1And R2Each independently selected from: halogen, cyano, nitro, halogen substituted C1-4Alkyl, cyano-substituted C1-4Alkyl or nitro substituted C1-4An alkyl group; further, R1And R2Each independently selected from: halogen, nitryl, methyl substituted by fluorine atoms, ethyl substituted by fluorine atoms, n-propyl substituted by fluorine atoms or isopropyl substituted by fluorine atoms, methyl substituted by nitryl, ethyl substituted by nitryl, n-propyl substituted by nitryl or isopropyl substituted by nitryl; further, R1And R2Each independently selected from: fluorine, chlorine, bromine, nitro, monofluoromethyl, difluoromethyl or trifluoromethyl; further, R1And R2Are all trifluoromethyl.
Further, R3Is methyl, ethyl, n-propyl, isopropyl, 1-butyl, 2-methyl-1-propyl, 2-butyl or 2-methyl-2-propyl; further, R3Is methyl.
Further, R1And R2Are all trifluoromethyl, and R3Is methyl.
It is understood that the crude chiral alcohol of formula (I) can be prepared by conventional methods, and is understood to be within the scope of the present invention.
Further, in the step 101, in the crude product of the chiral alcohol shown in the formula (I), the mass percentage of impurities is 0.01% -20%; furthermore, the mass percentage of the impurities is 0.01-10%; furthermore, the mass percentage of the impurities is 0.05-8%; furthermore, the mass percentage of the impurities is 0.05-5%; furthermore, the mass percentage of the impurities is 0.05-3%.
Further, at least one impurity of the following structure is included:
R1、R2and R3Is as defined above.
Further, it is preferable to prepare the compound represented by the formula (I) by the following method:
s1011: providing a compound with a structure shown in a formula (II);
the structural compound represented by the formula (II) may be obtained by commercially available raw materials or by conventional synthesis methods, and is not particularly limited herein.
S1012: and (3) carrying out asymmetric catalytic hydrogenation on the compound with the structure shown in the formula (II) to obtain a crude product of the compound shown in the formula (I).
Further, in the asymmetric catalytic hydrogenation reaction, the adopted catalyst is a high-molecular polymerization diphosphine dinitrogen ruthenium catalyst; further, in the asymmetric catalytic hydrogenation reaction, the adopted catalyst is a solid-phase chiral catalyst; further, in the asymmetric catalytic hydrogenation reaction, the catalyst used has a structure represented by the formula (A):
r is a high molecular polymer;
m is a transition metal;
x, Y are each independently halogen;
represents a bisphosphine ligand;
R4is H or C1-8An alkyl group.
Further, the high molecular polymer is selected from: cellulose, starch, hydroxy acrylate, polyethylene glycol, polyethylene terephthalate, polybutylene terephthalate, polycarbonate, polylactic acid, or polybutylene succinate.
Further, in the asymmetric catalytic hydrogenation reaction, the catalyst used has a structure represented by the following formula (B):
n is an integer of 12 to 65;
the catalyst introduces polyethylene glycol with a specific chain length on a molecule, so that on one hand, the catalyst is guided by the long chain with the specific chain length to assist the catalytic reaction of the catalyst, so as to improve the catalytic activity, and further achieve the purpose of improving the asymmetric conversion rate; on the other hand, due to the existence of polyethylene glycol, the catalyst can be subjected to solid phase, and due to the existence of the molecular chain, the interaction between the heavy metal ions and the catalyst is improved, the metal ions are prevented from entering a reaction system, the risk of heavy metal residue is reduced, the catalyst is simple in post-treatment, only simple in suction filtration and separation, high in recovery rate and suitable for industrial production.
In addition, the catalyst is adopted for catalytic reaction, so that the purity of the obtained reaction liquid is high, the difficulty of subsequent purification and separation can be effectively reduced, and a refined product with the impurity content of less than 0.3 percent can be simply and efficiently obtained by combining the catalyst with a subsequent refining method.
In the structures shown in formula (A) and formula (B) "Represents a bisphosphine ligand, and the specific type of bisphosphine ligand is not particularly limited, and may be BINAP or Diop; further, the bisphosphate ligand is BINAP.
Further, X and Y are the same; further, X and Y are both chlorine;
further, R4Is H or C1-4An alkyl group; further, R4Is methyl to improve asymmetric conversion.
Further, n is 12, 13, 14, 15, 16, 17, 18, 19 or 20; further, n is 12, 13, 14, 15 or 16.
Further, the catalyst employed in the asymmetric catalytic hydrogenation reaction in step S1012 has a structure represented by the following formula (C):
the catalyst has stronger selectivity to the substrate of the invention, and can effectively improve the asymmetric conversion rate.
Further, step S1012 includes the steps of:
mixing a structural compound shown in a formula (II), alkali, a catalyst and a solvent, reacting in a hydrogen atmosphere, and concentrating a reaction solution after the reaction is finished to obtain a crude product of chiral alcohol shown in the formula (I).
Further, the base is selected from: one or more of potassium tert-butoxide, potassium ethoxide and sodium ethoxide; still further, the base is selected from potassium tert-butoxide; further, the solvent is selected from: one or more of ethanol, methanol, isopropanol, toluene, dichloromethane, and cyclohexane; still further, the solvent is selected from toluene.
Further, in the asymmetric catalytic hydrogenation reaction, the pressure is 5-45 atm; further, the temperature in the asymmetric catalytic reaction is 10 ℃ to 60 ℃, and further, the temperature in the catalytic hydrogenation reaction is 25 ℃ to 45 ℃.
Further, in the above asymmetric catalytic hydrogenation reaction, the mass of the catalyst is 0.1% to 0.3% of the mass of the structural compound represented by the formula (II). Further, in the above asymmetric catalytic reaction, 1L to 2L of a solvent is added per 100g of the compound having the structure represented by the formula (II).
In addition, the reaction time of the asymmetric catalytic hydrogenation is not particularly limited, and the reaction can be monitored by a TCL plate, and after the reaction is finished, the reaction can be treated according to conventional post-treatment.
S102: refining the crude chiral alcohol shown in the formula (I) by using a refining solvent to prepare a refined product of the chiral alcohol shown in the formula (I); wherein the refined solvent is at least one selected from diethyl ether, n-heptane, methyl tert-butyl ether, and isopropyl ether.
Further, in step S102, isopropyl ether is used as the purification solvent.
Further, in step S102, 0.1 to 5mL of the purified solvent is added per 1g of the compound represented by the formula (I); further, in step S102, 0.5 to 3mL of the purified solvent is added per 1g of the compound represented by the formula (I); further, in step S102, 1 to 2.5mL of the purified solvent is added per 1g of the compound represented by the formula (I).
Further, in step S102, the crude compound represented by formula (I) is recrystallized by cooling crystallization using a purified solvent.
Further, in step S102, the refining step includes the steps of:
s1021: mixing the compound shown in the formula (I) with a refined solvent, and dissolving at 50-60 ℃;
s1022: cooling to 0-5 deg.C, standing, separating crystal, collecting crystal, and drying to obtain refined product of compound shown in formula (I).
Further, in step S1022, the temperature of the mixed solution is gradually decreased to 0-5 ℃.
Further, in the drying step, drying is performed at a temperature of 25 ℃ to 40 ℃ under reduced pressure.
By adopting the refined solvent to purify the crude product of the compound shown in the formula (I), the purity of the compound shown in the formula (I) can be effectively improved, and the residual quantity of process impurities can be controlled below 0.3% on the basis of keeping a higher yield of the product. The refining method is simple, does not need special instruments and equipment, does not need special operation skills, and is particularly suitable for industrial production application.
The present invention will be described below with reference to specific examples.
The catalysts used for the asymmetric catalytic reaction in the following examples are:
wherein n is 12.
Example 1
(1) Synthesis of crude product
In an autoclave, under the argon atmosphere, 1000g of compound 1 is added from a charging port, 15L of toluene is added to fully dissolve the raw materials, the raw materials are fully stirred, argon is continuously introduced to carry out bubbling degassing, the bubbling is carried out for 1 hour continuously, and the degassing is finished. 2g of catalyst was added to the addition port and the addition port was quickly closed. Replacing argon with hydrogen, slowly introducing hydrogen to 3.0Mpa, and closing the inflation valve. The reaction is carried out at 25-40 ℃ with rapid stirring. When the pressure drops to a level where it remains constant, the reaction is deemed to have stopped. Sampling and liquid phase analysis are carried out to confirm the conversion rate. After the reaction is finished, the system is filtered and concentrated to prepare a crude product with the purity (HPLC) of 96.1 percent and the chirality of 97 percent.
(2) Refining treatment
And (2) adding the crude product (200g) of the compound 2 obtained in the step (1) into 400ml of isopropyl ether, heating to 50-60 ℃ to dissolve the solid, cooling to 0-5 ℃ to crystallize for 1h, performing suction filtration, and drying at 35 ℃ under reduced pressure to obtain a refined product.
Example 2
(1) Synthesis of crude product
In an autoclave, under the argon atmosphere, 1000g of compound 1 is added from a charging port, 15L of toluene is added to fully dissolve the raw materials, the raw materials are fully stirred, argon is continuously introduced to carry out bubbling degassing, the bubbling is carried out for 1 hour continuously, and the degassing is finished. 2g of catalyst was added to the addition port and the addition port was quickly closed. Replacing argon with hydrogen, slowly introducing hydrogen to 3.0Mpa, and closing the inflation valve. The reaction is carried out at 25-40 ℃ with rapid stirring. When the pressure drops to a level where it remains constant, the reaction is deemed to have stopped. Sampling and liquid phase analysis are carried out to confirm the conversion rate. After the reaction is finished, the system is filtered and concentrated to prepare a crude product with the purity (HPLC) of 96.1 percent and the chirality of 97 percent.
(2) Refining treatment
And (2) adding the crude product (200g) of the compound 2 obtained in the step (1) into 400ml of diethyl ether, heating to 50-60 ℃ to dissolve the solid, cooling to 0-5 ℃ to crystallize for 1h, performing suction filtration, and drying at 35 ℃ under reduced pressure to obtain a refined product.
Example 3
(1) Synthesis of crude product
In an autoclave, under the argon atmosphere, 1000g of compound 1 is added from a charging port, 15L of toluene is added to fully dissolve the raw materials, the raw materials are fully stirred, argon is continuously introduced to carry out bubbling degassing, the bubbling is carried out for 1 hour continuously, and the degassing is finished. 2g of catalyst was added to the addition port and the addition port was quickly closed. Replacing argon with hydrogen, slowly introducing hydrogen to 3.0Mpa, and closing the inflation valve. The reaction is carried out at 25-40 ℃ with rapid stirring. When the pressure drops to a level where it remains constant, the reaction is deemed to have stopped. Sampling and liquid phase analysis are carried out to confirm the conversion rate. After the reaction is finished, the system is filtered and concentrated to prepare a crude product with the purity (HPLC) of 96.1 percent and the chirality of 97 percent.
(2) Refining treatment
And (2) adding the crude product (200g) of the compound 2 obtained in the step (1) into 400ml of methyl tert-butyl ether, heating to 50-60 ℃ to dissolve the solid, cooling to 0-5 ℃ to crystallize for 1h, performing suction filtration, and drying at 35 ℃ under reduced pressure to obtain a refined product.
Example 4
(1) Synthesis of crude product
In an autoclave, under the argon atmosphere, 1000g of compound 1 is added from a charging port, 15L of toluene is added to fully dissolve the raw materials, the raw materials are fully stirred, argon is continuously introduced to carry out bubbling degassing, the bubbling is carried out for 1 hour continuously, and the degassing is finished. 2g of catalyst was added to the addition port and the addition port was quickly closed. Replacing argon with hydrogen, slowly introducing hydrogen to 3.0Mpa, and closing the inflation valve. The reaction is carried out at 25-40 ℃ with rapid stirring. When the pressure drops to a level where it remains constant, the reaction is deemed to have stopped. Sampling and liquid phase analysis are carried out to confirm the conversion rate. After the reaction is finished, the system is filtered and concentrated to prepare a crude product with the purity (HPLC) of 96.1 percent and the chirality of 97 percent.
(2) Refining treatment
And (2) adding the crude product (200g) of the compound 2 obtained in the step (1) into 400ml of n-heptane, heating to 50-60 ℃ to dissolve the solid, cooling to 0-5 ℃ to crystallize for 1h, performing suction filtration, and drying under reduced pressure at 35 ℃ to obtain a refined product.
Example 5
(1) Synthesis of crude product
In an autoclave, under the argon atmosphere, 1000g of compound 1 is added from a charging port, 15L of toluene is added to fully dissolve the raw materials, the raw materials are fully stirred, argon is continuously introduced to carry out bubbling degassing, the bubbling is carried out for 1 hour continuously, and the degassing is finished. 2g of catalyst was added to the addition port and the addition port was quickly closed. Replacing argon with hydrogen, slowly introducing hydrogen to 3.0Mpa, and closing the inflation valve. The reaction is carried out at 25-40 ℃ with rapid stirring. When the pressure drops to a level where it remains constant, the reaction is deemed to have stopped. Sampling and liquid phase analysis are carried out to confirm the conversion rate. After the reaction is finished, the system is filtered and concentrated to prepare a crude product with the purity (HPLC) of 96.1 percent and the chirality of 97 percent.
(2) Refining treatment
And (2) adding the crude product (200g) of the compound 2 obtained in the step (1) into 200mL of n-heptane and 200mL of isopropyl ether, heating to 50-60 ℃ to dissolve the solid, cooling to 0-5 ℃ to crystallize for 1h, performing suction filtration, and performing reduced pressure drying at 35 ℃ to obtain a refined product.
Comparative example 1
(1) Synthesis of crude product
In an autoclave, under the argon atmosphere, 1000g of compound 1 is added from a charging port, 15L of toluene is added to fully dissolve the raw materials, the raw materials are fully stirred, argon is continuously introduced to carry out bubbling degassing, the bubbling is carried out for 1 hour continuously, and the degassing is finished. 2g of catalyst was added to the addition port and the addition port was quickly closed. Replacing argon with hydrogen, slowly introducing hydrogen to 3.0Mpa, and closing the inflation valve. The reaction is carried out at 25-40 ℃ with rapid stirring. When the pressure drops to a level where it remains constant, the reaction is deemed to have stopped. Sampling and liquid phase analysis are carried out to confirm the conversion rate. After the reaction is finished, the system is filtered and concentrated to prepare a crude product with the purity (HPLC) of 96.1 percent and the chirality of 97 percent.
(2) Refining treatment
And (2) adding the crude product (200g) of the compound 2 obtained in the step (1) into 400ml of cyclohexane, heating to 50-60 ℃ to dissolve the solid, cooling to 0-5 ℃ to crystallize for 1h, performing suction filtration, and drying at 35 ℃ under reduced pressure to obtain a refined product.
Test results
The above examples 1 to 5 and comparative examples 1 to 5 were tested for yield, purity and maximum single impurity, and the test results are shown in the following table 1:
TABLE 1
As can be seen from Table 1, the purified solvents of examples 1-5 can make the purity (HPLC) and chiral purity of the target product reach 99.5% or more, the yield is 90% or more, and the single impurity content is controlled to be 0.05% or less, which meets the requirements of industrial production.
The technical features of the embodiments described above may be arbitrarily combined, and for the sake of brevity, all possible combinations of the technical features in the embodiments described above are not described, but should be considered as being within the scope of the present specification as long as there is no contradiction between the combinations of the technical features.
The above-mentioned embodiments only express several embodiments of the present invention, and the description thereof is more specific and detailed, but not construed as limiting the scope of the invention. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the inventive concept, which falls within the scope of the present invention. Therefore, the protection scope of the present patent shall be subject to the appended claims.
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