CN110143983A - A kind of preparation method of high stability Aldoforwe ester - Google Patents

A kind of preparation method of high stability Aldoforwe ester Download PDF

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CN110143983A
CN110143983A CN201910558431.2A CN201910558431A CN110143983A CN 110143983 A CN110143983 A CN 110143983A CN 201910558431 A CN201910558431 A CN 201910558431A CN 110143983 A CN110143983 A CN 110143983A
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compound
reaction
added
method described
crystallization
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李培
何杰
姜爱斌
王辉
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BEIJING JIMEITANG MEDICINE RESEARCH Co Ltd
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BEIJING JIMEITANG MEDICINE RESEARCH Co Ltd
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    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/547Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
    • C07F9/6561Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom containing systems of two or more relevant hetero rings condensed among themselves or condensed with a common carbocyclic ring or ring system, with or without other non-condensed hetero rings
    • C07F9/65616Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom containing systems of two or more relevant hetero rings condensed among themselves or condensed with a common carbocyclic ring or ring system, with or without other non-condensed hetero rings containing the ring system having three or more than three double bonds between ring members or between ring members and non-ring members, e.g. purine or analogs
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07BGENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B2200/00Indexing scheme relating to specific properties of organic compounds
    • C07B2200/13Crystalline forms, e.g. polymorphs

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Abstract

The invention belongs to pharmaceutical synthesis field, a kind of preparation method of high stability Aldoforwe ester, it is characterised in that the following steps are included: 1) compound 1 replaces through bromotrimethylsilane, then obtain compound 2 through NaOH aqueous hydrolysis;2) compound 2 and compound 3 are catalyzed to obtain compound 4 through triethylamine in N-Methyl pyrrolidone;3) compound 4 obtains compound 5, i.e. [[2- (6- amino -9H- purine -9- base) ethyoxyl] methyl] phosphonic acids two (pivaloyloxymethyl) ester by purification.A kind of preparation method of high stability Aldoforwe ester of the present invention, this method have the advantages that raw material drug stabilisation is good, simple production process, are suitble to large-scale commercial production.

Description

A kind of preparation method of high stability Aldoforwe ester
Technical field
The present invention relates to one kind to have hepatitis type B virus active replication evidence for treating, and with serum amino transferase The adult chronic hepatitis B patient that (ALT or AST) is persistently increased or the liver function of liver histological activity lesion is compensatory Preparation method, and in particular to the preparation method of Aldoforwe ester belongs to pharmaceutical synthesis field.
Background technique
Aldoforwe ester is the precursor of adefovirdipivoxil, plays antivirus action after being hydrolyzed to adefovirdipivoxil in vivo.A De Good fortune Wei ester is a kind of thermal instability drug, susceptible to hydrolysis.It is used for long-term treatment, the nucleotide analog of chronic hepatitis B Antiviral drugs.In addition, Aldoforwe ester has, drug resistance incidence is low, drug resistant evening time, long-term administration safety occurs Well, the features such as clinical efficiency is high.Therefore, Aldoforwe ester still has preferable market prospects.Original grinds patent CN1216062 guarantor Anhydrous crystal forms (form 1), dihydrate crystal form (form 2), methanol solvate crystal form (form 3), fumarate crystal form (shape are protected State 4), wherein anhydrous crystal forms are medicinal crystal-form, and DSC nearby has an endothermic peak at 102 DEG C, powder diffraction 2 angles θ 6.9,11.8, 15.7,17.2,20.7 nearby there are XRD spectrum peaks.
Original grinds the preparation route that patent CN1216062 describes Aldoforwe ester.The route utilizes the ([[2- (6- of compound 1 Amino -9H- purine -9- base) ethyoxyl] methyl] diethyl phosphonate) replace through bromotrimethylsilane, then hydrolyze to obtain through NaOH Compound 2 (adefovirdipivoxil), compound 2 and compound 3 (chloromethyl pivalate) are in N-Methyl pyrrolidone, triethylamine catalysis Under obtain compound 4 (Aldoforwe ester):
The synthetic route step is short, and raw material and reagent, solvent are easily obtained, easy to operate, no special installation demand, in a word The technique is more mature.But patent CN1216062 technological parameter is ground according to original, obtained bulk pharmaceutical chemicals (anhydrous crystal forms) heat is unstable It is fixed, it is susceptible to hydrolysis;Stability is poor, and the shelf-life is shorter;Partial size is smaller, and mobility is poor, is unfavorable for subsequent preparation and uses.
Summary of the invention
The present invention is directed to described problem, and inventor enhances raw material drug stabilisation, extends the bulk pharmaceutical chemicals shelf-life, explores one The preparation method of kind high stability Aldoforwe ester, this method is easy to operate, bulk pharmaceutical chemicals high income, and bulk pharmaceutical chemicals quality and technique are steady It is fixed, it is suitble to commercially produce.
The technical solution adopted by the invention is as follows:
A kind of preparation method of high stability Aldoforwe ester, characterized by comprising:
(1) compound 1 replaces in reaction reagent a through silane reagent, then obtains compound 2 through NaOH aqueous hydrolysis;
(2) compound 2 and compound 3 are catalyzed to obtain compound 4 through organic weak base in reaction dissolvent b;
(3) compound 4 passes through crystal refining, obtains compound 5, i.e. [[2- (6- amino -9H- purine -9- base) ethyoxyl] first Base] phosphonic acids two (pivaloyloxymethyl) ester.
Reaction temperature described in the step (1) is 50~80 DEG C;The reaction dissolvent a be polar non-solute or Nonpolar solvent;1 dosage of compound is 1 molar equivalent;The silane reagent dosage is 2~5 molar equivalents.
Reaction dissolvent a described in the step (1) is DMF, acetonitrile or tetrahydrofuran;The silane reagent is trimethyl Chlorosilane, bromotrimethylsilane or Iodotrimethylsilane.
Reaction temperature described in the step (2) is 40~70 DEG C;The reaction dissolvent b be polar non-solute or Nonpolar solvent;The reaction is organic weak base with alkali;The base amount is 2~6 molar equivalents;The compound 3 Dosage is 4~8 molar equivalents.
Reaction dissolvent b described in the step (2) is DMF, N-Methyl pyrrolidone;The organic weak base is triethylamine Or pyridine.
Reaction temperature described in the step (3) is 40~60 DEG C;The crystallization solvent be ethyl acetate, isopropyl ether, Acetone, methyl tertiary butyl ether(MTBE), acetone and isopropyl ether is a kind of or any two or more combinations.
The proportion of crystallization solvent described in the step (3) is compound 4: ethyl acetate or acetone: isopropyl ether or methyl- tert Butyl ether is 1:2:2, wherein the solvent water content is less than 0.1%.
Crystallization mode described in the step (3) is 35~40 DEG C of 0.1~1% crystal seeds of addition, is cooled to 25~35 DEG C of guarantors Warm crystallization, then it is cooled to 0~10 DEG C of crystallization.
It further illustrates: preferably 50~80 DEG C of reaction temperature described in the step (1), more preferable 60~70 DEG C, Reaction time 1~2 hour.
The preferred DMF of reaction dissolvent, acetonitrile, tetrahydrofuran described in the step (1), more preferable acetonitrile.
The preferred trim,ethylchlorosilane of silane reagent described in the step (1), bromotrimethylsilane, trimethyl iodine silicon Alkane, more preferable bromotrimethylsilane.
Bromotrimethylsilane dosage preferably 2~5 molar equivalents described in the step (1), more preferable 3.5 moles are worked as Amount.
Preferably 40~70 DEG C of reaction temperature described in the step (2), more preferable 50~55 DEG C, the reaction time 5~7 Hour.
Reaction dissolvent described in the step (2) is preferably DMF, N-Methyl pyrrolidone, more preferable N- methyl pyrrole Pyrrolidone.
The preferred triethylamine of reaction alkali, pyridine described in the step (2), more preferable triethylamine.
Base amount preferably 2~6 molar equivalents, more preferable 4 molar equivalent described in the step (2).
3 dosage of compound preferably 4~8 molar equivalents, more preferable 6 molar equivalent described in the step (2).
Preferably 40~60 DEG C of reaction temperature described in the step (3), more preferable 40~45 DEG C.
Reaction-crystallization solvent ethyl acetate described in the step (3) and isopropyl ether, acetone and methyl- tert fourth Base ether, acetone and isopropyl ether, more preferable acetone and methyl tertiary butyl ether(MTBE).
Preferably 35~40 DEG C 0.1~1% crystal seeds of addition of crystallization mode described in the step (3), more preferable 37~ 39 DEG C of 0.3% crystal seeds of addition.
Crystallization mode described in the step (3) is preferably cooled to 25~35 DEG C of heat preservation crystallizations, and more preferable 30~35 DEG C crystallization.
Beneficial effect
Innovation of the present invention:
The raw material drug stabilisation that the prior art obtains is poor, and the shelf-life is shorter;Partial size is smaller, and mobility is poor, is unfavorable for Subsequent preparation uses.Improvement is optimized such as to existing technique in the problem of for technique, the present invention:
1. being refined using acetone and methyl tertiary butyl ether(MTBE) to the compound 4 of preparation, dropped by the way that crystal seed and gradient is added Warm crystallization obtains big partial size Aldoforwe ester, reduces its surface area contacted with the external world, reaches preparation high stability adefovirdipivoxil The purpose of ester.
2. a pair original grinds patent CN1216062 and respectively walks all materials proportion, re-starts and investigate and be optimized.
By improving above, reduces side reaction, improve bulk pharmaceutical chemicals quality, enhance the stability of bulk pharmaceutical chemicals, be suitable for In commercially producing.
For present invention process without especial equipment requirements, no special reaction parameter is easy to operate, and 1 feather weight work is completed at present Skill verifying, meets business mass production demand, route total recovery reaches 30%~40%, and 99.9% or more purity meets internal control mark It is quasi-.
Detailed description of the invention
Fig. 1 is 2 nuclear magnetic resonance spectroscopy of compound;
Fig. 2 is 2 carbon-13 nmr spectra of compound;
Fig. 3 is 5 nuclear magnetic resonance spectroscopy of compound;
Fig. 4 is 5 carbon-13 nmr spectra of compound;
Fig. 5 is 1 compound of embodiment, 5 differential calorimetric (DSC);
Fig. 6 is 1 compound of embodiment, 5 powder diffraction;
Fig. 7 is 1 compound of embodiment, 5 infrared spectrum.
Fig. 8 is 1 compound of comparative example, 5 differential calorimetric (DSC);
Fig. 9 is 1 compound of comparative example, 5 powder diffraction
Specific embodiment
Below with reference to embodiment and specific embodiment, the present invention is described in further detail.But this should not be understood It is only limitted to embodiment below to invent the range of the theme, it is all that this hair is belonged to based on the technology that the content of present invention is realized Bright range.
Embodiment 1:
Acetonitrile 5.20kg (2w/w) is added into 50L reaction kettle, is added with stirring 1 2.60kg of compound (1eq), front three Bromide silane 4.24kg (3.5eq) is warming up to 65 ± 5 DEG C, insulation reaction 2 hours.45 ± 5 DEG C of organic phases are concentrated under reduced pressure into aneroid Body distillates, organic to be added to purified water 7.80kg (3w/w) dissolution, is warming up to 55 ± 5 DEG C and stirs 0.5 hour;To 50L reaction kettle Middle dropwise addition 30%NaOH aqueous solution tune pH to 2.5~3.5, is warming up to 75 ± 5 DEG C of insulated and stirreds 2 hours;It is cooled to 3 ± 3 DEG C of guarantors Temperature stirring 3 hours;Centrifugation, filter cake are successively washed with purified water 2.60kg (1w/w), ethyl alcohol 1.30kg (0.5w/w);It is anti-to 50L It answers in kettle and adds purified water 10.40kg (4w/w), be added with stirring filter cake, be warming up to 75 ± 5 DEG C, be beaten 2 hours;It is cooled to 3 ± 3 DEG C heat preservation 3 hours;Centrifugation, filter cake are washed with purified water 2.60kg (1w/w);Filter cake obtains compound 2 in 65 ± 5 DEG C of vacuum dryings White powder 1.86kg, yield 86.2%.1HNMR(400MHz,dDMSO) δ: 3.3898~3.4108 (d, 2H, O-CH2-P), 3.7974~3.8104 (m, 2H, O-CH2-CH2), 4.1678~4.1939 (m, 2H ,-CH2CH2-N),7.8276(s,1H,N- CH-N),8.0001(s,1H,N-CH-N-CH2)。13CNMR(400Hz,DMSO)δ:43.3421,68.2786,69.9573, 117.7349,142.6915,148.2684,151.9032,154.8810 seeing attached drawing 1~2.
Saline solution is prepared: 39.00kg purified water being added into 50L kettle, is added with stirring 14.62kgNaCl.
N-Methyl pyrrolidone is added into 50L reaction kettle, is added with stirring 2 1.70kg of compound, triethylamine 2.52kg (4eq), 3 5.62kg of compound (6eq), nitrogen charging gas shielded are warming up to 50~55 DEG C, keep the temperature 5~7 hours, and HPLC monitors chemical combination 4 > 74% of object;Reaction solution is cooled to 25 ± 5 DEG C;Reaction solution is transferred in 100L turnover barrel and adds 34kg (20w/w) acetic acid second Ester, 25 ± 5 DEG C of stirring 0.5h;Filters pressing, filter cake are washed with 8.50kg ethyl acetate (5w/w), merge organic phase to 200L kettle;Have Machine is added 17.00kg purified water (10w/w), stirs 0.5h, liquid separation;Water phase is transferred in 200L kettle, adds 17.00kg ethyl acetate (10w/w) stirs 0.5h, liquid separation;Merge organic phase, add 17.00kg purified water (10w/w), stirs 0.5h, liquid separation;Organic phase Middle addition 17.00kg purified water (10w/w) stirs 0.5h, liquid separation;Organic addition 17.00kg saline solution (10w/w), stirring 0.5h, liquid separation;Organic addition 17.00kg saline solution (10w/w) stirs 0.5h, liquid separation;Organic addition 17.00kg saline solution (10w/w) stirs 0.5h, liquid separation;Organic addition 3.40kg (2w/w) anhydrous sodium sulfate, 170g (0.1w/w) active carbon, in 25 ± 5 DEG C of stirring 1h;Filters pressing, filter cake are washed with 3.40kg (2w/w) ethyl acetate;Filtrate is transferred in 200L kettle, and 40 ± 5 DEG C subtract Pressure is concentrated into about 8.5L (5v/w);It is added 15.30kg methyl tertiary butyl ether(MTBE) (9w/w), is warming up to 43 ± 3 DEG C, stir 0.5h;It is cold But to 5 ± 5 DEG C, crystallization 12h;Centrifugation, filter cake are washed with 1.70kg methyl tertiary butyl ether(MTBE) (1w/w);Filter cake is in 40 ± 5 DEG C of vacuum It is dry, obtain 4 white 1.66kg of compound, yield 53.2%.
Acetone 2.50kg (2w/w) is added into 10L four-hole bottle, is added with stirring 4 1.25kg of compound, it is warming up to 40~ 45℃;It is slowly added to methyl tertiary butyl ether(MTBE) 2.50kg (2w/w), is warming up to 40~45 DEG C, insulated and stirred 0.5h;Keep the temperature filters pressing extremely In 20L devitrification of glass kettle, 40~45 DEG C are warming up to, keeps the temperature 0.5h;Slow cooling;38 ± 1 DEG C of 0.3% crystal seeds of addition;Slowly drop Temperature keeps the temperature growing the grain 6h to 30~35 DEG C;Slow cooling keeps the temperature crystallization 12h to 5 ± 5 DEG C;Centrifugation, filter cake methyl tertiary butyl ether(MTBE) 1.25kg (1w/w) washing;Filter cake is dried in vacuo in 40 ± 5 DEG C, obtains 5 white crystalline powder 1.00kg of compound, yield 78.1%.1HNMR(400MHz,dDMSO)δ:1.1452(s,18H,-CH3), 3.9021~3.9914 (m, 4H, N-CH2-CH2-O), 4.3267~4.3529 (s, 2H, O-CH2- P), 5.5453~5.6049 (m, 4H, O-CH2-CO),7.1958(s,2H,NH2), 8.0760~8.1465 (m, 2H, N-CH-N)13CNMR(400Hz,DMSO)δ:175.9465,155.8738,152.2783, 149.4673,140.8699,118.5507,81.4563,70.4544,64.9420,63.3296,42.2869,26.3393.See Attached drawing 3~4.
It is operated according to embodiment 1, total recovery 35.8%.
Embodiment 2
DMF5.20kg (2w/w) is added into 50L reaction kettle, is added with stirring 1 2.60kg of compound (1eq), trimethyl Chlorosilane 1.72kg (2eq) is warming up to 55 ± 5 DEG C, insulation reaction 2 hours.45 ± 5 DEG C of organic phases are concentrated under reduced pressure into no liquid and evaporate Out, organic to be added to purified water 7.80kg (3w/w) dissolution, it is warming up to 55 ± 5 DEG C and stirs 0.5 hour;It is dripped into 50L reaction kettle Add 30%NaOH aqueous solution tune pH to 2.5~3.5, is warming up to 75 ± 5 DEG C of insulated and stirreds 2 hours;3 ± 3 DEG C of heat preservations are cooled to stir It mixes 3 hours;Centrifugation, filter cake are successively washed with purified water 2.60kg (1w/w), ethyl alcohol 1.30kg (0.5w/w);To 50L reaction kettle In plus purified water 10.40kg (4w/w), be added with stirring filter cake, be warming up to 75 ± 5 DEG C, be beaten 2 hours;It is cooled to 3 ± 3 DEG C of guarantors Temperature 3 hours;Centrifugation, filter cake are washed with purified water 2.60kg (1w/w);Filter cake obtains 2 white of compound in 65 ± 5 DEG C of vacuum dryings Powder 1.71kg, yield 79.2%.
Saline solution is prepared: 39.00kg purified water being added into 50L kettle, is added with stirring 14.62kgNaCl.
DMF is added into 50L reaction kettle, is added with stirring 2 1.70kg of compound, triethylamine 1.26kg (2eq), chemical combination 3 3.75kg of object (4eq), nitrogen charging gas shielded are warming up to 40~50 DEG C, keep the temperature 5~7 hours, and HPLC monitors 4 > 74% of compound; Reaction solution is cooled to 25 ± 5 DEG C;Reaction solution is transferred in 100L turnover barrel and adds 34kg (20w/w) ethyl acetate, 25 ± 5 DEG C are stirred Mix 0.5h;Filters pressing, filter cake are washed with 8.50kg ethyl acetate (5w/w), merge organic phase to 200L kettle;Organic addition 17.00kg Purified water (10w/w) stirs 0.5h, liquid separation;Water phase is transferred in 200L kettle, is added 17.00kg ethyl acetate (10w/w), stirring 0.5h, liquid separation;Merge organic phase, add 17.00kg purified water (10w/w), stirs 0.5h, liquid separation;17.00kg is added in organic phase Purified water (10w/w) stirs 0.5h, liquid separation;Organic addition 17.00kg saline solution (10w/w) stirs 0.5h, liquid separation;Organic phase Add 17.00kg saline solution (10w/w), stirs 0.5h, liquid separation;Organic addition 17.00kg saline solution (10w/w) stirs 0.5h, point Liquid;Organic addition 3.40kg (2w/w) anhydrous sodium sulfate, 170g (0.1w/w) active carbon, in 25 ± 5 DEG C of stirring 1h;Filters pressing, filter Cake is washed with 3.40kg (2w/w) ethyl acetate;Filtrate is transferred in 200L kettle, and 40 ± 5 DEG C are concentrated under reduced pressure into about 8.5L (5v/ w);It is added 15.30kg methyl tertiary butyl ether(MTBE) (9w/w), is warming up to 43 ± 3 DEG C, stir 0.5h;5 ± 5 DEG C are cooled to, crystallization 12h; Centrifugation, filter cake are washed with 1.70kg methyl tertiary butyl ether(MTBE) (1w/w);Filter cake is dried in vacuo in 40 ± 5 DEG C, obtains 4 white of compound 1.42kg, yield 45.5%.
Ethyl acetate 2.50kg (2w/w) is added into 10L four-hole bottle, is added with stirring 4 1.25kg of compound, is warming up to 40~45 DEG C;It is slowly added to isopropyl ether 2.50kg (2w/w), is warming up to 40~45 DEG C, insulated and stirred 0.5h;Filters pressing is kept the temperature to 20L In devitrification of glass kettle, 40~45 DEG C are warming up to, keeps the temperature 0.5h;Slow cooling;36 ± 1 DEG C of 0.1% crystal seeds of addition;Slow cooling is extremely 25~30 DEG C, keep the temperature growing the grain 6h;Slow cooling keeps the temperature crystallization 12h to 5 ± 5 DEG C;Centrifugation, filter cake methyl tertiary butyl ether(MTBE) 1.25kg (1w/w) washing;Filter cake is dried in vacuo in 40 ± 5 DEG C, obtains 5 white crystalline powder 0.86kg of compound, yield 68.8%.
It is operated according to embodiment 2, total recovery 24.8%.
Embodiment 3
Into 50L reaction kettle be added tetrahydrofuran 5.20kg (2w/w), be added with stirring 1 2.60kg of compound (1eq), Iodotrimethylsilane 7.92kg (5eq) is warming up to 75 ± 5 DEG C, insulation reaction 2 hours.45 ± 5 DEG C of organic phases are concentrated under reduced pressure into nothing Liquid distillates, organic to be added to purified water 7.80kg (3w/w) dissolution, is warming up to 55 ± 5 DEG C and stirs 0.5 hour;It is reacted to 50L 30%NaOH aqueous solution tune pH to 2.5~3.5 is added dropwise in kettle, is warming up to 75 ± 5 DEG C of insulated and stirreds 2 hours;It is cooled to 3 ± 3 DEG C Insulated and stirred 3 hours;Centrifugation, filter cake are successively washed with purified water 2.60kg (1w/w), ethyl alcohol 1.30kg (0.5w/w);To 50L Add purified water 10.40kg (4w/w) in reaction kettle, be added with stirring filter cake, be warming up to 75 ± 5 DEG C, is beaten 2 hours;It is cooled to 3 ± 3 DEG C keep the temperature 3 hours;Centrifugation, filter cake are washed with purified water 2.60kg (1w/w);Filter cake obtains chemical combination in 65 ± 5 DEG C of vacuum dryings 2 yellow powder 1.76kg of object, yield 81.5%.
Saline solution is prepared: 39.00kg purified water being added into 50L kettle, is added with stirring 14.62kgNaCl.
N-Methyl pyrrolidone is added into 50L reaction kettle, is added with stirring 2 1.70kg of compound, pyridine 2.95kg (6eq), 3 5.62kg of compound (6eq), nitrogen charging gas shielded are warming up to 60~70 DEG C, keep the temperature 5~7 hours, and HPLC monitors chemical combination 4 > 74% of object;Reaction solution is cooled to 25 ± 5 DEG C;Reaction solution is transferred in 100L turnover barrel and adds 34kg (20w/w) acetic acid second Ester, 25 ± 5 DEG C of stirring 0.5h;Filters pressing, filter cake are washed with 8.50kg ethyl acetate (5w/w), merge organic phase to 200L kettle;Have Machine is added 17.00kg purified water (10w/w), stirs 0.5h, liquid separation;Water phase is transferred in 200L kettle, adds 17.00kg ethyl acetate (10w/w) stirs 0.5h, liquid separation;Merge organic phase, add 17.00kg purified water (10w/w), stirs 0.5h, liquid separation;Organic phase Middle addition 17.00kg purified water (10w/w) stirs 0.5h, liquid separation;Organic addition 17.00kg saline solution (10w/w), stirring 0.5h, liquid separation;Organic addition 17.00kg saline solution (10w/w) stirs 0.5h, liquid separation;Organic addition 17.00kg saline solution (10w/w) stirs 0.5h, liquid separation;Organic addition 3.40kg (2w/w) anhydrous sodium sulfate, 170g (0.1w/w) active carbon, in 25 ± 5 DEG C of stirring 1h;Filters pressing, filter cake are washed with 3.40kg (2w/w) ethyl acetate;Filtrate is transferred in 200L kettle, and 40 ± 5 DEG C subtract Pressure is concentrated into about 8.5L (5v/w);It is added 15.30kg methyl tertiary butyl ether(MTBE) (9w/w), is warming up to 43 ± 3 DEG C, stir 0.5h;It is cold But to 5 ± 5 DEG C, crystallization 12h;Centrifugation, filter cake are washed with 1.70kg methyl tertiary butyl ether(MTBE) (1w/w);Filter cake is in 40 ± 5 DEG C of vacuum It is dry, obtain 4 white 1.46kg of compound, yield 46.8%.
Acetone 2.50kg (2w/w) is added into 10L four-hole bottle, is added with stirring 4 1.25kg of compound, it is warming up to 40~ 45℃;It is slowly added to isopropyl ether 2.50kg (2w/w), is warming up to 40~45 DEG C, insulated and stirred 0.5h;Filters pressing is kept the temperature to 20L glass In crystallization kettle, 40~45 DEG C are warming up to, keeps the temperature 0.5h;Slow cooling;38 ± 1 DEG C of 0.3% crystal seeds of addition;Slow cooling to 30~ 35 DEG C, keep the temperature growing the grain 6h;Slow cooling keeps the temperature crystallization 12h to 5 ± 5 DEG C;Centrifugation, filter cake methyl tertiary butyl ether(MTBE) 1.25kg (1w/w) washing;Filter cake is dried in vacuo in 40 ± 5 DEG C, obtains 5 white crystalline powder 0.88kg of compound, yield 70.4%.
It is operated according to embodiment 3, total recovery 26.9%.
Comparative example 1 (CN1216062):
Acetonitrile 5.20kg (2w/w) is added into 50L reaction kettle, is added with stirring 1 2.60kg of compound (1eq), front three Base iodine silane 4.24kg (3.5eq) is warming up to 65 ± 5 DEG C, insulation reaction 2 hours.45 ± 5 DEG C of organic phases are concentrated under reduced pressure into aneroid Body distillates, organic to be added to purified water 7.80kg (3w/w) dissolution, is warming up to 55 ± 5 DEG C and stirs 0.5 hour;To 50L reaction kettle Middle dropwise addition 30%NaOH aqueous solution tune pH to 2.5~3.5, is warming up to 75 ± 5 DEG C of insulated and stirreds 2 hours;It is cooled to 3 ± 3 DEG C of guarantors Temperature stirring 3 hours;Centrifugation, filter cake are successively washed with purified water 2.60kg (1w/w), ethyl alcohol 1.30kg (0.5w/w);It is anti-to 50L It answers in kettle and adds purified water 10.40kg (4w/w), be added with stirring filter cake, be warming up to 75 ± 5 DEG C, be beaten 2 hours;It is cooled to 3 ± 3 DEG C heat preservation 3 hours;Centrifugation, filter cake are washed with purified water 2.60kg (1w/w);Filter cake obtains compound 2 in 65 ± 5 DEG C of vacuum dryings White powder 1.86kg, yield 86.2%.
N-Methyl pyrrolidone is added into 50L reaction kettle, is added with stirring 2 1.70kg of compound, triethylamine 2.52kg (4eq), 3 5.62kg of compound (6eq), nitrogen charging gas shielded are warming up to 50~55 DEG C, keep the temperature 5~7 hours, and HPLC monitors chemical combination 4 > 74% of object;Reaction solution is cooled to 25 ± 5 DEG C;Reaction solution is transferred in 100L turnover barrel and adds 34kg (20w/w) isopropyl acetate Ester, 25 ± 5 DEG C of stirring 0.5h;Filters pressing, filter cake are washed with 8.50kg isopropyl acetate (5w/w), merge organic phase to 200L kettle; Organic addition 17.00kg purified water (10w/w) stirs 0.5h, liquid separation;Water phase is transferred in 200L kettle, adds 17.00kg acetic acid different Propyl ester (10w/w) stirs 0.5h, liquid separation;Merge organic phase, add 17.00kg purified water (10w/w), stirs 0.5h, liquid separation;Have 17.00kg purified water (10w/w) is added in machine phase, stirs 0.5h, liquid separation;Filtrate is transferred in 200L kettle, and 40 ± 5 DEG C of decompressions are dense It is reduced to dry;3.40kg acetone (2w/w) dissolution is added, 6.80kg (4w/w) methyl tertiary butyl ether(MTBE) is added and is warming up to 43 ± 3 DEG C, stirs Mix 0.5h;5 ± 5 DEG C are cooled to, crystallization 12h;Centrifugation, filter cake are washed with 1.70kg methyl tertiary butyl ether(MTBE) (1w/w);Filter cake is in 40 ± 5 DEG C of vacuum drying, obtain 5 white powder 1.25kg of compound, yield 40.1%.
It is operated according to comparative example 1, total recovery 34.6%.
1 sample of embodiment and 1 sample comparison result of comparative example
1 sample of embodiment is compared with 1 sample of comparative example: it is consistent that the two DSC, powder diffraction and original grind patent report, Show that the two is all five crystal types, other testing results are more consistent in addition to partial size.1 sample D of embodiment50It is 86 μm, and compares 1 sample D of example50It is 35 μm, i.e. 1 sample of embodiment is bigger than 1 sample particle diameter of comparative example;And 1 sample of embodiment is than comparative example 1 Sample flow is good.
1 sample of embodiment and 1 sample comparison result of comparative example
Study on the stability
Sample prepared by embodiment 1 and comparative example 1, carries out acceleration investigation (40 ± 2 DEG C of temperature, humidity 75 ± 5%), and Data comparison is carried out, as a result as follows:
Embodiment sample accelerates to investigate result
1 sample of embodiment is placed under acceleration conditions, and adefovir (AD) monoester accelerates March, is only risen to by 0.24% 0.34%, increase minimum;Dimer, adefovirdipivoxil are not detected.It is placed under 1 sample acceleration environment of comparative example, adefovirdipivoxil list Ester accelerates March, only rises to 0.32% by 0.11%, increases larger;Dimer impurity rises to 0.19% by 0, increases larger; Adefovirdipivoxil is not detected.Therefore 1 sample stability of embodiment, it is much higher than 1 sample of comparative example.
1 sample of embodiment has separately been carried out to the influence factor under the conditions of 40 DEG C of high temperature, high humidity 92.5%, illumination 5000lx to examine It examines, as a result as follows:
1 sample effects factor of embodiment is investigated
Test item Adefovir (AD) monoester/% Dimer/% Adefovirdipivoxil/% Total miscellaneous/%
1 sample of embodiment 0 day 0.24 - - 0.24
40 DEG C of 1 high-temperature sample of embodiment 10 days 0.23 - - 0.23
1 sample high humidity of embodiment 92.5%10 days 0.35 - - 0.38
1 sample illumination 5000lx of embodiment 10 days 0.22 - - 0.22
40 DEG C of 1 high-temperature sample of embodiment 30 days 0.27 - - 0.27
1 sample high humidity of embodiment 92.5%30 days 0.40 - - 0.44
1 sample illumination 5000lx of embodiment 30 days 0.23 - - 0.23
Chinese Pharmacopoeia limit/% 1.0 0.5 0.5 2.0
1 sample of embodiment is placed under the conditions of influence factor, and only under the conditions of high humidity 92.5%, adefovir (AD) monoester slightly increases It is long;Dimer, adefovirdipivoxil are not detected.
Therefore it is fabulous according to sample stability prepared by embodiment 1, technique is without especial equipment requirements, no special reaction parameter, It is easy to operate, 1 feather weight process certification is completed at present, meets business mass production demand.

Claims (8)

1. a kind of preparation method of high stability Aldoforwe ester, characterized by comprising:
(1) compound 1 replaces in reaction reagent a through silane reagent, then obtains compound 2 through NaOH aqueous hydrolysis;
(2) compound 2 and compound 3 are catalyzed to obtain compound 4 through organic weak base in reaction dissolvent b;
(3) compound 4 passes through crystal refining, obtains compound 5, i.e. [[2- (6- amino -9H- purine -9- base) ethyoxyl] methyl] Phosphonic acids two (pivaloyloxymethyl) ester.
2. according to the method described in claim 1, it is characterized by: reaction temperature described in the step (1) is 50 ~ 80 DEG C; The reaction dissolvent a is polar non-solute or nonpolar solvent;1 dosage of compound is 1 molar equivalent;It is described Silane reagent dosage be 2 ~ 5 molar equivalents.
3. according to the method described in claim 2, it is characterized by: reaction dissolvent a described in the step (1) is DMF, acetonitrile Or tetrahydrofuran;The silane reagent is trim,ethylchlorosilane, bromotrimethylsilane or Iodotrimethylsilane.
4. according to the method described in claim 1, it is characterized by: reaction temperature described in the step (2) is 40 ~ 70 DEG C; The reaction dissolvent b is polar non-solute or nonpolar solvent;The reaction is organic weak base with alkali;The alkali Dosage is 2 ~ 6 molar equivalents;3 dosage of compound is 4 ~ 8 molar equivalents.
5. according to the method described in claim 4, it is characterized by: reaction dissolvent b described in the step (2) is DMF, N- first Base pyrrolidones;The organic weak base is triethylamine or pyridine.
6. according to the method described in claim 1, it is characterized by: reaction temperature described in the step (3) is 40 ~ 60 DEG C; The crystallization solvent is that ethyl acetate, isopropyl ether, acetone, methyl tertiary butyl ether(MTBE), acetone and isopropyl ether are a kind of or two kinds any Combination of the above.
7. according to the method described in claim 1, it is characterized by: the proportion of crystallization solvent described in the step (3) is chemical combination Object 4: ethyl acetate or acetone: isopropyl ether or methyl tertiary butyl ether(MTBE) are 1:2:2, wherein the solvent water content is less than 0.1%.
8. according to the method described in claim 1, it is characterized by: crystallization mode described in the step (3) adds for 35 ~ 40 DEG C Enter 0.1 ~ 1% crystal seed, is cooled to 25 ~ 35 DEG C of heat preservation crystallizations, then be cooled to 0 ~ 10 DEG C of crystallization.
CN201910558431.2A 2019-06-26 2019-06-26 A kind of preparation method of high stability Aldoforwe ester Pending CN110143983A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
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CN1421449A (en) * 2002-12-04 2003-06-04 上海瑞广生化科技开发有限公司 9-[2-[[[di (trimethylacetoxyl) methyl] phosphoroso] methoxy]-ethyl] adenine crystal and its prepn and crystal application
CN1763057A (en) * 1997-07-25 2006-04-26 吉尔利德科学股份有限公司 Nucleotide analog compound
US20120238753A1 (en) * 2011-03-14 2012-09-20 Vellenki Siva Rama Prasad Process for the preparation of adefovir dipivoxil
CN104387421A (en) * 2014-11-27 2015-03-04 苏州二叶制药有限公司 Adefovir dipivoxil monohydrate and preparation method thereof

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CN1763057A (en) * 1997-07-25 2006-04-26 吉尔利德科学股份有限公司 Nucleotide analog compound
CN1421449A (en) * 2002-12-04 2003-06-04 上海瑞广生化科技开发有限公司 9-[2-[[[di (trimethylacetoxyl) methyl] phosphoroso] methoxy]-ethyl] adenine crystal and its prepn and crystal application
US20120238753A1 (en) * 2011-03-14 2012-09-20 Vellenki Siva Rama Prasad Process for the preparation of adefovir dipivoxil
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110483575A (en) * 2019-09-11 2019-11-22 北京悦康科创医药科技股份有限公司 A kind of synthetic method of Aldoforwe ester

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Application publication date: 20190820