Background
The chemical name of the Raltegravir Potassium is N- (2- (4- (4-fluorobenzylcarbamoyl) -5-hydroxy-1-methyl-6-oxo-1, 6-dihydropyrimidin-2-yl) propan-2-yl) -5-methyl-1, 3, 4-oxadiazole-2-carboxamide Potassium salt, the trade name of which is Isentress, developed by Merck company in America, approved by FDA on the market at 10 months of 2007, and is the first HIV integrase inhibitor applied to clinic in the world and used for treating acquired immunodeficiency syndrome (HIV).
Latirasvir compounds are disclosed in patent WO03035077 and methods for their synthesis are disclosed.
Patent WO 200606060730 discloses crystal form 1, crystal form 2 and crystal form 3 of blatiramer potassium. Wherein, the crystal form 1 is an anhydrate, the X-ray powder diffraction shows that the 2 theta value has characteristic peaks at 5.9 degrees, 12.5 degrees, 20.0 degrees, 20.6 degrees and 25.6 degrees, and the differential scanning calorimetry curve shows that the crystal form has an endothermic peak at 279 ℃; the crystal form 2 is a hydrated crystal sylvite form, the X-ray powder diffraction shows that the 2 theta value has characteristic peaks at 7.9 degrees, 13.8 degrees, 15.7 degrees, 24.5 degrees and 31.5 degrees, and the differential scanning calorimetry curve shows that the crystal form has two wide endothermic peaks at 146 ℃, 239 ℃ and a sharp absorption peak at 276 ℃; the crystal form 3 is also an anhydrate form of the potassium raltegravir, the 2 theta values of the crystal form 3 have characteristic peaks at 7.4 degrees, 7.8 degrees, 12.3 degrees, 21.6 degrees and 64.7 degrees as shown by X-ray powder diffraction, and a differential scanning calorimetry curve shows that the crystal form has a single endothermic peak at 284 ℃.
The preparation of the crystal form 3 in the patent requires that amorphous potassium salt is obtained firstly at-78 ℃, and then the amorphous potassium salt is crystallized in an ethanol solvent. The reaction conditions are harsh, the operation is complex, and industrialization is not easy to realize.
Patent WO2017001996 reports a preparation method of a crystal form 3 of raltegravir potassium, which is implemented according to the patent method, and the degradation impurity E (structure shown below) in the obtained raltegravir potassium product exceeds the product quality limit, and is not easy to refine, and the obtained product is a small amount of mixed crystal containing a crystal form 1.
Patent WO2018051239 also reports a process for the preparation of crystalline form 3 of raltegravir potassium, in which a ketone solvent is used. As is known, the reaction of ketone solvent under alkaline condition can easily produce isopropylidene acetone impurity, which is genotoxic impurity and is difficult to control in product limit.
The crystal form 1 and the crystal form 3 of the latrevir potassium are both anhydrous crystal forms, and the experimental data of the patent WO2018051239 show that the crystal form 3 has good chemical stability and crystal form stability, and meanwhile, the solubility experiment shows that the crystal form 3 has better water solubility than the crystal form 1, so that the crystal form 3 is a good choice for developing a latrevir potassium preparation. Therefore, the preparation process of the crystal form 3, which is stable in development and simple in operation, has the product quality meeting the quality standard requirements of the bulk drugs and can be industrially implemented, can provide more choices for the development of the preparation form of the lattiravir potassium and meets the market demand of the product.
Disclosure of Invention
The existing preparation method of the crystal form 3 of the raltegravir potassium is harsh in reaction conditions, difficult to implement in production process, or easy to generate degradation impurities, and the product quality can not meet the requirements, or the generation of genotoxic impurities is increased, and the product is difficult to control, so that a new preparation method of the crystal form 3 is urgently needed to be developed to meet the requirements of the existing market on the development of various preparation forms of the raltegravir potassium.
The invention provides a novel preparation method of a crystal form 3 of the raltegravir potassium, which is stable, simple to operate, capable of meeting the quality standard requirements of raw material medicines and capable of being industrially implemented.
One aspect of the invention provides a novel preparation method of a crystal form 3 of raloxivir potassium, which is characterized by comprising the following steps
(1) Suspending Latelavir in absolute ethyl alcohol, and controlling the temperature of the system to be below 10 ℃;
(2) preparing an absolute ethyl alcohol solution of potassium hydroxide, and dissolving the absolute ethyl alcohol solution clearly for later use;
(3) dropwise adding the potassium hydroxide ethanol solution prepared in the step 2 into the Latiravi ethanol suspension, heating the reaction system to 20-30 ℃ after dropwise adding, and keeping the temperature and stirring;
(4) and carrying out suction filtration and drying to obtain the solid of the crystal form 3 of the raltegravir potassium.
Wherein the purity of the solid obtained in the step 4 is not lower than 99.6 percent, and the purity of a single impurity is not higher than 0.10 percent.
In another preferred example, the molar ratio of the potassium hydroxide to the latifoliate viras in the step (2) is 0.95-1.05: 1.
The invention has the advantages that: the novel preparation method of the crystal form 3 of the raltegravir potassium is provided, the preparation method is simple to operate, and the production conditions are easy to control; the risk that gene toxic impurities are possibly generated in the original process is avoided; through the accurate control of reaction temperature, reduce the production of degradation impurity, can fine realization powder granularity's control moreover, avoid the production of mixed crystal, reduce the suction filtration degree of difficulty simultaneously, be convenient for the industrialization implementation.
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. For reasons of brevity and description are not repeated herein.
Detailed Description
The invention will be further illustrated with reference to the following specific examples. It should be understood that these examples are for illustrative purposes only and are not intended to limit 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 percentages and parts by weight.
The test materials and reagents used in the following examples are commercially available without specific reference.
X-ray powder diffraction (XRPD):
x-ray powder diffraction instrument: brucker D8 advance X-ray powder diffractometer; the parameters of the X-ray powder diffraction are as follows: copper target
Scanning was performed at room temperature.
Voltage: 40 kilovolt (kv)
Current: 40 milliampere (mA)
Scanning mode: continuous
Scanning range: 2.0 to 50.0 DEG C
Step length: 0.020 °
The measurement time per step is 0.1 second
Differential Scanning Calorimetry (DSC):
differential Scanning Calorimetry (DSC) instrument: type TA Q2000.
Differential Scanning Calorimetry (DSC) analysis method parameters were as follows:
temperature range: 25 to 250 DEG C
Scanning speed: 10 ℃/min
Protective gas: nitrogen, 50 ml/min
Example 1
331.5g of potassium hydroxide and 12L of absolute ethyl alcohol are added into a reaction bottle, and the mixture is mechanically stirred and dissolved in a clear solution under the argon environment for later use.
2.5kg of Laticaravir free acid and 12.5L of absolute ethyl alcohol are added into a 30L reaction kettle and stirred, and the temperature of the system is controlled to be not higher than 10 ℃.
Dropwise adding the prepared potassium hydroxide ethanol solution into an ethanol solution of the Laticagrev free acid, and after dropwise adding, heating the reaction system to 20-25 ℃. Stirring for 1-2 hours under heat preservation, performing suction filtration, washing a filter cake for 1-2 times by using absolute ethyl alcohol, drying the obtained wet product at 40-45 ℃ under reduced pressure to constant weight to obtain a solid in a crystal form 3 of the raltegravir potassium, wherein an XRD spectrogram is shown in figure 1, and a DSC spectrogram is shown in figure 2 (the weight yield is 103.1%, and the purity is 99.8%).
Example 2
331.5g of potassium hydroxide and 12L of absolute ethyl alcohol are added into a reaction bottle, and the mixture is mechanically stirred and dissolved in a clear solution under the argon environment for later use.
2.5kg of Laticaravir free acid and 12.5L of absolute ethyl alcohol are added into a 30L reaction kettle and stirred, and the temperature of the system is controlled to be not higher than 10 ℃.
Dropwise adding the prepared potassium hydroxide ethanol solution into an ethanol solution of the Laticagrev free acid, and after dropwise adding, heating the reaction system to 20-25 ℃. Stirring for 1-2 hours under heat preservation, performing suction filtration, washing a filter cake for 1-2 times by using absolute ethyl alcohol, drying the obtained wet product at 40-45 ℃ under reduced pressure to constant weight to obtain a solid in a crystal form 3 of the raltegravir potassium, wherein an XRD spectrogram is shown in figure 1, and a DSC spectrogram is shown in figure 2 (the weight yield is 100.3%, and the purity is 99.7%).
Example 3
337.6g of potassium hydroxide and 12L of absolute ethyl alcohol are added into a reaction bottle, and the mixture is mechanically stirred and dissolved in a clear solution under the argon environment for standby.
2.5kg of Laticaravir free acid and 12.5L of absolute ethyl alcohol are added into a 30L reaction kettle and stirred, and the temperature of the system is controlled to be not higher than 10 ℃.
Dropwise adding the prepared potassium hydroxide ethanol solution into an ethanol solution of the Laticagrev free acid, and after dropwise adding, heating the reaction system to 20-25 ℃. Stirring for 1-2 hours under heat preservation, performing suction filtration, washing a filter cake for 1-2 times by using absolute ethyl alcohol, drying the obtained wet product at 40-45 ℃ under reduced pressure to constant weight to obtain a solid in a crystal form 3 of the raltegravir potassium, wherein an XRD spectrogram is shown in figure 1, and a DSC spectrogram is shown in figure 2 (the weight yield is 104.5%, and the purity is 99.8%).
Example 4
337.6g of potassium hydroxide and 12L of absolute ethyl alcohol are added into a reaction bottle, and the mixture is mechanically stirred and dissolved in a clear solution under the argon environment for standby.
2.5kg of Laticaravir free acid and 12.5L of absolute ethyl alcohol are added into a 30L reaction kettle and stirred, and the temperature of the system is controlled to be not higher than 10 ℃.
Dropwise adding the prepared potassium hydroxide ethanol solution into an ethanol solution of the Laticagrev free acid, and after dropwise adding, heating the reaction system to 20-25 ℃. Stirring for 1-2 hours under heat preservation, performing suction filtration, washing a filter cake for 1-2 times by using absolute ethyl alcohol, drying the obtained wet product at 40-45 ℃ under reduced pressure to constant weight to obtain a solid in a crystal form 3 of the raltegravir potassium, wherein an XRD spectrogram is shown in figure 1, and a DSC spectrogram is shown in figure 2 (the weight yield is 103.5%, and the purity is 99.6%).
Comparative example 1
331.5g of potassium hydroxide and 12L of absolute ethyl alcohol are added into a reaction bottle, and the mixture is mechanically stirred and dissolved in a clear solution under the argon environment for later use.
Adding 2.5kg of Laticaravir free acid and 12.5L of absolute ethyl alcohol into a 30L reaction kettle, stirring, and controlling the system temperature to be 15-20 ℃.
And dropwise adding the prepared potassium hydroxide ethanol solution into an ethanol solution of the Laticagrev free acid, and after dropwise adding, quickly heating the reaction system to 20-25 ℃. Stirring for 1-2 hours under heat preservation, performing suction filtration, wherein the suction filtration speed is low, and the filter cake is viscous.
Comparative example 2
331.5g of potassium hydroxide and 12L of absolute ethyl alcohol are added into a reaction bottle, and the mixture is mechanically stirred and dissolved in a clear solution under the argon environment for later use.
Adding 2.5kg of Laticaravir free acid and 12.5L of absolute ethyl alcohol into a 30L reaction kettle, stirring, and controlling the system temperature to be 20-25 ℃.
And (3) dropwise adding the prepared potassium hydroxide ethanol solution into an ethanol solution of the Laticagrev free acid, and after dropwise adding, keeping the temperature and stirring for 1-2 hours, wherein the obtained product is not filtered, thick crystal slurry and difficult to pump and filter.
The experimental result of the influencing factors of the crystal form 3 of the Latiravir obtained by the preparation method of the invention is as follows:
(1) the placing conditions are as follows: 40 ℃ and 75 +/-5% RH
Time of standing
|
Chemical purity
|
Condition of impurities
|
Stability of crystal form
|
0M
|
99.807%
|
Less than or equal to 0.10 percent of single impurity
| Form | 3
|
1M
|
99.767%
|
Less than or equal to 0.10 percent of single impurity
|
Stabilization
|
2M
|
99.669%
|
Less than or equal to 0.10 percent of single impurity
|
Stabilization
|
3M
|
99.76%
|
Less than or equal to 0.10 percent of single impurity
|
Stabilization
|
6M
|
99.7489%
|
Less than or equal to 0.10 percent of single impurity
|
Stabilization |
(2) The placing conditions are as follows: 25 ℃ and 60. + -. 5% RH
Time of standing
|
Chemical purity
|
Condition of impurities
|
Stability of crystal form
|
0M
|
99.9067%
|
Less than or equal to 0.10 percent of single impurity
| Form | 3
|
3M
|
99.9645%
|
Less than or equal to 0.10 percent of single impurity
|
Stabilization
|
6M
|
99.7274%
|
Less than or equal to 0.10 percent of single impurity
|
Stabilization
|
15M
|
99.6623%
|
Less than or equal to 0.10 percent of single impurity
|
Stabilization
|
18M
|
99.3821%
|
Less than or equal to 0.10 percent of single impurity
|
Stabilization |
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.