WO2014019282A1 - Meropenem bulk drug, preparation method thereof and pharmaceutical composition containing same - Google Patents

Meropenem bulk drug, preparation method thereof and pharmaceutical composition containing same Download PDF

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Publication number
WO2014019282A1
WO2014019282A1 PCT/CN2012/082068 CN2012082068W WO2014019282A1 WO 2014019282 A1 WO2014019282 A1 WO 2014019282A1 CN 2012082068 W CN2012082068 W CN 2012082068W WO 2014019282 A1 WO2014019282 A1 WO 2014019282A1
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meropenem
impurity
mother liquor
crude
preparation
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PCT/CN2012/082068
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French (fr)
Chinese (zh)
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任鹏
管曙光
谭汉梯
唐南湘
唐秋停
向斌波
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深圳市海滨制药有限公司
新乡海滨药业有限公司
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Publication of WO2014019282A1 publication Critical patent/WO2014019282A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D477/00Heterocyclic compounds containing 1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula:, e.g. carbapenicillins, thienamycins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulphur-containing hetero ring
    • C07D477/02Preparation
    • C07D477/04Preparation by forming the ring or condensed ring systems
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/40Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having five-membered rings with one nitrogen as the only ring hetero atom, e.g. sulpiride, succinimide, tolmetin, buflomedil
    • A61K31/407Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having five-membered rings with one nitrogen as the only ring hetero atom, e.g. sulpiride, succinimide, tolmetin, buflomedil condensed with other heterocyclic ring systems, e.g. ketorolac, physostigmine
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/0012Galenical forms characterised by the site of application
    • A61K9/0019Injectable compositions; Intramuscular, intravenous, arterial, subcutaneous administration; Compositions to be administered through the skin in an invasive manner
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A61P31/04Antibacterial agents
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D477/00Heterocyclic compounds containing 1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula:, e.g. carbapenicillins, thienamycins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulphur-containing hetero ring
    • C07D477/02Preparation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D477/00Heterocyclic compounds containing 1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula:, e.g. carbapenicillins, thienamycins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulphur-containing hetero ring
    • C07D477/10Heterocyclic compounds containing 1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula:, e.g. carbapenicillins, thienamycins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulphur-containing hetero ring with hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached in position 4, and with a carbon atom having three bonds to hetero atoms with at the most one bond to halogen, e.g. an ester or nitrile radical, directly attached in position 2
    • C07D477/12Heterocyclic compounds containing 1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula:, e.g. carbapenicillins, thienamycins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulphur-containing hetero ring with hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached in position 4, and with a carbon atom having three bonds to hetero atoms with at the most one bond to halogen, e.g. an ester or nitrile radical, directly attached in position 2 with hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, attached in position 6
    • C07D477/16Heterocyclic compounds containing 1-azabicyclo [3.2.0] heptane ring systems, i.e. compounds containing a ring system of the formula:, e.g. carbapenicillins, thienamycins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulphur-containing hetero ring with hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached in position 4, and with a carbon atom having three bonds to hetero atoms with at the most one bond to halogen, e.g. an ester or nitrile radical, directly attached in position 2 with hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, attached in position 6 with hetero atoms or carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. an ester or nitrile radical, directly attached in position 3
    • C07D477/20Sulfur atoms

Definitions

  • the present invention relates to the field of pharmacy, and in particular, to a meropenem drug substance, a process for the preparation thereof, and a pharmaceutical composition comprising the meropenem drug substance.
  • API Active Pharmaceutical Ingredient
  • the API is the raw material used in the production of various preparations and is the active ingredient in the preparation.
  • the perfect definition of APIs in ICH Q7A is: Any substance or mixture of substances intended for use in the manufacture of pharmaceuticals, and when used in pharmaceuticals, becomes an active ingredient of pharmaceuticals. This substance may have pharmacological activity or other direct effects in the diagnosis, treatment, symptom relief, treatment or prevention of the disease, or may affect the function or structure of the body.
  • the Pharmacopoeia of the Chinese Pharmacopoeia 2010 edition of 606 pages on Meropenem standard specifies the relevant substances:
  • the maximum impurity peak area before and after the main peak should not be greater than 0.6 times (0.3%) of the main peak area of the control solution, other single
  • the impurity peak area shall not be greater than 0.2 times (0.1%) of the main peak area of the control solution, and the sum of the impurity peak areas shall not be greater than 2 times (1.0%) of the main peak area of the control solution.
  • Residual solvent regulations Determination of acetone, acetonitrile, dichlorodecane, ethyl acetate and tetrahydrofuran in compliance with the regulations, Chinese Pharmacopoeia 2010 edition of the second appendix P residual solvent determination method Schedule 1 common solvents and limits specified in the drug: Acetone detection limit is 0.5% (5000 ppm); acetonitrile is 0.041% (410 ppm); dichlorodecane is 0.06% (600 ppm); ethyl acetate has a detection limit of 0.5% (5000 ppm); THF has a detection limit of 0.072% (720 ppm).
  • Example 1 discloses a method for preparing meropenem trihydrate crystals, which comprises dissolving melopenem in water at 30 ° C, cooling in a water bath, and depositing a small amount of crystals. Acetone was added, stirred for 1 hour, and crystallized by filtration, washed with acetone, and dried under reduced pressure at room temperature for 2 hours to obtain crystals of meropenem trihydrate.
  • the purification method has a high yield, but the acetone residue is high, which may reach the detection limit of the acetone in the drug specified in the Chinese Pharmacopoeia 2010 Appendix 2 residual solvent determination method.
  • acetone belongs to the third type of easy-to-manufacture type of the public security organs, and it is easy to make explosives. Although acetone belongs to three types of solvents, acute or short-term studies have shown that these solvents are less toxic and the results of genotoxicity studies are negative, but there is no The long-term toxicity or carcinogenicity of these solvents, and it is hepatotoxic to humans. Long-term use of high-injection of acetone residues is undoubtedly harmful to the health of patients. For example, some cancer patients have abnormally elevated levels of urine acetone.
  • US2009264643 discloses a process for the purification of meropenem trihydrate, which involves a process of adding aqueous ammonia, citric acid to adjust the pH, and then crystallizing with tetrahydrofuran. This method is rather cumbersome, and the Chinese Pharmacopoeia 2010 edition of the second appendix residual solvent determination method specifies that the detection limit of THF in the drug is 0.072%, and this purification method is generally difficult to achieve.
  • tetrahydrofuran belongs to the second class of solvents. It is a non-genotoxic but animal carcinogenic solvent. Its health hazards are: dizziness, headache, chest tightness, chest pain, cough, fatigue, stomach pain, dry mouth, nausea, vomiting after high concentration inhalation.
  • Such symptoms may be accompanied by symptoms of eye irritation, and some patients may have liver dysfunction.
  • High dose or repeated exposure may cause hepatic fat infiltration and cell lysis; prolonged exposure may result in loss of sexual function, fertility, or kidney disease. Therefore, it should be avoided in the last step of the process, otherwise the THF residue is too high will seriously threaten the safety of meropenem injection.
  • CN201010232062.7 discloses a preparation method of meropenem trihydrate crystals, which is completely crystallized in an aqueous solution, and the filtrate is added with an organic solvent to recover meropenem.
  • the residual organic solvent in the meropenem trihydrate crystal prepared by this method is less than 0.05%, but it needs to be carried out in two steps, the yield is not high, and the recovery of the organic solvent by the organic solvent to remove the meropenem will greatly increase the organic solvent.
  • the amount of use is not conducive to environmental protection, and is not conducive to reducing costs.
  • CN201110218567.2 discloses a preparation method of meropenem, which comprises dissolving crude meropenem in 10% sodium hydroxide water, filtering after activated carbon, crystallization, and adding acetic acid B. The ester is recovered from meropenem. The method also needs to be carried out in two steps, and the yield is not high; and the recovery of meropenem from the filtrate with ethyl acetate will greatly increase the amount of ethyl acetate used, which is not conducive to environmental protection and is not conducive to cost reduction. Furthermore, Yutaka Takeuchi et al., Chem. Pharm. Bull.
  • Impurities in meropenem or any active pharmaceutical ingredient (API) are undesirable and, in extreme cases, may be harmful to patients undergoing treatment with API-containing dosage forms.
  • API active pharmaceutical ingredient
  • the 2011 Annual Report on Adverse Drug Reaction Monitoring released by the official website of the State Food and Drug Administration showed that anti-infectives in chemical products ranked first in total adverse reaction reports and serious adverse reactions reports, accounting for 51.2%. This is inconsistent with the control of impurities and solvent residues, some unclear impurities in some antibiotics, and unstable quality during long-term storage. Therefore, it is urgent to provide a lower impurity content, clear impurity conditions, and lower solvent residues.
  • a meropenem raw material and a formulation composition having stable quality and low adverse reactions.
  • the thermal stability of meropenem is poor.
  • the amount of mother liquor in the large production process is large, mainly water. If the mother liquor is directly heated, concentrated at high temperature and vacuum, the high temperature state will accelerate the degradation of meropenem, and the recovered mother liquor has a large mass. This recycling method has no practical value. If you use a new organic solvent for recycling, the amount of organic solvent that needs to be added is also large due to the large amount of water. It is also undesirable from environmental and cost considerations.
  • Nanofiltration membrane separation technology Chinese translation for “Nano Filtration is a functional filtration technique that allows solvent molecules or certain low molecular weight solutes or low-cost ions to pass through.
  • Nanofiltration membranes are semi-permeable membranes with nanoscale pores and a rejection of greater than 95%.
  • the minimum molecular weight is about 1 nm
  • the molecular weight of the retained organic matter is about 150 ⁇ 500
  • the ability to retain the soluble salt is between 2 and 98%
  • the desalting of the monovalent anion salt solution is lower than that of the high-priced anionic salt solution, mainly for removal.
  • the organic matter and color of surface water remove the hardness of groundwater, partially remove dissolved salts, concentrate juice, etc.
  • a filter mother liquor can also be obtained, which is an aqueous solution containing meropenem 1-2%, and the solution is subjected to nanofiltration. After the membrane is concentrated, the water volume is greatly reduced.
  • the weight ratio before and after the nanofiltration concentration is 5:1 - 15:1, and the concentration of meropenem after concentration is 5-20%, and the concentration is greatly increased.
  • the mother liquor after the removal of the crude meropenem contains a large amount of organic solvent, wherein the ratio of the volume of the organic solvent to the volume of water Approximately 3:1 to 6:1, these organic solvents are mainly one or more of acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol, and mercaptoethyl ketone.
  • This mother liquor is too wasteful to waste as a waste liquid. For recycling, the cost is also high. If the concentrate concentrated by the nanofiltration membrane is added to the crude mother liquor which is mainly an organic solvent, the next batch of crude meropenem can be directly crystallized, so that the organic solvent can be fully utilized.
  • the concentrated liquid obtained by concentrating the nanofiltration membrane may be added to the mother liquor in which the crude product is not precipitated after the hydrogenation filtration in the subsequent crude product preparation, and the organic solvent such as acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol, hydrazine is added dropwise according to a conventional method.
  • the organic solvent such as acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol, hydrazine is added dropwise according to a conventional method.
  • One or more of the ethyl ethyl ketones, the ratio of the volume of the adjusted organic solvent to the volume of the water is about 3:1 to 6:1, and the same can be crystallized to obtain the crude product of meropenem.
  • an object of the present invention is to determine the content of the main impurity A and the impurity B by quantitatively controlling the content of the main ingredient A and the impurity B, and to strictly control the residual solvent to provide a meropenem drug substance.
  • the raw material drug is different from the prior art, and has high purity, clear impurity condition, low solvent residue, long-term storage stability, and quality control index. Ensuring that the product is effective and safe.
  • Another object of the present invention is to provide a method for preparing a meropenem drug, which comprises refining a crude meropenem drug to obtain a meropenem drug substance and a solution containing a low concentration of meropenem, and the resulting solution is concentrated by a nanofiltration membrane. Enter the preparation of the subsequent crude meropenem.
  • the method is simple, compact and controllable, and has high yield and low cost, and has great economic advantages.
  • Still another object of the present invention is to provide a pharmaceutical composition of meropenem which has excellent stability as the active ingredient of the meropenem drug of the present invention.
  • the present invention provides a meropenem drug substance, wherein the content of meropenem in the drug substance is 98.5%-101.0%, calculated as an anhydrate; the impurity A in the related substance of the drug substance , impurity B is not more than 0.25%; any unknown single impurity is not more than 0.05%; the sum of other impurities except A and B is not more than 0.2%; acetone residue is not more than 400ppm, preferably not more than 100ppm.
  • impurity A is:
  • the present invention provides a method for preparing a meropenem drug, the method comprising: purifying and filtering the crude meropenem to obtain a mother liquor 3 and a meropenem drug substance, and the mother liquor 3 is concentrated by a nanofiltration membrane, The obtained concentrate is added to a mother liquid (mother liquid 2) which has been subjected to hydrogenation in the subsequent crude product preparation, and which has been precipitated after filtration or a mother liquid (mother liquor 1) in which no crude product is precipitated, and crystallized to obtain a crude product of meropenem.
  • the reaction process is generally: adding meropenem (or protecting meropenem concentrate), a reaction solvent, a catalyst (such as palladium carbon) to a high pressure hydrogenation reactor, removing air, introducing a hydrogen reaction, and completing the reaction, and recovering palladium carbon by filtration.
  • a mother liquor which is not precipitated as a crude product; the mother liquor is the mother liquor of the unprecipitated crude product of the present invention, referred to as mother liquor 1;
  • the mother liquor 1 is added with an organic solvent, controlled to stir and crystallize at a temperature, and filtered to obtain a mother liquor 2 and a crude product of meropenem; this mother liquor 2 is a mother liquor of the precipitated crude product of the present invention, which is referred to as a mother liquor 2 .
  • the crude product of meropenem is refined and filtered to obtain mother liquor 3 and meropenem bulk drug; mother liquor 3 is concentrated by nanofiltration to obtain nanofiltration concentrated solution, which is added to mother liquor 1 or mother liquor 2 in the subsequent crude product preparation, and then crystallized to obtain meropenem Crude.
  • This process can be recycled and controlled under the conditions of controlling the quality of meropenem crude and meropenem. It can not only greatly reduce the amount of organic solvent used, but also maximize the recovery of meropenem in mother liquor 3. Greatly improve product yield and reduce production costs.
  • the meropenem crude and seed crystals are preferably prepared according to the method described below in the present invention, or may be prepared by any of the methods of preparing meropenem in the prior art, such as the method of preparing meropenem in CN1960992A or CN200610083362.7.
  • the nanofiltration of the mother liquor was concentrated.
  • the weight ratio of the mother liquor to the obtained concentrate is 5:1 to 15:1, preferably 7:1 to 10:1;
  • the content of meropenem in the obtained concentrate is 5 to 20%, preferably 7 to 15%.
  • the total volume of the organic solvent in the system for obtaining the crude meropenem is 3:1 ⁇ 6:1; the organic solvent is selected from the group consisting of acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol and sulfhydryl. One or more of ethyl ketones.
  • the nanofiltration concentration described herein is preferably carried out in accordance with the methods of the present invention, and can be carried out by any of the methods of the prior art.
  • the membrane concentration can be concentrated by a polytetrafluoroethylene nanofiltration membrane, a polystyrene nanofiltration membrane, a polyethersulfone resin nanofiltration membrane, a composite membrane, a cellulose acetate membrane, a polyamide membrane, etc., and the nanofiltration concentrated separation device can be buy.
  • the molecular weight of the organic membrane retained by the nanofiltration membrane is about 150 to 500.
  • the molecular weight of meropenem trihydrate is 437.5, and the molecular weight of meropenem anhydrous is 383.5. Therefore, solvent molecules and water molecules can pass, and meropenem is trapped, and a nanofiltration membrane that satisfies this condition can be applied.
  • the mother liquor after concentration by nanofiltration is preferably added to the mother liquor (mother liquor 2) which has been subjected to hydrogenation after the subsequent crude product preparation by the method of the present invention, or the mother liquor (mother liquor 1) in which the crude product is not precipitated, and crystallized to obtain a crude product of meropenem. It can also be directly added to the reaction liquid, the crystallization liquid and the filtered mother liquid for preparing the crude meropenem in any method of the prior art, and simultaneously crystallized to obtain crude meropenem.
  • the nanofiltration concentrate is directly added to the aqueous solution after hydrogenation filtration in CN1960992A, and the mixed solution is added to tetrahydrofuran to obtain the crude meropenem; or the nanofiltration concentrate is directly added to the sample 2 of CN200610083362.7 to filter the perfect roperan.
  • the mother liquor of (5.1g) direct crystallization of meropenem is obtained; or the nanofiltration concentrate is directly added to the organic solvent to be separately crystallized and recovered as the next batch of crude meropenem.
  • the present invention provides a method for preparing a meropenem drug, the method comprising the steps of:
  • the mother liquor 3 obtained in the step 3) is concentrated by nanofiltration, and then added to the next batch of the crude product to be hydrogenated, and the mother liquor which has been precipitated or not precipitated after filtration is crystallized to obtain a crude product of meropenem.
  • the content of C 17 H 25 N 3 5 5 S in the crude product of meropenem is not less than 92% by weight percentage, calculated as anhydrate; impurity A and impurity B are both Not more than 0.8%; any unknown single impurity is not more than 0.3%; the sum of other impurities except A and B is not more than 3.0%.
  • impurity A is:
  • the impurity B is:
  • the content of C 17 H 25 N 3 5 5 S in the crude meropenem is not less than 95% by weight, calculated as anhydrate;
  • A, impurity B is not more than 0.6%; any unknown single impurity is not more than 0.3%; the sum of other impurities except A and B is not more than 2.0%.
  • the step of dissolving the crude meropenem in water at a temperature of 50 ° C to 80 ° C in the step 1) comprises: adding the crude meropenem to 10 to 20 times by weight, preferably 15 to 20 times by weight of 5 ⁇ 20 ° C in water for injection, stir and mix evenly, and then the resulting suspension is heated to 50 ° C ⁇ 80 ° C, preferably 60 ° C ⁇ 80 ° C dissolved; wherein the dissolution time is less than 4 minutes, preferably Less than 1 minute.
  • the temperature of the resulting solution is lowered to 10 ° C to 25 ° C; wherein the time for cooling is less than 4 minutes, preferably less than 1 minute.
  • the temperature rise and fall in step 1) can be carried out by means of a heat exchanger, for example the heat exchanger described in the Chinese patent application CN201120235961.2.
  • the method of the present invention utilizes the heat exchange of the heat exchanger to rapidly dissolve and rapidly cool the temperature; the crude meropenem can be dissolved by any means which can achieve rapid dissolution, and the solution can be cooled by any means which can achieve rapid cooling.
  • the solution I can be decolorized by using 1 to 20% of the activated carbon of the meropenem weight of 1 to 20% at 15 ° C to 25 ° C for 1 to 30 minutes, preferably 1 to 10 minutes, and then filtered.
  • the filtrate II was obtained.
  • the solution is decolorized by in-line filtration through an activated carbon filter.
  • the activated carbon treatment is carried out by the method of the invention, and the solution can also be activated by any known means.
  • the activated carbon used is not particularly limited.
  • the temperature of the filtrate II is lowered to 0 ° C ⁇ 5 ° C for crystallization, and crystallized for 2 ⁇ 20 hours, preferably 5 ⁇ 10 hours; filtered to obtain the mother liquid 3 and the filter cake
  • the filter cake is washed with acetone to wash the crystal, and dried under vacuum at 20 ° C to 40 ° C, preferably 25 ° C to 30 ° C for 3 to 10 hours, preferably 5 to 6 hours, thereby obtaining a meropenem drug substance.
  • the crystal is preferably stirred and crystallized, and the stirring speed is 100 to 200 rpm, preferably 110 to 130 rpm.
  • the crystal growth time of the present invention refers to the crystal growth time, and the step 3) the crystal growth time is the time during which the crystal growth between the seed crystals and the filtration is added.
  • step 3 further comprises: adding seed crystals to the filtrate II obtained in the step 2) before crystallization; wherein the temperature of the seed crystal is 0 ° C ⁇ 20 ° C, preferably 0 ° C ⁇ 5 ° C;
  • the mass ratio of the seed crystal to the crude product of meropenem is 1%: 1 ⁇ 10%: 1, preferably 1%: 1 ⁇ 2%: 1.
  • step 3 1% to 10% by weight of the filtrate II is taken before crystallization, crystallized by adding an organic solvent thereto, and the obtained seed crystal is added to the remaining filtrate II for crystallization.
  • the organic solvent is selected from one or more of acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol and mercaptoethyl ketone, preferably acetone and/or tetrahydrofuran;
  • the weight (kg) of the partial filtrate II and the organic solvent is 1:2 to 1:6, and the seed crystal preparation temperature is 5 ° C to 20 ° C, preferably 10 ° C to 15 ° C.
  • step 4) of the method of the invention at a pressure of 5 X 10 5 Pa ⁇ 20 X 10 5 Pa, preferably 15 x 10 5 Pa ⁇ 20 ⁇ 10 5 Pa and 5 to 35 ° C, preferably 10 to 25 ° C
  • the nanofiltration concentration of the mother liquor 3 is carried out at a temperature such that the weight ratio of the mother liquor 3 to the obtained concentrate is 5:1 to 15:1, preferably 7:1 to 10:1; and the meropenem content in the obtained concentrate is 5 ⁇ 20% by weight, preferably 7 to 15% by weight.
  • the crystallization of the crude meropenem in the step 4) gives a volume ratio of the total volume of the organic solvent to the water of 3:1 to 6:1; the organic solvent is selected from the group consisting of acetone, tetrahydrofuran, isopropanol, and decyl alcohol.
  • the crystallization temperature is from 5 ° C to 15 ° C.
  • the mother liquor (mother liquor 2) in which the crude product has been precipitated after hydrogenation or filtration or the mother liquor (mother liquor 1) in which the crude product is not precipitated is the mother liquor 1 and the mother liquor 2 in the process of preparing the crude meropenem by the following method;
  • mother liquor 1 a mother liquid without precipitation of crude product
  • mother liquor 1 The mother liquor is added with an organic solvent, the temperature is controlled at 10-15 ° C, the mixture is filtered, washed, and the product is dried to obtain a crude product of meropenem (Compound I); the mother liquor is a mother liquor which has been precipitated as a crude liquid, and the mother liquor can be used as a mother liquor for which a crude product has been precipitated. , referred to as mother liquor 2.
  • the organic solvent is selected from one or more of tetrahydrofuran, acetone, isopropanol, decyl alcohol, ethanol, mercaptoethyl ketone; preferably tetrahydrofuran, acetone; preferably, the sum of the volume of the organic solvent in the mother liquor 2 and water The volume ratio is 3: 1 ⁇ 6: 1.
  • the content of meropenem is 98.5% ⁇ 101.0%, calculated as anhydrate;
  • the impurity A and the impurity B in the related substances of the raw material drug are not more than 0.25%; a single impurity is not more than 0.05%; the sum of other impurities except A and B is not more than 0.2%;
  • the acetone residue is not more than 400ppm, preferably not more than 100ppm;
  • impurity A is:
  • Impurity B is:
  • the present invention provides a meropenem pharmaceutical composition
  • a meropenem pharmaceutical composition comprising the meropenem drug of the present invention and a pharmaceutically acceptable excipient; preferably, the excipient is sterile sodium carbonate, wherein the The weight ratio of the drug substance to the sterile sodium carbonate is 1000: 195 to 1000: 222, preferably 1000: 208; preferably, the pharmaceutical composition is an injection.
  • the content of meropenem in the drug substance is 98.5% ⁇ 101.0%, calculated as an anhydrate; the impurity A and the impurity B in the related substances of the drug substance are not more than 0.25%. Any unknown single impurity is not more than 0.05%; the sum of other impurities except A and B is not more than 0.2%; the acetone residue is not more than 400ppm, preferably not more than 100ppm.
  • the invention also provides a preparation method of the meropenem pharmaceutical composition for injection, the method comprising: pulverizing the sterile meropenem drug substance and the sterile sodium carbonate, and detecting the sterility and the particle size requirement, according to the meropenem drug substance and
  • the weight ratio of sterile sodium carbonate is 1000: 195 ⁇ 1000: 222, and the mixture is mixed with a high-efficiency mixer.
  • the packaging container is aseptically processed and filled according to the US medicine.
  • the USP32-NF27 injection was tested by meropenem and packaged into the warehouse.
  • the meropenem pharmaceutical composition for injection provided by the invention has better stability, and the clarity and color after long-term storage still meet the requirements, and the medicine can be ensured to be safe and effective.
  • the content determination item, the related substance item, and the residual solvent item in the detection method of the present invention are all carried out according to the method of Meropenem in the United States Pharmacopoeia USP32-NF27, that is, the meropenem raw material provided by the present invention.
  • Medicine the content of meropenem in the raw material medicine is 98.5% ⁇ 101.0%, calculated as anhydrate; in the related substances of the raw material medicine: any two main impurities (impurity A and impurity B) shall not be greater than 0.25%, Calculated as anhydrate; other individual impurities shall not be greater than 0.05%, calculated as anhydrate; the sum of other impurities shall not be greater than 0.2%.
  • the acetone residue is not more than 400 ppm (0.04%), preferably not more than 100 ppm.
  • the two main impurities in the standard refer to the relative retention times of impurity A and impurity B, impurity A and impurity B (based on the retention time of meropenem for about 6 minutes) of about 0.5 and 2.2, respectively.
  • impurity A is:
  • Impurity B is a dimer of one molecule of meropenem and one molecule of ring-opening (Mw: 766), or it can be its isomer B 2 :
  • Quality control indicators are essential for ensuring the effectiveness and safety of the product. Impurities and residual solvents in meropenem or any active pharmaceutical ingredient (API) are superfluous, only the impurities are clearly defined, and the limits of identification are exceeded. Impurity studies identify the chemical structure of the impurity, in order to determine the impurity limit according to the nature of the impurity, in order to ensure the safety and effectiveness of the drug substance and preparation. In addition, the problem of the stability of the drug substance and the preparation is also related to the safety and effectiveness of the drug, so that the stability of the drug substance and the preparation is safer and more effective.
  • the meropenem raw material provided by the invention has high purity, clear impurity condition, low solvent residue, good solubility, and quality control index can ensure the product is effective and safe.
  • the meropenem drug substance provided by the invention has better stability, and the clarity and color after long-term storage still meet the requirements of the pharmacopoeia, and the possibility of causing side effects is smaller.
  • the crude product of meropenem is purified by purified water to obtain a high-quality meropenem drug substance, and the mother liquid 3 obtained is concentrated by a nanofiltration membrane, and then added to a crude liquid preparation (hydrogen mother 2) after being subjected to hydrogenation after filtration and filtration.
  • a crude liquid preparation hydrogen mother 2
  • the mother liquor mother liquor 1 in which no crude product was precipitated
  • the crude product of meropenem was obtained by crystallization.
  • the separate recovery step of the mother liquor is eliminated, the working hours are shortened, the amount of organic solvent used can be greatly reduced, and the meropenem in the mother liquor 3 can be recovered as much as possible, the product yield is greatly improved, and the production cost is remarkably reduced.
  • the invention can concentrate the heat-labile meropenem solution in a relatively short time at a relatively low temperature, greatly reducing the decomposition of meropenem, the nanofiltration concentration process is easy to control, and the temperature rise is low, which ensures that the product is in the material. The liquid does not deteriorate.
  • the invention has the advantages of simple process, low cost, compact process and simple control, and the obtained meropenem raw material has high purity, low solvent residue, good solubility and good long-term storage stability, and is suitable for industrial large-scale sterile meropenem raw materials. Production of pharmaceuticals and pharmaceutical preparations. DRAWINGS
  • Figure 1 shows the nuclear magnetic carbon spectrum of impurity A
  • Figure 2 is the nuclear magnetic resonance spectrum of impurity A
  • Figure 3 is an infrared analysis spectrum of impurity A
  • Figure 4 is a mass spectrum of impurity A
  • Figure 5 is an ultraviolet absorption spectrum of impurity A
  • Figure 6 is the nuclear magnetic resonance spectrum of impurity B
  • Figure 7 is an infrared analysis spectrum of impurity B
  • Figure 8 is a mass spectrum of impurity B
  • Figure 9 shows the ultraviolet absorption spectrum of impurity B.
  • FIG. 10 is a flow chart of the preparation method of the present invention. The best mode for carrying out the invention
  • the concentrate protecting meropenem (formula) or protecting meropenem can be prepared by any method known in the art, such as the method shown in CN200610083362.7.
  • the crude meropenem can be prepared by the method of Example 13, or by any method of preparing meropenem in the prior art, such as the method of preparing meropenem in CN1960992A or CN200610083362.7.
  • the content of C 17 H 25 N 3 5 5 S in the crude meropenem is not less than 92%, calculated as anhydrate; the impurity A and the impurity B are not more than 0.8%; any unknown single impurity is not More than 0.3%; the sum of other impurities except A and B is not more than 3.0%.
  • the content determination item, the related substance item, and the residual solvent item in the detection method of the present invention are carried out in accordance with the method of Meropenem in the United States Pharmacopoeia USP32-NF27.
  • the stability test was conducted in accordance with the United States Pharmacopoeia USP32-NF27 method.
  • the decolorizing solution I was filtered in-line through an activated carbon filter to obtain a filtrate II.
  • the filter cake was rinsed with acetone, and the filter cake was dried under vacuum at 30 ° C for 5 hours, and pulverized to obtain meragene saponin 680 g, yield 68%.
  • the content of meropenem is 99.6% (based on anhydrous matter); the impurity A in the relevant substance is 0.06%; the impurity B is 0.11%; any unknown single impurity is 0.02%; the sum of other impurities except A and B is 0.05%
  • the acetone residue is 80 ppm.
  • the physical properties of the meropenem drug substance are as follows:
  • IR ⁇ cm 1755, 1627, 1393, 1252, 1130.
  • the impurities were separated and mass spectrometrically determined by the LC/MS system.
  • the spectra are very consistent.
  • the molecular weight of each impurity was obtained, and the structure was initially determined.
  • the relative retention times of impurity A and impurity B were 0.5 and 2.2, respectively.
  • Liquid phase preparation of impurities In order to obtain more samples for further verification, referring to the mobile phase conditions in the preliminary separation and identification, the preparative liquid chromatography is used to separate the impurity AB, and the preparation is repeated several times to obtain a salt solution of all the impurities, and the impurity amount reaches the milligram level.
  • the impurities A and B are chemically synthesized to obtain lg impurity A, purity >95%; impurity B is about 50 mg, purity >90%
  • the impurity A was prepared according to the method described in The Journal of Antibiotics Vol. 46 No. 5 P831 to P832, and confirmed to be an impurity A by the structure, and was in conformity with the literature.
  • Impurity B was prepared according to the method described in Chem. Pharm. Bull. 43(4) P690 (1995), confirmed by structure as impurity B, and in accordance with the literature.
  • the impurity AB obtained by synthesis is compared with the impurity AB in the liquid phase of the product.
  • the UV spectra are compared, and the results indicate that they correspond to AB impurities respectively.
  • the impurities A and B obtained by chemical synthesis are respectively added by the addition method.
  • the mother liquor 2 contains about 16% water and 84% THF.
  • Example 3 For the preparation method, refer to Example 13.
  • the decolorization solution I was filtered through an activated carbon filter to obtain a filtrate II.
  • the filter cake was rinsed with acetone, and the filter cake was dried at 25 ° C for 6 hours, and pulverized to obtain 14 kg of meropenem raw material, yield 70%.
  • the content of meropenem is 99.7% (based on anhydrous matter); the impurity A in the relevant substance is 0.04%; the impurity B is 0.09%; any unknown single impurity is 0.03%; the sum of other impurities except A and B is 0.05% ; acetone residue is 20ppm
  • the physical properties of the meropenem drug substance are as follows:
  • IR ⁇ cm 1755, 1627, 1393, 1252, 1130.
  • Example 4 The impurity A B was analyzed and measured in accordance with the method described in Example 1, and the results were in agreement.
  • Example 4 The impurity A B was analyzed and measured in accordance with the method described in Example 1, and the results were in agreement.
  • Example 3 340 kg of the meropenem refined mother liquor obtained in Example 3 was added to the nanofiltration equipment solution tank; the outlet pressure of the nanofiltration equipment was controlled to start concentration at 20 X 10 5 Pa, and the temperature of the concentrated liquid was controlled to be 5 ° C ⁇ 35.0 ° C, concentrated. The liquid was reduced from 340kg to 42kg, and 298kg of concentrated wastewater was obtained. The sampled concentrated wastewater was used to detect the meropenem content, and the result was not detected. The concentration of meropenem was 9%.
  • the mother liquor 2 contains about 14% water and THF+ acetone is 86%; Preparation method refers to Example 13 Example 5
  • the decolorization solution I was filtered through an activated carbon filter to obtain a filtrate II.
  • the filter cake was rinsed with acetone, and the filter cake was dried at 20 ° C for 10 hours, and pulverized to obtain merapene 6.2 g, a yield of 69%.
  • the content of meropenem is 99.8% (calculated as anhydrate); the impurity A in the relevant substance is 0.05%; the impurity B is 0.07%; any unknown single impurity is 0.03%; the sum of other impurities except A and B is 0.08% ; Acetone residue was not detected.
  • the physical properties of the meropenem drug substance are as follows:
  • IR ⁇ cm 1755, 1627, 1393, 1252, 1130.
  • the 18.5 kg of the meropenem refined mother liquor obtained in Example 5 was added to the nanofiltration equipment solution tank. Control the outlet pressure of the nanofiltration equipment 5 X 10 5 Pa to start concentration, control the concentration of the liquid in the concentration process to 10 °C ⁇ 30 °C, reduce the concentrate from 18.8kg to 3.76kg, obtain 15kg of concentrated wastewater, and sample the concentrated wastewater to detect meropenem The content was not detected; the concentration of meropenem was 5%.
  • the mother liquor 2 contains about 15% water and THF + mercaptoethyl ketone is 85%; Preparation method refers to Example 13
  • Example 7
  • the decolorization solution I was filtered through an activated carbon filter to obtain a filtrate II.
  • the filter cake was rinsed with acetone, and the filter cake was dried at 25 ° C for 6 hours, and pulverized to obtain 21 kg of meropenem raw material, yield 70%.
  • the content of meropenem is 99.7% (calculated as anhydrous matter); the impurity A in the relevant substance is 0.05%; the impurity B is 0.06%; any unknown single impurity is 0.02%; the sum of other impurities except A and B is 0.06% ; acetone residue is 60ppm
  • the physical properties of the meropenem drug substance are as follows:
  • IR ⁇ cm 1755, 1627, 1393, 1252, 1130.
  • the decolorizing solution I was filtered in-line through an activated carbon filter to obtain a filtrate II.
  • the temperature was lowered to 5 °C, 3 kg of seed crystals were added, the stirring speed was maintained at 110 rpm, the crystals were maintained for 20 hours, and filtered to obtain a mother liquor 3, and the mother liquor 3 was subjected to the next nanofiltration concentration.
  • the filter cake was rinsed with acetone, and the filter cake was dried at 25 ° C for 6 hours, and pulverized to obtain 41.4 kg of meropenem raw material, yield 69%.
  • the content of meropenem is 99.5% (based on anhydrous matter); the impurity A in the relevant substance is 0.07%; the impurity B is 0.09%; any unknown single impurity is 0.02%; the sum of other impurities except A and B is 0.06%
  • the acetone residue is 50 ppm.
  • Example 10 The impurities A and B were analyzed and measured in accordance with the method described in Example 1, and the results were in agreement.
  • Example 10 The impurities A and B were analyzed and measured in accordance with the method described in Example 1, and the results were in agreement.
  • Example 9 3 600 kg of the meropenem refined mother liquor obtained in Example 9 was added to the nanofiltration equipment solution tank, and the outlet pressure of the nanofiltration equipment was controlled to start concentration at 20 X 10 5 Pa, and the temperature of the liquid in the concentration process was controlled to be 10 °C ⁇ 25 °C, concentrated to 40kg, 560L of concentrated wastewater was obtained, and the content of meropenem was detected by sampling and concentrating wastewater. The result was not detected; the concentration of meropenem was 20%.
  • Example 11 The preparation method of the mother liquid 1 is as described in Example 13.
  • Example 11 The preparation method of the mother liquid 1 is as described in Example 13.
  • Example 10 1 kg of the crude meropenem obtained in Example 10 was added to 13 kg of water for injection at 70 ° C, dissolved by stirring for 2 minutes, and rapidly lowered to 25 ° C in 4 minutes.
  • the filter cake was rinsed with acetone, and the cake was dried under vacuum at 25 ° C for 6 hours, and pulverized to obtain 670 g of meropenem prodrug, and the yield was 67%.
  • the content of meropenem is 99.4% (based on anhydrous matter); the impurity A in the relevant substance is 0.08%; the impurity B is 0.13%; any unknown single impurity is 0.03%; the sum of other impurities except A and B is 0.07%
  • the acetone residue is 10 ppm.
  • Example 12 The impurities A and B were analyzed and measured in accordance with the method described in Example 1, and the results were in agreement.
  • Example 12 The impurities A and B were analyzed and measured in accordance with the method described in Example 1, and the results were in agreement.
  • mother liquor 2 4300 L of the filtered mother liquor having a precipitated crude product was obtained, wherein the water content was about 700 L and the THF was about 3600 L; that is, about 16% of water and 84% of THF.
  • This mother liquor can be used as a filtered mother liquor which has been precipitated as a crude product, referred to as mother liquor 2 .
  • the tetrahydrofuran in 2625L tetrahydrofuran can be replaced by one or more of acetone, isopropanol, decyl alcohol, ethanol, mercaptoethyl ketone; the volume ratio of the volume of the organic solvent in the mother liquor 2 to water is 3: 1 ⁇ 6: 1 can be.
  • the tetrahydrofuran in 2625L of tetrahydrofuran can be replaced by one or more of acetone, isopropanol, decyl alcohol, ethanol and mercaptoethyl ketone, and the crude meropenem can be prepared.
  • Example 15 The 500 g of sterile meropenem drug substance prepared by the method described in Example 1 and 104 g of sterile sodium carbonate were pulverized, and the test was carried out according to the requirements of sterility and particle size, and the mixture was uniformly mixed with a high-efficiency mixer, and the packaging container was aseptically processed. Filling, according to the United States Pharmacopoeia USP32-NF27 injection with meropenem under the test method qualified, packaged into the warehouse.
  • Example 15 Example 15
  • Example 16 1000g of sterile meropenem drug substance prepared by the method described in Example ⁇ , 222g of sterile sodium carbonate pulverized, tested to meet the requirements of sterility and particle size, and uniformly mixed with a high-efficiency mixer, and the packaging container is aseptically processed. Filling, according to the United States Pharmacopoeia USP32-NF27 injection with meropenem under the test method qualified, packaged into the warehouse.
  • Example 16 1000g of sterile meropenem drug substance prepared by the method described in Example ⁇ , 222g of sterile sodium carbonate pulverized, tested to meet the requirements of sterility and particle size, and uniformly mixed with a high-efficiency mixer, and the packaging container is aseptically processed. Filling, according to the United States Pharmacopoeia USP32-NF27 injection with meropenem under the test method qualified, packaged into the warehouse.
  • Example 16 1000g of sterile meropenem drug substance prepared by the method described in Example ⁇
  • the content of meropenem is 98.4% (based on anhydrous matter); the impurity A in the relevant substance is 0.19%; the impurity B is 0.27%; any unknown single impurity is 0.10%; the sum of other impurities except A and B is 0.26%
  • the acetone residue was 599 ppm.
  • the concentrate is cooled to 0 ° C to 10 ° C, 1 g of seed crystals is added to the concentrate, and 20.1 L of tetrahydrofuran at a temperature of 0 ° C to 10 ° C is added as a solvent for the concentrate, followed by stirring for 6 hours, and stirring.
  • the temperature was from 0 ° C to 5 ° C, and the precipitated crystals were collected, washed with acetone and dried at 30 ° C for 3 hours to obtain 165 g of meropenem.
  • the content of meropenem is 98.9% (in terms of anhydrous matter); the maximum impurities before and after the main peak in the relevant substances are 0.13%, 0.23%, respectively. He has a single impurity of 0.08%; the sum of each impurity is 0.52%, and the organic residue of THF is 998 ppm.
  • the weight ratio of the meropenem drug substance to sodium carbonate prepared according to the method described in Example 14 was
  • Impurity A ⁇ 0.25% 0.06% 0.12% 0.12% 0.14% 0.14% 0.15% 0.15% Impurity B ⁇ 0.25% 0.11% 0.08% 0.05% 0.06% 0.06% 0.06% 0.04% Any unknown single impurity: ⁇ 0.05% 0.02% 0.03% 0.04% 0.02% 0.03% 0.03% 0.02% Except for the sum of other impurities except A and B: ⁇ 0.2% 0.05% 0.05% 0.10% 0.09% 0.08% 0.11% 0.06% Example 1 sample and No. 5 standard
  • detection items of the meropenem drug substance provided by the present invention such as specific rotation, acidity, clarity, bacterial endotoxin, sterility, moisture, visible foreign matter, insoluble particles, organic residues, pyrophoric residues, heavy metals, crystal water, Accelerated test stability results such as anhydrous content also meet the requirements.
  • Impurity A ⁇ 0.25% 0.05% 0.09% 0.11% 0.11% 0.12% 0.14% 0.14% Impurity B ⁇ 0.25% 0.06% 0.08% 0.08% 0.05% 0.05% 0.06% 0.04% Any unknown single impurity: ⁇ 0.05% 0.02% 0.03% 0.02% 0.01% 0.02% 0.02% 0.03% Sum of other impurities except A and B: ⁇ 0.2% 0.06% 0.09% 0.07% 0.07% 0.08% 0.09% 0.06% It can be seen that the package is packaged at a temperature of 25. C ⁇ 2. C. Humidity 60% RH ⁇ 5% RH is placed under long-term test conditions for 24 months. The impurities are still in compliance with the regulations and the stability is very good. Therefore, the preparation of injection as a raw material medicine is safer and more effective for intravenous administration.
  • detection items of the meropenem drug substance provided by the present invention such as specific rotation, acidity, clarity, color, bacterial endotoxin, sterility, moisture, visible foreign matter, insoluble particles, organic residue, ignition residue, heavy metal, crystallization Long-term test stability results such as water and anhydrous content also meet the requirements.
  • compositions prepared in the comparative examples 1 and 2 having a high impurity content and having a high residual organic residue of acetone or tetrahydrofuran were at a temperature of 25. C ⁇ 2.
  • the long-term test conditions of the meropenem pharmaceutical composition are still in compliance with the regulations, and the stability is very good. The use as an injection for intravenous administration is safer and more effective.
  • detection items of the meropenem pharmaceutical composition for injection provided by the present invention, such as traits, identification, alkalinity, clarity, related substances, loss on drying, content uniformity, bacterial endotoxin, sterility, visible foreign matter, insoluble particles, Long-term test stability results such as content determination also meet the requirements, so the product can be guaranteed to be effective and safe.

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Abstract

Disclosed in the present invention is a bulk drug of meropenem, characterized in that the meropenem content in the bulk drug is 98.5%~101.0% based on the anhydrous substances; the impurities A and B in the related substances of the bulk drug are both no more than 0.25%; any single unknown impurity is no more than 0.05%; the sum of the other impurities in addition to A and B is no more than 0.2%; the residue of acetone is no more than 400ppm, preferably no more than 100ppm. Also disclosed in the present invention is a meropenem pharmaceutical composition with very good stability for injection using the meropenem bulk drug provided by the present invention as the active ingredient. The meropenem bulk drug provided by the present invention has high purity, well-defined impurity levels, low residual solvent content, good solubility, and good stability for long-term storage, so it ensures that the drug is effective and safe. The present invention has a simple process, a very low cost, a compact process, and is easy to control, so it is suitable for the production of sterile meropenem bulk drug and pharmaceutical preparations on an industrial scale.

Description

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一种美罗培南原料药、 其制备方法及包含其的药物组合物 技术领域 Meropenem raw material drug, preparation method thereof and pharmaceutical composition containing the same
本发明属于制药领域, 具体而言, 本发明涉及一种美罗培南原料药、 其制备方法、 以及包含该美罗培南原料药的药物组合物。 背景技术  The present invention relates to the field of pharmacy, and in particular, to a meropenem drug substance, a process for the preparation thereof, and a pharmaceutical composition comprising the meropenem drug substance. Background technique
美罗培南 (Meropenem ), 化学名为(-)-(4R,5S,6S)-3-[(3S,5S)-5- (二曱基 胺酰基 )-3-吡咯烷]硫 -6-[(lR)-l-羟乙基 ]-4-曱基 -7-氧 -1-氮杂双环 [3.2.0]-庚 -2- 烯 -2-羧酸三水合物, 是一种碳青霉烯类抗生素, 具有广谱抗菌性并且可供 注射, 用于治疗多种不同的感染, 包括脑膜炎及肺炎, 其在常态下是以三 水合物的形式存在的, CAS登记号为 【 119478 ~ 56 ~ 7】, 具体结构式如式 ( I ) 所示。  Meropenem, chemical name (-)-(4R,5S,6S)-3-[(3S,5S)-5-(didecylamino)-3-pyrrolidine]sulfur-6-[ (lR)-l-hydroxyethyl]-4-mercapto-7-oxo-1-azabicyclo[3.2.0]-hept-2-ene-2-carboxylic acid trihydrate, is a carbon blue Amylin antibiotics, with broad-spectrum antibacterial properties and available for injection, for the treatment of a variety of different infections, including meningitis and pneumonia, which are normally in the form of trihydrates, CAS registration number [119478] ~ 56 ~ 7], the specific structural formula is shown in formula (I).
Figure imgf000003_0001
Figure imgf000003_0001
( I ) 原料药英文名为 API (Active Pharmaceutical Ingredient) ,指用于生产各 类制剂的原料药物,是制剂中的有效成份。原料药在 ICH Q7A中的完善定 义为: 旨在用于药品制造中的任何一种物质或物质的混合物, 而且在用于 制药时, 成为药品的一种活性成分。 此种物质在疾病的诊断, 治疗, 症状 緩解, 处理或疾病的预防中有药理活性或其他直接作用, 或者能影响机体 的功能或结构。  (I) The API (Active Pharmaceutical Ingredient) is the raw material used in the production of various preparations and is the active ingredient in the preparation. The perfect definition of APIs in ICH Q7A is: Any substance or mixture of substances intended for use in the manufacture of pharmaceuticals, and when used in pharmaceuticals, becomes an active ingredient of pharmaceuticals. This substance may have pharmacological activity or other direct effects in the diagnosis, treatment, symptom relief, treatment or prevention of the disease, or may affect the function or structure of the body.
中国药典 2010年版二部 606页关于美罗培南(Meropenem )的标准中 对有关物质进行了规定: 主峰前和后的最大杂质峰面积均不得大于对照溶 液主峰面积的 0.6倍(0.3% ),其他单个杂质峰面积不得大于对照溶液主峰 面积的 0.2倍( 0.1% ), 各杂质峰面积的和不得大于对照溶液主峰面积的 2 倍( 1.0% )。 其中残留溶剂规定: 检测丙酮、 乙腈、 二氯曱烷、 乙酸乙酯 与四氢呋喃符合规定, 中国药典 2010年版二部附录覆 P残留溶剂测定法 附表 1 药品中常见的残留溶剂及限度中规定: 丙酮检测限度为 0.5% ( 5000ppm ); 乙腈为 0.041% ( 410ppm ); 二氯曱烷为 0.06% ( 600ppm ); 乙酸乙酯的检测限度为 0.5% ( 5000ppm ); THF 的检测限度为 0.072% ( 720ppm )。 The Pharmacopoeia of the Chinese Pharmacopoeia 2010 edition of 606 pages on Meropenem standard specifies the relevant substances: The maximum impurity peak area before and after the main peak should not be greater than 0.6 times (0.3%) of the main peak area of the control solution, other single The impurity peak area shall not be greater than 0.2 times (0.1%) of the main peak area of the control solution, and the sum of the impurity peak areas shall not be greater than 2 times (1.0%) of the main peak area of the control solution. Residual solvent regulations: Determination of acetone, acetonitrile, dichlorodecane, ethyl acetate and tetrahydrofuran in compliance with the regulations, Chinese Pharmacopoeia 2010 edition of the second appendix P residual solvent determination method Schedule 1 common solvents and limits specified in the drug: Acetone detection limit is 0.5% (5000 ppm); acetonitrile is 0.041% (410 ppm); dichlorodecane is 0.06% (600 ppm); ethyl acetate has a detection limit of 0.5% (5000 ppm); THF has a detection limit of 0.072% (720 ppm).
目前公开文献报道的美罗培南的精制方法, 如 US4888344 实施例 1 中公开了美罗培南三水合物晶体的制备方法, 该方法包括将美罗培南粗品 于 30°C溶于水中, 水浴冷却, 析出少量晶体, 加入丙酮, 搅拌 1小时, 过 滤得到晶体, 用丙酮洗涤, 减压室温干燥 2小时得到美罗培南三水合物晶 体。 这种精制方法收率较高, 但丙酮残留高, 可能可以达到中国药典 2010 年版二部附录残留溶剂测定法中规定药品中丙酮不超过 0.5%的检测限度。 但美国药典 USP32-NF27中美罗培南三水合物标准中对溶剂残留有及其严 格的要求, 其中丙酮残留不得高于 0.05%, 这种精制方法一般很难达到。 而且丙酮属于公安机关管制类型中的易制毒第三类、 易制爆类, 虽然丙酮 属于三类溶剂, 急性或短期研究显示, 这些溶剂毒性较低, 基因毒性研究 结果呈阴性, 但尚无这些溶剂的长期毒性或致癌性的数据, 且它对人体具 有肝毒性, 长期使用丙酮残留高的注射剂无疑对患者的健康极其不利, 如 有些癌症患者尿样丙酮水平会异常升高。  The refining method of meropenem reported in the open literature, as disclosed in US Pat. No. 4,888,344, Example 1, discloses a method for preparing meropenem trihydrate crystals, which comprises dissolving melopenem in water at 30 ° C, cooling in a water bath, and depositing a small amount of crystals. Acetone was added, stirred for 1 hour, and crystallized by filtration, washed with acetone, and dried under reduced pressure at room temperature for 2 hours to obtain crystals of meropenem trihydrate. The purification method has a high yield, but the acetone residue is high, which may reach the detection limit of the acetone in the drug specified in the Chinese Pharmacopoeia 2010 Appendix 2 residual solvent determination method. However, the United States Pharmacopoeia USP32-NF27 has a stringent requirement for solvent residues in the meropenem trihydrate standard, wherein the acetone residue should not be higher than 0.05%. This refining method is generally difficult to achieve. Moreover, acetone belongs to the third type of easy-to-manufacture type of the public security organs, and it is easy to make explosives. Although acetone belongs to three types of solvents, acute or short-term studies have shown that these solvents are less toxic and the results of genotoxicity studies are negative, but there is no The long-term toxicity or carcinogenicity of these solvents, and it is hepatotoxic to humans. Long-term use of high-injection of acetone residues is undoubtedly harmful to the health of patients. For example, some cancer patients have abnormally elevated levels of urine acetone.
US2009264643 公开了一种美罗培南三水合物的精制方法, 其中涉及 先后加入氨水、 曱酸调节 pH值, 然后用四氢呋喃结晶的工艺。 此方法比 较繁瑣, 而且中国药典 2010年版二部附录残留溶剂测定法中规定药品中 THF 的检测限度为 0.072%, 这种精制方法一般艮难达到。 并且四氢呋喃 属于二类溶剂, 属于无基因毒性但有动物致癌性的溶剂, 它健康危害有: 高浓度吸入后可出现头晕、 头痛、 胸闷、 胸痛、 咳嗽、 乏力、 胃痛、 口干、 恶心、 呕吐等症状, 可伴有眼刺激症状, 部分患者可发生肝功能障碍。 高 剂量或反复接触, 可出现肝脂肪浸润及细胞溶解; 长期接触会导致失去性 功能、生育能力,或肾疾病。所以应避免在工艺的最后一步使用,否则 THF 残留太高将严重威胁美罗培南注射剂的安全。  US2009264643 discloses a process for the purification of meropenem trihydrate, which involves a process of adding aqueous ammonia, citric acid to adjust the pH, and then crystallizing with tetrahydrofuran. This method is rather cumbersome, and the Chinese Pharmacopoeia 2010 edition of the second appendix residual solvent determination method specifies that the detection limit of THF in the drug is 0.072%, and this purification method is generally difficult to achieve. And tetrahydrofuran belongs to the second class of solvents. It is a non-genotoxic but animal carcinogenic solvent. Its health hazards are: dizziness, headache, chest tightness, chest pain, cough, fatigue, stomach pain, dry mouth, nausea, vomiting after high concentration inhalation. Such symptoms may be accompanied by symptoms of eye irritation, and some patients may have liver dysfunction. High dose or repeated exposure may cause hepatic fat infiltration and cell lysis; prolonged exposure may result in loss of sexual function, fertility, or kidney disease. Therefore, it should be avoided in the last step of the process, otherwise the THF residue is too high will seriously threaten the safety of meropenem injection.
CN201010232062.7公开了一种美罗培南三水合物结晶的制备方法,其 完全在水溶液中结晶, 滤液加有机溶剂回收美罗培南。 这种方法制得的美 罗培南三水合物结晶中各种有机溶剂残留低于 0.05% ,但需要分二步进行, 收率不高, 而且滤液加有机溶剂回收美罗培南就将大大增加有机溶剂的使 用量, 不利于环保, 也不利于降低成本。  CN201010232062.7 discloses a preparation method of meropenem trihydrate crystals, which is completely crystallized in an aqueous solution, and the filtrate is added with an organic solvent to recover meropenem. The residual organic solvent in the meropenem trihydrate crystal prepared by this method is less than 0.05%, but it needs to be carried out in two steps, the yield is not high, and the recovery of the organic solvent by the organic solvent to remove the meropenem will greatly increase the organic solvent. The amount of use is not conducive to environmental protection, and is not conducive to reducing costs.
CN201110218567.2公开了一种美罗培南的制备方法,其包括将美罗培 南粗品溶解在 10%氢氧化钠水中, 活性炭处理后过滤、 析晶, 再加乙酸乙 酯回收美罗培南。 该方法也需要分二步进行, 收率不高; 而且滤液加乙酸 乙酯回收美罗培南也将大大增加乙酸乙酯的使用量, 不利于环保, 也不利 于降低成本。 此外 Yutaka Takeuchi等人于 Chem. Pharm. Bull.43(4)689 - 692(1995)中记载了美罗培南在酸性和碱性条件下比中性环境更不稳定,并 且该文献 P690显示等量的碳酸氢钠、 美罗培南水溶液冻干得到美罗培南 钠盐, 400mg美罗培南钠盐溶解在 lml水中维持在 30°C , 用 HPLC监控, 可以发现 6小时后 HPLC峰面积比为: 美罗培南 47%, 降解产物 A 11%, 降解产物 B 38% , 相比碱性较弱的碳酸氢钠, pH大约为 14.3的 10%氢氧 化钠溶液无疑会使美罗培南的降解更加严重。 Yutaka Takeuchi等人于 The Journal of Antibiotics Vol.46 No.5 P829也记载了在酸性( H < 2 )和碱性( H > 13 )环境下, 美罗培南立即水解, 主要降解产物(指开环产物 A )生成。 因此这种将美罗培南粗品溶解在强碱性的 10 %氢氧化钠水中重结晶的方 法, 非但不能实现美罗培南的提纯目的而且会增大美罗培南的杂质。 所以 其实施例声称得到的美罗培南经中国药典 2010年版二部美罗培南有关物 质检测, 单一最大杂质 0.03%, 总杂质 0.13% , 其可信度值得怀疑, 而且 对照中国药典 2010年版二部美罗培南有关物质检测标准,其没有提及 "主 峰前和后的最大杂质" 含量多少, 我们无法确定 "单一最大杂质"及 "总 杂质" 是否包括 "主峰前和后的最大杂质", 以至于无法清晰地获知其中 美罗培南杂质的状况。 CN201110218567.2 discloses a preparation method of meropenem, which comprises dissolving crude meropenem in 10% sodium hydroxide water, filtering after activated carbon, crystallization, and adding acetic acid B. The ester is recovered from meropenem. The method also needs to be carried out in two steps, and the yield is not high; and the recovery of meropenem from the filtrate with ethyl acetate will greatly increase the amount of ethyl acetate used, which is not conducive to environmental protection and is not conducive to cost reduction. Furthermore, Yutaka Takeuchi et al., Chem. Pharm. Bull. 43 (4) 689-692 (1995), describe that meropenem is more unstable under acidic and basic conditions than the neutral environment, and the document P690 shows an equivalent amount. Sodium bicarbonate and meropenem aqueous solution were lyophilized to obtain meropenem sodium salt. 400 mg of meropenem sodium salt was dissolved in 1 ml of water and maintained at 30 ° C. It was found by HPLC that the HPLC peak area ratio after 6 hours was: meropenem 47%, Degradation product A 11%, degradation product B 38%, 10% sodium hydroxide solution with a pH of about 14.3 will undoubtedly make the degradation of meropenem more serious than the less alkaline sodium bicarbonate. Yutaka Takeuchi et al., The Journal of Antibiotics Vol. 46 No. 5 P829 also describes the immediate hydrolysis of meropenem in acidic (H < 2 ) and basic (H > 13) environments, the main degradation products (referring to ring-opening products). A) Generated. Therefore, this method of recrystallizing the crude product of meropenem in a strong alkaline 10% sodium hydroxide solution can not only achieve the purification purpose of meropenem but also increase the impurities of meropenem. Therefore, the example claimed that the meropenem has been tested by the Chinese Pharmacopoeia 2010 edition of the second meropenem-related substances, the single largest impurity is 0.03%, the total impurity is 0.13%, and its credibility is questionable, and the Chinese Pharmacopoeia 2010 edition two meropenem Regarding the substance testing standards, there is no mention of the "maximum impurities before and after the main peak". We cannot determine whether the "single maximum impurity" and "total impurities" include the "maximum impurities before and after the main peak", so that it is impossible to be clear. The situation of the impurities of meropenem is known.
在美罗培南或任何活性药物成分(API ) 中的杂质为不需要的, 并且 在极端情况下, 甚至可能对正接受含 API的剂型治疗的患者有害。 例如国 家食品药品监管局官方网站发布的 《2011年药品不良反应监测年度报告》 显示, 化学药品中抗感染类在总不良反应报告和严重不良反应报告中均排 首位, 占比高达 51.2%。 这与杂质、 溶剂残留控制不严, 有些抗生素存在 不明杂质, 长期储存过程中质量不稳定都有一定的关系, 所以, 迫切需要 提供一种杂质含量更低、 杂质状况清晰、 溶剂残留更低、 质量稳定、 不良 反应小的美罗培南原料及制剂组合物。  Impurities in meropenem or any active pharmaceutical ingredient (API) are undesirable and, in extreme cases, may be harmful to patients undergoing treatment with API-containing dosage forms. For example, the 2011 Annual Report on Adverse Drug Reaction Monitoring released by the official website of the State Food and Drug Administration showed that anti-infectives in chemical products ranked first in total adverse reaction reports and serious adverse reactions reports, accounting for 51.2%. This is inconsistent with the control of impurities and solvent residues, some unclear impurities in some antibiotics, and unstable quality during long-term storage. Therefore, it is urgent to provide a lower impurity content, clear impurity conditions, and lower solvent residues. A meropenem raw material and a formulation composition having stable quality and low adverse reactions.
美罗培南的热稳定性差, 大生产过程中母液量大, 主要为水, 如果将 母液直接加热, 高温真空浓缩, 长时间处于高温状态将加速美罗培南的降 解, 这样回收的母液杂质量大, 因此这种回收方法没有实际应用价值。 如 果釆用加入全新的有机溶剂进行回收的方式, 由于水量大, 因此需要加入 的有机溶剂量也艮大, 从环保方面、 成本方面考虑也都是不可取的。  The thermal stability of meropenem is poor. The amount of mother liquor in the large production process is large, mainly water. If the mother liquor is directly heated, concentrated at high temperature and vacuum, the high temperature state will accelerate the degradation of meropenem, and the recovered mother liquor has a large mass. This recycling method has no practical value. If you use a new organic solvent for recycling, the amount of organic solvent that needs to be added is also large due to the large amount of water. It is also undesirable from environmental and cost considerations.
纳滤膜分离技术(英文名为 Nanofiltration, 简称 NF , 中文译为 "纳 滤") 是允许溶剂分子或某些低分子量溶质或低价离子透过的一种功能性 过滤技术。 纳滤膜为半透膜, 其存在着纳米级的细孔, 且截留率大于 95 %的最小分子约为 lnm, 截留有机物的分子量大约为 150 ~ 500左右, 截 留溶解性盐的能力为 2 ~ 98%之间, 对单价阴离子盐溶液的脱盐低于高价 阴离子盐溶液,主要用于去除地表水的有机物和色度,脱除地下水的硬度, 部分去除溶解性盐, 浓缩果汁等。 Nanofiltration membrane separation technology (English name is Nanofiltration, referred to as NF, Chinese translation for "Nano Filtration is a functional filtration technique that allows solvent molecules or certain low molecular weight solutes or low-cost ions to pass through. Nanofiltration membranes are semi-permeable membranes with nanoscale pores and a rejection of greater than 95%. The minimum molecular weight is about 1 nm, the molecular weight of the retained organic matter is about 150 ~ 500, the ability to retain the soluble salt is between 2 and 98%, and the desalting of the monovalent anion salt solution is lower than that of the high-priced anionic salt solution, mainly for removal. The organic matter and color of surface water, remove the hardness of groundwater, partially remove dissolved salts, concentrate juice, etc.
目前将美罗培南原料药制备过程产生的反应液经过纳滤浓缩后进入 下一批美罗培南粗品的制备的应用还未见报道。 如果直接将美罗培南结晶 液纳滤浓缩, 纳滤过程是否会对含大量美罗培南的结晶液稳定性产生影 响, 尚需要考察。 并且, 由于美罗培南浓度大, 体积不能浓缩到很小, 否 则晶体会析出造成纳滤膜堵塞, 这样就需要再加入大量有机溶剂析晶, 很 难得到有机溶剂残留低的美罗培南原料药。 发明内容  At present, the application of the reaction liquid produced by the preparation of the drug substance of meropenem into the next batch of crude meropenem has not been reported. If the meropenem crystals are directly concentrated by nanofiltration, whether the nanofiltration process will affect the stability of the crystallization solution containing a large amount of meropenem is still to be investigated. Moreover, since the concentration of meropenem is large, the volume cannot be concentrated to a small extent, otherwise the crystals will precipitate and cause the nanofiltration membrane to clog, so that a large amount of organic solvent is required to be crystallized, and it is difficult to obtain a meropenem drug substance having a low residual organic solvent. Summary of the invention
经过大量实验, 本申请人惊喜地发现, 美罗培南粗品如经纯水精制, 除美罗培南原料药外, 还可以得到过滤母液, 其为含美罗培南 1 ~ 2%的水 溶液, 此溶液经过纳滤膜浓缩后水量大大减少, 纳滤浓缩前后重量比为 5: 1 - 15: 1 , 浓缩后的美罗培南含量为 5 ~ 20%, 浓度大大提高。  After a large number of experiments, the applicant was pleasantly surprised to find that the crude product of meropenem is purified by pure water. In addition to the meropenem raw material, a filter mother liquor can also be obtained, which is an aqueous solution containing meropenem 1-2%, and the solution is subjected to nanofiltration. After the membrane is concentrated, the water volume is greatly reduced. The weight ratio before and after the nanofiltration concentration is 5:1 - 15:1, and the concentration of meropenem after concentration is 5-20%, and the concentration is greatly increased.
同时, 由于美罗培南粗品的生产中需要加入大量有机溶剂到结晶体系 中以析出美罗培南粗品, 因此过滤除去美罗培南粗品后的母液含大量有机 溶剂, 其中有机溶剂体积之和与水的体积之比大约为 3: 1 ~ 6: 1 , 这些有机 溶剂主要为丙酮、 四氢呋喃、 异丙醇、 曱醇、 乙醇、 曱基乙基酮的一种或 多种。 这种母液作为废液浪费太大, 如回收则成本也会 4艮高。 如果将纳滤 膜浓缩后的浓缩液加入此主要为有机溶剂的粗品母液中, 则可直接结晶得 到下一批美罗培南粗品, 从而使有机溶剂得到充分利用。  At the same time, since the crude product of meropenem needs to be added to the crystallization system to precipitate the crude meropenem, the mother liquor after the removal of the crude meropenem contains a large amount of organic solvent, wherein the ratio of the volume of the organic solvent to the volume of water Approximately 3:1 to 6:1, these organic solvents are mainly one or more of acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol, and mercaptoethyl ketone. This mother liquor is too wasteful to waste as a waste liquid. For recycling, the cost is also high. If the concentrate concentrated by the nanofiltration membrane is added to the crude mother liquor which is mainly an organic solvent, the next batch of crude meropenem can be directly crystallized, so that the organic solvent can be fully utilized.
或者, 可以将纳滤膜浓缩后的浓缩液加入到后续粗品制备中氢化过滤 后未析出粗品的母液, 按常规方法滴加有机溶剂, 如丙酮、 四氢呋喃、 异 丙醇、 曱醇、 乙醇、 曱基乙基酮的一种或多种, 调整有机溶剂体积之和与 水的体积之比大约为 3: 1 ~ 6: 1 , 同样可结晶得到美罗培南粗品。  Alternatively, the concentrated liquid obtained by concentrating the nanofiltration membrane may be added to the mother liquor in which the crude product is not precipitated after the hydrogenation filtration in the subsequent crude product preparation, and the organic solvent such as acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol, hydrazine is added dropwise according to a conventional method. One or more of the ethyl ethyl ketones, the ratio of the volume of the adjusted organic solvent to the volume of the water is about 3:1 to 6:1, and the same can be crystallized to obtain the crude product of meropenem.
基于上述发现, 本发明的一个目的是通过对原料药有效成分美罗培南 进行含量测定,对主要杂质 A和杂质 B进行物质确定和含量分析,对残留 溶剂严格控制, 提供一种美罗培南原料药, 该原料药区别于现有技术, 纯 度高、 杂质状况清晰、 溶媒残留低、 长期储存稳定性好、 质量控制指标能 够保证产品有效安全。 Based on the above findings, an object of the present invention is to determine the content of the main impurity A and the impurity B by quantitatively controlling the content of the main ingredient A and the impurity B, and to strictly control the residual solvent to provide a meropenem drug substance. The raw material drug is different from the prior art, and has high purity, clear impurity condition, low solvent residue, long-term storage stability, and quality control index. Ensuring that the product is effective and safe.
本发明的另一个目的是提供一种美罗培南原料药的制备方法, 该方法 包括, 将美罗培南粗品经精制得到美罗培南原料药和含低浓度美罗培南的 溶液, 所得溶液经过纳滤膜浓缩后进入后续美罗培南粗品的制备。 该方法 工艺简单、 紧凑、 可控, 同时收率高、 成本低, 具有巨大的经济优势。  Another object of the present invention is to provide a method for preparing a meropenem drug, which comprises refining a crude meropenem drug to obtain a meropenem drug substance and a solution containing a low concentration of meropenem, and the resulting solution is concentrated by a nanofiltration membrane. Enter the preparation of the subsequent crude meropenem. The method is simple, compact and controllable, and has high yield and low cost, and has great economic advantages.
本发明的再一个目的是提供一种美罗培南药物组合物, 该药物组合物 以本发明提供的美罗培南原料药为活性成分, 具有很好的稳定性。  Still another object of the present invention is to provide a pharmaceutical composition of meropenem which has excellent stability as the active ingredient of the meropenem drug of the present invention.
本发明的目的是通过以下技术方案来实现的。  The object of the present invention is achieved by the following technical solutions.
一方面, 本发明提供一种美罗培南原料药, 以重量百分比计, 所述原 料药中美罗培南的含量为 98.5% ~ 101.0%, 以无水物计算; 所述原料药的 有关物质中杂质 A、 杂质 B 均不大于 0.25%; 任何未知单个杂质不大于 0.05%; 除 A和 B外其它杂质总和不大于 0.2%; 丙酮残留不大于 400ppm, 优选不大于 100ppm。  In one aspect, the present invention provides a meropenem drug substance, wherein the content of meropenem in the drug substance is 98.5%-101.0%, calculated as an anhydrate; the impurity A in the related substance of the drug substance , impurity B is not more than 0.25%; any unknown single impurity is not more than 0.05%; the sum of other impurities except A and B is not more than 0.2%; acetone residue is not more than 400ppm, preferably not more than 100ppm.
其中杂质 A为:  Among them, impurity A is:
Figure imgf000007_0001
Figure imgf000007_0002
Figure imgf000007_0001
Figure imgf000007_0002
另一方面, 本发明还提供一种美罗培南原料药的制备方法, 所述方法 包括: 将美罗培南粗品经精制、 过滤得到母液 3及美罗培南原料药, 母液 3经过纳滤膜浓缩后, 将所得浓缩液加入到后续粗品制备中氢化、 过滤后 已析出粗品的母液(母液 2 ) 或未析出粗品的母液(母液 1 ) 中, 结晶得 到美罗培南粗品。  In another aspect, the present invention provides a method for preparing a meropenem drug, the method comprising: purifying and filtering the crude meropenem to obtain a mother liquor 3 and a meropenem drug substance, and the mother liquor 3 is concentrated by a nanofiltration membrane, The obtained concentrate is added to a mother liquid (mother liquid 2) which has been subjected to hydrogenation in the subsequent crude product preparation, and which has been precipitated after filtration or a mother liquid (mother liquor 1) in which no crude product is precipitated, and crystallized to obtain a crude product of meropenem.
需要指出的是, 本发明所述的美罗培南粗品及下文涉及的美罗培南晶 种是指具有通式 (I ) 的化合物:
Figure imgf000008_0001
It should be noted that the crude meropenem according to the present invention and the meropenem seed crystal referred to below refer to a compound having the general formula (I):
Figure imgf000008_0001
( I ) 在美罗培南的制备中, 美罗培南粗品一般由保护美罗培南 (la ) 氢化 制备得到, 为未精制美罗培南 (化合物 I ), 反应式如下:  (I) In the preparation of meropenem, the crude meropenem is generally prepared by hydrogenation of meropenem (la), which is unrefined meropenem (compound I). The reaction formula is as follows:
Figure imgf000008_0002
反应过程一般为: 将保护美罗培南 (或者保护美罗培南浓缩液)、 反 应溶剂、 催化剂 (如钯碳)加入到高压氢化釜中, 除去空气, 通入氢气反 应, 反应毕, 过滤回收钯碳, 得到未析出粗品的母液; 此母液为本发明所 述未析出粗品的母液, 简称母液 1;
Figure imgf000008_0002
The reaction process is generally: adding meropenem (or protecting meropenem concentrate), a reaction solvent, a catalyst (such as palladium carbon) to a high pressure hydrogenation reactor, removing air, introducing a hydrogen reaction, and completing the reaction, and recovering palladium carbon by filtration. Obtaining a mother liquor which is not precipitated as a crude product; the mother liquor is the mother liquor of the unprecipitated crude product of the present invention, referred to as mother liquor 1;
此母液 1中加入有机溶剂, 控制温度搅拌析晶, 过滤, 得母液 2及美 罗培南粗品; 此母液 2为本发明所述已析出粗品的母液, 简称母液 2。  The mother liquor 1 is added with an organic solvent, controlled to stir and crystallize at a temperature, and filtered to obtain a mother liquor 2 and a crude product of meropenem; this mother liquor 2 is a mother liquor of the precipitated crude product of the present invention, which is referred to as a mother liquor 2 .
美罗培南粗品经精制、 过滤得到母液 3及美罗培南原料药; 母液 3经 过纳滤浓缩得到纳滤浓缩液, 将其加入后续粗品制备中的母液 1或母液 2 中, 再一起结晶制备得到美罗培南粗品。  The crude product of meropenem is refined and filtered to obtain mother liquor 3 and meropenem bulk drug; mother liquor 3 is concentrated by nanofiltration to obtain nanofiltration concentrated solution, which is added to mother liquor 1 or mother liquor 2 in the subsequent crude product preparation, and then crystallized to obtain meropenem Crude.
所述制备方法的工艺流程见附图 10。  The process flow of the preparation method is shown in Fig. 10.
这个过程在控制美罗培南粗品、 美罗培南原料药质量合格的条件下, 可以循环往复, 一直套用下去, 不仅能够大大地减少有机溶剂的使用量, 还能最大限度地回收母液 3中的美罗培南, 极大提高了产品收率, 降低了 生产成本。  This process can be recycled and controlled under the conditions of controlling the quality of meropenem crude and meropenem. It can not only greatly reduce the amount of organic solvent used, but also maximize the recovery of meropenem in mother liquor 3. Greatly improve product yield and reduce production costs.
所述美罗培南粗品及晶种优选按照本发明下文所述方法制得, 也可以 通过现有技术中制备美罗培南的任何方法制备, 如 CN1960992A 或 CN200610083362.7中制备美罗培南的方法。  The meropenem crude and seed crystals are preferably prepared according to the method described below in the present invention, or may be prepared by any of the methods of preparing meropenem in the prior art, such as the method of preparing meropenem in CN1960992A or CN200610083362.7.
优选地, 在该方法中, 在 5 X 105Pa ~ 20 X 105Pa、 优选 15 x 105 Pa ~ 20 χ 105 Pa的压力和 5 ~ 35 °C、优选 10 ~ 25 °C的温度下进行母液的纳滤浓缩。 Preferably, in the method, a pressure of 5 X 10 5 Pa to 20 X 10 5 Pa, preferably 15 x 10 5 Pa to 20 χ 10 5 Pa, and a temperature of 5 to 35 ° C, preferably 10 to 25 ° C The nanofiltration of the mother liquor was concentrated.
并且, 所述母液与所得浓缩液的重量比为 5: 1 ~ 15: 1 , 优选 7: 1 ~ 10: 1 ; 所得浓缩液中美罗培南的含量为 5 ~ 20%, 优选 7 ~ 15%。 Moreover, the weight ratio of the mother liquor to the obtained concentrate is 5:1 to 15:1, preferably 7:1 to 10:1; The content of meropenem in the obtained concentrate is 5 to 20%, preferably 7 to 15%.
此外, 所述结晶得到美罗培南粗品的体系中有机溶剂的总体积与水的 体积比为 3: 1 ~ 6: 1; 有机溶剂选自丙酮、 四氢呋喃、 异丙醇、 曱醇、 乙醇 和曱基乙基酮中的一种或多种。  In addition, the total volume of the organic solvent in the system for obtaining the crude meropenem is 3:1 ~ 6:1; the organic solvent is selected from the group consisting of acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol and sulfhydryl. One or more of ethyl ketones.
本文所述的纳滤浓缩优选按照本发明所述方法进行, 也可应用现有技 术任何方法进行。 所述膜浓缩可以通过聚四氟乙烯纳滤膜、 聚苯乙烯纳滤 膜、 聚醚砜树脂纳滤膜、 复合膜、 醋酸纤维素膜、 聚酰胺膜等进行浓缩, 纳滤浓缩分离设备可购买。 纳滤膜截留有机物的分子量为 150 ~ 500左右。 美罗培南三水合物的分子量为 437.5 , 无水美罗培南分子量为 383.5 , 因此 溶剂分子及水分子可以通过, 而美罗培南被截留下来, 满足这个条件的纳 滤膜就可以应用。  The nanofiltration concentration described herein is preferably carried out in accordance with the methods of the present invention, and can be carried out by any of the methods of the prior art. The membrane concentration can be concentrated by a polytetrafluoroethylene nanofiltration membrane, a polystyrene nanofiltration membrane, a polyethersulfone resin nanofiltration membrane, a composite membrane, a cellulose acetate membrane, a polyamide membrane, etc., and the nanofiltration concentrated separation device can be buy. The molecular weight of the organic membrane retained by the nanofiltration membrane is about 150 to 500. The molecular weight of meropenem trihydrate is 437.5, and the molecular weight of meropenem anhydrous is 383.5. Therefore, solvent molecules and water molecules can pass, and meropenem is trapped, and a nanofiltration membrane that satisfies this condition can be applied.
纳滤浓缩后母液, 优选按照本发明方法加入到后续粗品制备中氢化、 过滤后已析出粗品的母液(母液 2 )或未析出粗品的母液(母液 1 ), 结晶 得到美罗培南粗品。 也可直接加入到现有技术任何方法中的制备美罗培南 粗品的反应液、 结晶液、 过滤后母液中, 同时结晶得到美罗培南粗品。 如 直接将纳滤浓缩液加入 CN1960992A实施例 3中氢化过滤后水溶液, 混合 液滴加四氢呋喃, 同时结晶得到美罗培南粗品; 或直接将纳滤浓缩液加入 CN200610083362.7的实施例 2中过滤完美罗培南(5.1g )的母液中, 直接 结晶得到美罗培南粗品; 或者直接将纳滤浓缩液加入有机溶剂单独结晶回 收, 作为下一批美罗培南粗品。  The mother liquor after concentration by nanofiltration is preferably added to the mother liquor (mother liquor 2) which has been subjected to hydrogenation after the subsequent crude product preparation by the method of the present invention, or the mother liquor (mother liquor 1) in which the crude product is not precipitated, and crystallized to obtain a crude product of meropenem. It can also be directly added to the reaction liquid, the crystallization liquid and the filtered mother liquid for preparing the crude meropenem in any method of the prior art, and simultaneously crystallized to obtain crude meropenem. For example, the nanofiltration concentrate is directly added to the aqueous solution after hydrogenation filtration in CN1960992A, and the mixed solution is added to tetrahydrofuran to obtain the crude meropenem; or the nanofiltration concentrate is directly added to the sample 2 of CN200610083362.7 to filter the perfect roperan. In the mother liquor of (5.1g), direct crystallization of meropenem is obtained; or the nanofiltration concentrate is directly added to the organic solvent to be separately crystallized and recovered as the next batch of crude meropenem.
另一方面, 本发明还提供一种美罗培南原料药的制备方法, 所述方法 包括以下步骤:  In another aspect, the present invention provides a method for preparing a meropenem drug, the method comprising the steps of:
1 )使美罗培南粗品溶解在温度为 50°C ~ 80°C的水中, 再将所得溶液 的温度降至 10°C ~ 30°C得溶液 I;  1) Dissolving the crude meropenem in water at a temperature of 50 ° C ~ 80 ° C, and then reducing the temperature of the resulting solution to 10 ° C ~ 30 ° C to obtain a solution I;
2 )将经步骤 1 )得到的溶液 I经活性炭脱色后过滤, 以得到滤液 II; 2) The solution I obtained in the step 1) is decolorized by activated carbon and filtered to obtain a filtrate II;
3 )将经步骤 2 )得到的滤液 II的温度降至 0°C ~ 20°C以结晶, 过滤后 得到母液 3和滤饼, 所述滤饼经洗晶、 干燥后得到美罗培南原料药; 以及3) The temperature of the filtrate II obtained in the step 2) is lowered to 0 ° C ~ 20 ° C to crystallize, and after filtration, the mother liquid 3 and the filter cake are obtained, and the filter cake is washed and dried to obtain a meropenem raw material drug; as well as
4 )将经步骤 3 )得到的母液 3通过纳滤浓缩后, 加入到下一批粗品制 备中氢化、 过滤后已析出或未析出粗品的母液, 结晶得到美罗培南粗品。 4) The mother liquor 3 obtained in the step 3) is concentrated by nanofiltration, and then added to the next batch of the crude product to be hydrogenated, and the mother liquor which has been precipitated or not precipitated after filtration is crystallized to obtain a crude product of meropenem.
在本发明上述制备方法的步骤 1 ) 中, 以重量百分比计, 美罗培南粗 品中 C17H25N305S的含量不少于 92%, 按无水物计算; 杂质 A、 杂质 B均 不大于 0.8%; 任何未知单个杂质不大于 0.3%; 除 A和 B外其它杂质总和 不大于 3.0%。 其中所述杂质 A为: In the step 1) of the above preparation method of the present invention, the content of C 17 H 25 N 3 5 5 S in the crude product of meropenem is not less than 92% by weight percentage, calculated as anhydrate; impurity A and impurity B are both Not more than 0.8%; any unknown single impurity is not more than 0.3%; the sum of other impurities except A and B is not more than 3.0%. Wherein the impurity A is:
Figure imgf000010_0001
所述杂质 B为:
Figure imgf000010_0001
The impurity B is:
Figure imgf000010_0002
优选地, 在本发明上述制备方法的步骤 1 ) 中, 以重量百分比计, 所 述美罗培南粗品中 C17H25N305S的含量不少于 95%, 以无水物计算; 杂质 A、 杂质 B均不大于 0.6%; 任何未知单个杂质不大于 0.3%; 除 A和 B外 其它杂质总和不大于 2.0%。
Figure imgf000010_0002
Preferably, in the step 1) of the above preparation method of the present invention, the content of C 17 H 25 N 3 5 5 S in the crude meropenem is not less than 95% by weight, calculated as anhydrate; A, impurity B is not more than 0.6%; any unknown single impurity is not more than 0.3%; the sum of other impurities except A and B is not more than 2.0%.
优选地, 步骤 1 ) 中所述使美罗培南粗品溶解在温度为 50°C ~ 80°C的 水中包括: 将所述美罗培南粗品加入到 10 ~ 20倍重量、 优选 15 ~ 20倍重 量的 5 ~ 20 °C的注射用水中, 搅拌混合均匀, 然后将所得混悬物加热到 50 °C ~ 80°C、 优选 60°C ~ 80°C溶解; 其中所述溶解的时间小于 4分钟, 优选 小于 1分钟。  Preferably, the step of dissolving the crude meropenem in water at a temperature of 50 ° C to 80 ° C in the step 1) comprises: adding the crude meropenem to 10 to 20 times by weight, preferably 15 to 20 times by weight of 5 ~ 20 ° C in water for injection, stir and mix evenly, and then the resulting suspension is heated to 50 ° C ~ 80 ° C, preferably 60 ° C ~ 80 ° C dissolved; wherein the dissolution time is less than 4 minutes, preferably Less than 1 minute.
溶解之后, 优选地, 将所得溶液的温度降至 10°C ~ 25°C ; 其中降温的 时间小于 4分钟, 优选小于 1分钟。  After dissolution, preferably, the temperature of the resulting solution is lowered to 10 ° C to 25 ° C; wherein the time for cooling is less than 4 minutes, preferably less than 1 minute.
其中步骤 1 ) 中的温度升高和降低均可通过换热器进行, 例如中国专 利申请 CN201120235961.2 中所述的换热器。 优选釆用本发明的方法利用 换热器换热快速溶解并快速降温; 也可釆用任何可以达到快速溶解的方式 溶解美罗培南粗品, 釆用任何可以达到快速降温的方式将溶液降温。  The temperature rise and fall in step 1) can be carried out by means of a heat exchanger, for example the heat exchanger described in the Chinese patent application CN201120235961.2. Preferably, the method of the present invention utilizes the heat exchange of the heat exchanger to rapidly dissolve and rapidly cool the temperature; the crude meropenem can be dissolved by any means which can achieve rapid dissolution, and the solution can be cooled by any means which can achieve rapid cooling.
在本发明方法的步骤 2 ) 中, 溶液 I可以在 15°C ~ 25°C下经釆用美罗 培南粗品重量 1 ~ 20%的活性炭脱色 1 ~ 30分钟、优选 1 ~ 10分钟后过滤, 以得到滤液 II。  In the step 2) of the method of the present invention, the solution I can be decolorized by using 1 to 20% of the activated carbon of the meropenem weight of 1 to 20% at 15 ° C to 25 ° C for 1 to 30 minutes, preferably 1 to 10 minutes, and then filtered. The filtrate II was obtained.
或者, 步骤 2 ) 中, 溶液通过活性炭过滤器在线过滤脱色。 优选釆用 本发明的方法进行活性炭处理, 该溶液也可釆用任何已知方式进行活性炭 处理, 所用的活性炭未作特别限制。 Alternatively, in step 2), the solution is decolorized by in-line filtration through an activated carbon filter. Preferably, the activated carbon treatment is carried out by the method of the invention, and the solution can also be activated by any known means. The activated carbon used is not particularly limited.
在本发明方法的步骤 3)中包括, 将滤液 II的温度降至 0°C ~5°C以结 晶, 并养晶 2 ~ 20小时, 优选 5 ~ 10小时; 过滤后得到母液 3和滤饼, 所 述滤饼用丙酮淋洗以洗晶,在 20°C ~40°C、优选 25°C ~30°C下真空干燥 3 ~ 10小时、 优选 5~6小时, 从而得到美罗培南原料药。 其中, 所述养晶优 选为搅拌养晶, 搅拌速度为 100 ~ 200转 /分钟, 优选 110 ~ 130转 /分钟。 本发明的养晶时间是指晶体生长时间, 步骤 3) 所述养晶时间为加入晶种 析晶至过滤之间的那段晶体生长的时间。  In the step 3) of the method of the present invention, the temperature of the filtrate II is lowered to 0 ° C ~ 5 ° C for crystallization, and crystallized for 2 ~ 20 hours, preferably 5 ~ 10 hours; filtered to obtain the mother liquid 3 and the filter cake The filter cake is washed with acetone to wash the crystal, and dried under vacuum at 20 ° C to 40 ° C, preferably 25 ° C to 30 ° C for 3 to 10 hours, preferably 5 to 6 hours, thereby obtaining a meropenem drug substance. . Wherein, the crystal is preferably stirred and crystallized, and the stirring speed is 100 to 200 rpm, preferably 110 to 130 rpm. The crystal growth time of the present invention refers to the crystal growth time, and the step 3) the crystal growth time is the time during which the crystal growth between the seed crystals and the filtration is added.
步骤 3)的析晶过程中可添加或不添加晶种, 优选添加晶种。 优选地, 步骤 3)还包括, 在结晶前向步骤 2)得到的滤液 II中添加晶种; 其中添 加晶种的温度为 0°C ~20°C, 优选 0°C ~5°C; 添加的晶种与美罗培南粗品 的质量比为 1%:1 ~ 10%:1, 优选 1%:1 ~2%:1。  In the crystallization process of step 3), seed crystals may or may not be added, and seed crystals are preferably added. Preferably, the step 3) further comprises: adding seed crystals to the filtrate II obtained in the step 2) before crystallization; wherein the temperature of the seed crystal is 0 ° C ~ 20 ° C, preferably 0 ° C ~ 5 ° C; The mass ratio of the seed crystal to the crude product of meropenem is 1%: 1 ~ 10%: 1, preferably 1%: 1 ~ 2%: 1.
更优选地, 步骤 3 ) 中在结晶前, 取滤液 II的 1% ~ 10% (重量比), 向其中加入有机溶剂结晶形成晶种,将所得晶种加入到剩余的滤液 II中以 进行结晶 (如在结晶罐中); 其中, 所述有机溶剂选自丙酮、 四氢呋喃、 异丙醇、 曱醇、 乙醇和曱基乙基酮中的一种或多种, 优选丙酮和 /或四氢呋 喃; 所述部分滤液 II与有机溶剂的重量 (kg) :体积 (L) 比为 1:2 ~ 1:6, 晶种制备温度为 5°C ~20°C, 优选 10°C ~15°C。  More preferably, in step 3), 1% to 10% by weight of the filtrate II is taken before crystallization, crystallized by adding an organic solvent thereto, and the obtained seed crystal is added to the remaining filtrate II for crystallization. (in the crystallization tank); wherein the organic solvent is selected from one or more of acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol and mercaptoethyl ketone, preferably acetone and/or tetrahydrofuran; The weight (kg) of the partial filtrate II and the organic solvent is 1:2 to 1:6, and the seed crystal preparation temperature is 5 ° C to 20 ° C, preferably 10 ° C to 15 ° C.
在本发明方法的步骤 4) 中, 在 5 X 105Pa~20 X 105Pa、 优选 15 x 105 Pa ~ 20 χ 105 Pa的压力和 5 ~ 35°C、 优选 10 ~ 25 °C的温度下进行母液 3的 纳滤浓缩,使得所述母液 3与所得浓缩液的重量比为 5:1 ~ 15:1,优选 7:1 ~ 10:1; 所得浓缩液中美罗培南含量为 5 ~ 20重量%, 优选 7~15重量%。 In step 4) of the method of the invention, at a pressure of 5 X 10 5 Pa~20 X 10 5 Pa, preferably 15 x 10 5 Pa ~ 20 χ 10 5 Pa and 5 to 35 ° C, preferably 10 to 25 ° C The nanofiltration concentration of the mother liquor 3 is carried out at a temperature such that the weight ratio of the mother liquor 3 to the obtained concentrate is 5:1 to 15:1, preferably 7:1 to 10:1; and the meropenem content in the obtained concentrate is 5 ~ 20% by weight, preferably 7 to 15% by weight.
优选地, 步骤 4) 中所述结晶得到美罗培南粗品的体系中有机溶剂的 总体积与水的体积比为 3:1 ~6:1; 有机溶剂选自丙酮、 四氢呋喃、 异丙醇、 曱醇、 乙醇和曱基乙基酮中的一种或多种; 优选地, 结晶温度为 5°C ~15 °C。  Preferably, the crystallization of the crude meropenem in the step 4) gives a volume ratio of the total volume of the organic solvent to the water of 3:1 to 6:1; the organic solvent is selected from the group consisting of acetone, tetrahydrofuran, isopropanol, and decyl alcohol. One or more of ethanol and mercaptoethyl ketone; preferably, the crystallization temperature is from 5 ° C to 15 ° C.
进一步优选地, 所述氢化、 过滤后已析出粗品的母液(母液 2) 或未 析出粗品的母液(母液 1) 为通过下述方法制备美罗培南粗品过程中的母 液 1和母液 2;  Further preferably, the mother liquor (mother liquor 2) in which the crude product has been precipitated after hydrogenation or filtration or the mother liquor (mother liquor 1) in which the crude product is not precipitated is the mother liquor 1 and the mother liquor 2 in the process of preparing the crude meropenem by the following method;
将保护美罗培南(或者保护美罗培南浓缩液)、 THF、 水、 3,5,-二曱基 吡啶、 10%钯碳一并加入到高压反应釜中, 除去空气, 通入氢气, 室温反 应毕, 过滤洗涤回收钯碳, 得到未析出粗品的母液, 此母液可作为未析出 粗品的母液用, 简称母液 1; 此母液中加入有机溶剂, 控制温度 10-15 °C搅拌, 过滤, 洗涤, 产品 干燥, 得美罗培南 (化合物 I )粗品; 母液为已析出粗品的母液, 此母液 可作为已析出粗品的母液用, 简称母液 2。 Add meropenem (or protect meropenem concentrate), THF, water, 3,5,-dimercaptopyridine, 10% palladium carbon to the autoclave, remove the air, pass hydrogen, and react at room temperature. , washing and recovering palladium carbon to obtain a mother liquid without precipitation of crude product, the mother liquid can be used as a mother liquid without precipitation of crude product, referred to as mother liquor 1; The mother liquor is added with an organic solvent, the temperature is controlled at 10-15 ° C, the mixture is filtered, washed, and the product is dried to obtain a crude product of meropenem (Compound I); the mother liquor is a mother liquor which has been precipitated as a crude liquid, and the mother liquor can be used as a mother liquor for which a crude product has been precipitated. , referred to as mother liquor 2.
所述有机溶剂选自四氢呋喃、 丙酮、 异丙醇、 曱醇、 乙醇、 曱基乙基 酮的一种或多种; 优选四氢呋喃、 丙酮; 优选地, 母液 2中有机溶剂体积 之和与水的体积比为 3: 1 ~ 6: 1。  The organic solvent is selected from one or more of tetrahydrofuran, acetone, isopropanol, decyl alcohol, ethanol, mercaptoethyl ketone; preferably tetrahydrofuran, acetone; preferably, the sum of the volume of the organic solvent in the mother liquor 2 and water The volume ratio is 3: 1 ~ 6: 1.
根据上述方法制备得到的美罗培南原料药中, 美罗培南的含量为 98.5% ~ 101.0%, 以无水物计算; 所述原料药的有关物质中杂质 A、 杂质 B均不大于 0.25%; 任何未知单个杂质不大于 0.05%; 除 A和 B外其它杂 质总和不大于 0.2%; 丙酮残留不大于 400ppm, 优选不大于 lOOppm;  According to the above method, the content of meropenem is 98.5% ~ 101.0%, calculated as anhydrate; the impurity A and the impurity B in the related substances of the raw material drug are not more than 0.25%; a single impurity is not more than 0.05%; the sum of other impurities except A and B is not more than 0.2%; the acetone residue is not more than 400ppm, preferably not more than 100ppm;
其中杂质 A为:  Among them, impurity A is:
Figure imgf000012_0001
杂质 B为:
Figure imgf000012_0001
Impurity B is:
Figure imgf000012_0002
Figure imgf000012_0002
再一方面, 本发明提供了一种美罗培南药物组合物, 该药物组合物包 含本发明提供的美罗培南原料药和药学上可接受的辅料; 优选地, 该辅料 为无菌碳酸钠, 其中美罗培南原料药与无菌碳酸钠的重量比为 1000: 195 ~ 1000: 222, 优选 1000:208; 优选地, 所述药物组合物为注射剂。  In a further aspect, the present invention provides a meropenem pharmaceutical composition comprising the meropenem drug of the present invention and a pharmaceutically acceptable excipient; preferably, the excipient is sterile sodium carbonate, wherein the The weight ratio of the drug substance to the sterile sodium carbonate is 1000: 195 to 1000: 222, preferably 1000: 208; preferably, the pharmaceutical composition is an injection.
在所述美罗培南药物组合物中, 所述原料药中美罗培南的含量为 98.5% ~ 101.0%, 以无水物计算; 所述原料药的有关物质中杂质 A、 杂质 B均不大于 0.25%; 任何未知单个杂质不大于 0.05%; 除 A和 B外其它杂 质总和不大于 0.2%; 丙酮残留不大于 400ppm, 优选不大于 100ppm。  In the meropenem pharmaceutical composition, the content of meropenem in the drug substance is 98.5% ~ 101.0%, calculated as an anhydrate; the impurity A and the impurity B in the related substances of the drug substance are not more than 0.25%. Any unknown single impurity is not more than 0.05%; the sum of other impurities except A and B is not more than 0.2%; the acetone residue is not more than 400ppm, preferably not more than 100ppm.
本发明还提供该注射用的美罗培南药物组合物的制备方法, 所述方法 包括: 将无菌美罗培南原料药、 无菌碳酸钠粉碎, 检测符合无菌及粒度要 求, 按照美罗培南原料药与无菌碳酸钠的重量比为 1000: 195 ~ 1000: 222, 釆用高效混合机混合均勾, 将包装容器进行无菌处理, 灌装, 按照美国药 典 USP32-NF27注射用美罗培南项下方法检测合格, 包装入库。 The invention also provides a preparation method of the meropenem pharmaceutical composition for injection, the method comprising: pulverizing the sterile meropenem drug substance and the sterile sodium carbonate, and detecting the sterility and the particle size requirement, according to the meropenem drug substance and The weight ratio of sterile sodium carbonate is 1000: 195 ~ 1000: 222, and the mixture is mixed with a high-efficiency mixer. The packaging container is aseptically processed and filled according to the US medicine. The USP32-NF27 injection was tested by meropenem and packaged into the warehouse.
本发明提供的注射用的美罗培南药物组合物, 具有更好的稳定性, 长 期储存后澄清度与颜色依然符合要求, 能够保证药品的安全、 有效。  The meropenem pharmaceutical composition for injection provided by the invention has better stability, and the clarity and color after long-term storage still meet the requirements, and the medicine can be ensured to be safe and effective.
在不脱离本发明构思的前提下, 本发明可以进行任何可能的变化或替 换, 均属于本发明的保护范围。  It is within the scope of the present invention to make any possible variations or substitutions of the present invention without departing from the spirit and scope of the invention.
未作特别说明的话, 本发明检测方法中含量测定项、 有关物质项、 残 留溶剂项, 均按照美国药典 USP32-NF27中美罗培南 ( Meropenem ) 项下 的方法进行,即本发明提供的美罗培南原料药,所述原料药中美罗培南的含 量为 98.5% ~ 101.0%, 以无水物计算; 所述原料药有关物质中: 任一两个 主要杂质 (杂质 A和杂质 B ) 不得大于 0.25%, 按无水物计算; 其他单个 杂质不得大于 0.05%, 按无水物计算; 其他杂质总和不得大于 0.2%。 丙酮 残留不大于 400ppm ( 0.04% ), 优选不大于 100ppm。 标准中任一两个主要 杂质指杂质 A和杂质 B, 杂质 A和杂质 B的相对保留时间 (以美罗培南 的保留时间约 6min为基准) 分别约为 0.5和 2.2。  Unless otherwise specified, the content determination item, the related substance item, and the residual solvent item in the detection method of the present invention are all carried out according to the method of Meropenem in the United States Pharmacopoeia USP32-NF27, that is, the meropenem raw material provided by the present invention. Medicine, the content of meropenem in the raw material medicine is 98.5% ~ 101.0%, calculated as anhydrate; in the related substances of the raw material medicine: any two main impurities (impurity A and impurity B) shall not be greater than 0.25%, Calculated as anhydrate; other individual impurities shall not be greater than 0.05%, calculated as anhydrate; the sum of other impurities shall not be greater than 0.2%. The acetone residue is not more than 400 ppm (0.04%), preferably not more than 100 ppm. The two main impurities in the standard refer to the relative retention times of impurity A and impurity B, impurity A and impurity B (based on the retention time of meropenem for about 6 minutes) of about 0.5 and 2.2, respectively.
其中杂质 A为:  Among them, impurity A is:
Figure imgf000013_0001
Figure imgf000013_0002
Figure imgf000013_0001
Figure imgf000013_0002
单分子开环物(Mw: 401 ),可以为其异构体 A2:
Figure imgf000013_0003
Single molecule ring-opening (Mw: 401), which can be its isomer A 2 :
Figure imgf000013_0003
A2 A 2
杂质 B为一分子美罗培南与一分子开环物的二聚体(Mw: 766 ), 也 可以为其异构体 B2: Impurity B is a dimer of one molecule of meropenem and one molecule of ring-opening (Mw: 766), or it can be its isomer B 2 :
Figure imgf000014_0001
质量控制指标对能否保证产品的有效、 安全至关重要, 在美罗培南或 任何活性药物成分(API ) 中的杂质和残留溶剂为多余的, 只有对杂质进 行清晰地限定, 对超过鉴定限度的杂质研究鉴定该杂质的化学结构, 才能 根据杂质的性质, 有针对性地制订杂质限度, 才能保证原料药及制剂的安 全、有效。 另外,原料药及制剂的稳定性出现问题也关系到药物的安全性、 有效性不能得到保证, 所以原料药及制剂具有更好的稳定性也是更安全、 有效的保证。
Figure imgf000014_0001
Quality control indicators are essential for ensuring the effectiveness and safety of the product. Impurities and residual solvents in meropenem or any active pharmaceutical ingredient (API) are superfluous, only the impurities are clearly defined, and the limits of identification are exceeded. Impurity studies identify the chemical structure of the impurity, in order to determine the impurity limit according to the nature of the impurity, in order to ensure the safety and effectiveness of the drug substance and preparation. In addition, the problem of the stability of the drug substance and the preparation is also related to the safety and effectiveness of the drug, so that the stability of the drug substance and the preparation is safer and more effective.
与现有技术相比, 本发明的有益效果在于:  Compared with the prior art, the beneficial effects of the invention are:
1 ) 本发明提供的美罗培南原料药纯度高、 杂质状况清晰、 溶媒残留 低、 溶解性好、 质量控制指标能够保证产品有效、 安全。  1) The meropenem raw material provided by the invention has high purity, clear impurity condition, low solvent residue, good solubility, and quality control index can ensure the product is effective and safe.
2 ) 本发明提供的美罗培南原料药, 具有更好的稳定性, 长期储存后 澄清度与颜色依然符合药典要求, 引起副作用的可能性更小。  2) The meropenem drug substance provided by the invention has better stability, and the clarity and color after long-term storage still meet the requirements of the pharmacopoeia, and the possibility of causing side effects is smaller.
3 )本发明将美罗培南粗品经纯化水精制得到高品质美罗培南原料药, 并且所得母液 3经过纳滤膜浓缩后加入到后续粗品制备中氢化、 过滤后已 析出粗品的母液(母液 2 ) 或未析出粗品的母液(母液 1 ) 中, 结晶得到 美罗培南粗品。 取消了该母液单独回收步骤, 缩短了工时, 不仅能够大大 地减少有机溶剂的使用量, 还能最大限度地回收母液 3中的美罗培南, 极 大提高了产品收率, 显著降低了生产成本。  3) In the present invention, the crude product of meropenem is purified by purified water to obtain a high-quality meropenem drug substance, and the mother liquid 3 obtained is concentrated by a nanofiltration membrane, and then added to a crude liquid preparation (hydrogen mother 2) after being subjected to hydrogenation after filtration and filtration. In the mother liquor (mother liquor 1) in which no crude product was precipitated, the crude product of meropenem was obtained by crystallization. The separate recovery step of the mother liquor is eliminated, the working hours are shortened, the amount of organic solvent used can be greatly reduced, and the meropenem in the mother liquor 3 can be recovered as much as possible, the product yield is greatly improved, and the production cost is remarkably reduced.
4 ) 本发明可在较低温度下, 较短时间内浓缩对热不稳定的美罗培南 溶液, 大大减少了美罗培南的分解, 纳滤浓缩过程易控, 温升很低, 可确 保产品在料液内不变质。  4) The invention can concentrate the heat-labile meropenem solution in a relatively short time at a relatively low temperature, greatly reducing the decomposition of meropenem, the nanofiltration concentration process is easy to control, and the temperature rise is low, which ensures that the product is in the material. The liquid does not deteriorate.
5 )从浓缩结果可知, 美罗培南的分解未被检测到; 废水液中美罗培 南残留未检出, 浓缩收率为 100%, 说明操作条件合适, 纳滤膜截留分离 效果较好, 适宜现有产品的分离。  5) It can be seen from the concentration results that the decomposition of meropenem is not detected; the residue of meropenem in the wastewater is not detected, and the concentrated yield is 100%, indicating that the operating conditions are appropriate, and the nanofiltration membrane has good separation and separation effect, which is suitable for existing Separation of the product.
6 ) 本发明工艺简单、 成本极低、 工艺紧凑、 控制简单, 所得美罗培 南原料药纯度高、 溶媒残留低、 溶解性好、 长期储存稳定性好, 适用于工 业大规模无菌的美罗培南原料药及药物制剂生产。 附图说明 6) The invention has the advantages of simple process, low cost, compact process and simple control, and the obtained meropenem raw material has high purity, low solvent residue, good solubility and good long-term storage stability, and is suitable for industrial large-scale sterile meropenem raw materials. Production of pharmaceuticals and pharmaceutical preparations. DRAWINGS
为了更好地理解本发明的本质, 下面结合附图, 通过对本发明较佳实 施方式的描述, 详细说明但不限制本发明。 其中:  The invention will be described in detail, but not by way of limitation, the description of the preferred embodiments of the invention. among them:
图 1为杂质 A的核磁碳谱;  Figure 1 shows the nuclear magnetic carbon spectrum of impurity A;
图 2为杂质 A的核磁氢谱;  Figure 2 is the nuclear magnetic resonance spectrum of impurity A;
图 3为杂质 A的红外分析图谱;  Figure 3 is an infrared analysis spectrum of impurity A;
图 4为杂质 A的质谱图;  Figure 4 is a mass spectrum of impurity A;
图 5为杂质 A的紫外吸收图谱;  Figure 5 is an ultraviolet absorption spectrum of impurity A;
图 6为杂质 B的核磁氢谱;  Figure 6 is the nuclear magnetic resonance spectrum of impurity B;
图 7为杂质 B的红外分析图谱;  Figure 7 is an infrared analysis spectrum of impurity B;
图 8为杂质 B的质谱图;  Figure 8 is a mass spectrum of impurity B;
图 9为杂质 B的紫外吸收图谱。  Figure 9 shows the ultraviolet absorption spectrum of impurity B.
图 10为本发明制备方法工艺流程图 实施发明的最佳方式  Figure 10 is a flow chart of the preparation method of the present invention. The best mode for carrying out the invention
以下各实施例中所使用的原料、 试剂、 溶剂和其它试验材料、 膜浓缩 分离设备, 均为可以通过商购获得。  The materials, reagents, solvents, and other test materials and membrane concentration separation equipment used in the following examples are all commercially available.
保护美罗培南(式 la )或者保护美罗培南的浓缩液可由现有技术任何 方法制得, 如 CN200610083362.7所示方法。  The concentrate protecting meropenem (formula) or protecting meropenem can be prepared by any method known in the art, such as the method shown in CN200610083362.7.
美罗培南粗品可以参照实施例 13 的方法制备, 也可以通过现有技术 中制备美罗培南的任何方法制备, 如 CN1960992A或 CN200610083362.7 中制备美罗培南的方法。  The crude meropenem can be prepared by the method of Example 13, or by any method of preparing meropenem in the prior art, such as the method of preparing meropenem in CN1960992A or CN200610083362.7.
以重量百分比计, 所述美罗培南粗品中 C17H25N305S 的含量不少于 92%, 以无水物计算; 杂质 A、 杂质 B均不大于 0.8%; 任何未知单个杂质 不大于 0.3%; 除 A和 B外其它杂质总和不大于 3.0%。 The content of C 17 H 25 N 3 5 5 S in the crude meropenem is not less than 92%, calculated as anhydrate; the impurity A and the impurity B are not more than 0.8%; any unknown single impurity is not More than 0.3%; the sum of other impurities except A and B is not more than 3.0%.
未作特别说明的话, 本发明检测方法中含量测定项、 有关物质项、 残 留溶剂项均按照美国药典 USP32-NF27中美罗培南 ( Meropenem ) 项下的 方法进行。 稳定性考察试验按照美国药典 USP32-NF27方法进行。  Unless otherwise specified, the content determination item, the related substance item, and the residual solvent item in the detection method of the present invention are carried out in accordance with the method of Meropenem in the United States Pharmacopoeia USP32-NF27. The stability test was conducted in accordance with the United States Pharmacopoeia USP32-NF27 method.
所用仪器: 核磁共振( Varian 300 ); 红外光语 ( NICOLET 170SX FT ~ IR );质谱( API2000 );紫外光语( Thermo Spectronic 300 );液质联用( Agilent 1100 HPLC- AB API2000质谱 ); 制备液相色谱 ( Waters 2535 ); 元素分析 (德国 ELEMENTAR公司 vario EL元素分析仪)。 实施例 1 Apparatus used: nuclear magnetic resonance (Varian 300); infrared light language (NICOLET 170SX FT ~ IR); mass spectrometry (API2000); ultraviolet light ( Thermo Spectronic 300); LC/MS (Agilent 1100 HPLC-AB API2000 mass spectrometry); preparation Liquid chromatography (Waters 2535); Elemental analysis (Germany ELEMENTAR vario EL elemental analyzer). Example 1
将美罗培南粗品 1kg加入到 20kg温度为 10°C的注射用水中, 搅拌混 合均勾, 将混悬物通过换热器瞬间加热到 80°C溶解, 并通过换热器迅速降 到常温 25 °C , 得溶液 I。  Add 1kg of meropenem to 20kg of water for injection at a temperature of 10 °C, stir and mix, and then suspend the suspension through a heat exchanger to 80 ° C for dissolution, and quickly drop to 25 °C through a heat exchanger. C, solution I is obtained.
通过活性炭过滤器在线过滤脱色溶液 I, 得到滤液 II。  The decolorizing solution I was filtered in-line through an activated carbon filter to obtain a filtrate II.
放出 210g的滤液 II, 设定温度为 10°C , 加入 1050ml丙酮, 搅拌 15 分钟后过滤得到晶种。 降温至 2°C , 将制得的晶种加入剩余的 20.8kg滤液 II中, 保持搅拌速度为 130转 /分钟, 养晶 8小时, 过滤, 得到母液 3 , 母 液 3进入下一步纳滤浓缩。  210 g of the filtrate II was discharged, the temperature was set to 10 ° C, 1050 ml of acetone was added, and the mixture was stirred for 15 minutes, and then filtered to obtain a seed crystal. The temperature was lowered to 2 ° C, and the obtained seed crystals were added to the remaining 20.8 kg of the filtrate II, the stirring speed was maintained at 130 rpm, the crystal was maintained for 8 hours, and filtered to obtain a mother liquid 3, and the mother liquid 3 was subjected to the next nanofiltration concentration.
滤饼用丙酮淋洗, 滤饼真空 30°C干燥 5小时, 粉碎, 得到美罗培南原 料药 680g, 收率 68%。  The filter cake was rinsed with acetone, and the filter cake was dried under vacuum at 30 ° C for 5 hours, and pulverized to obtain meragene saponin 680 g, yield 68%.
其中美罗培南的含量为 99.6% (以无水物计); 有关物质中杂质 A为 0.06%; 杂质 B为 0.11%; 任何未知单个杂质为 0.02%; 除 A和 B外其它 杂质总和为 0.05%; 丙酮残留为 80ppm。  The content of meropenem is 99.6% (based on anhydrous matter); the impurity A in the relevant substance is 0.06%; the impurity B is 0.11%; any unknown single impurity is 0.02%; the sum of other impurities except A and B is 0.05% The acetone residue is 80 ppm.
一、 美罗培南结构确定:  First, the structure of meropenem is determined:
美罗培南原料药物理性质测定结果为:  The physical properties of the meropenem drug substance are as follows:
元素分析: C17H25N305S'3H20 Elemental analysis: C 17 H 25 N 3 0 5 S'3H 2 0
计算值: C, 46.67%; H, 7.14%; N, 9.60%; S, 7.33%;  Calculated: C, 46.67%; H, 7.14%; N, 9.60%; S, 7.33%;
实测值: C, 46.38%; H, 7.40%; N, 9.68%; S, 7.26%。  Found: C, 46.38%; H, 7.40%; N, 9.68%; S, 7.26%.
UV固 2。謹: 296 UV solid 2 . Dear: 296
IR^^cm"1: 1755, 1627, 1393, 1252, 1130. IR^^cm" 1 : 1755, 1627, 1393, 1252, 1130.
ifi-NMR (D20, δ/ppm): : 1.21(3H, d, J=7.1 Hz), 1.29 ( 3H, d, J=6.3Hz ) 1.97(1H, m), 2.99(3H, s), 3.06(3H, s), 3.09 (1H, m), 3.38(1H, m), 3.46(2H, m), 3.77(1H, dd, J=11.9和 6.2Hz), 4.05(1H, m), 4.23(2H, m),4.82(lH)。 Ifi-NMR (D 2 0, δ/ppm): : 1.21 (3H, d, J = 7.1 Hz), 1.29 ( 3H, d, J = 6.3 Hz ) 1.97 (1H, m), 2.99 (3H, s) , 3.06(3H, s), 3.09 (1H, m), 3.38(1H, m), 3.46(2H, m), 3.77(1H, dd, J=11.9 and 6.2Hz), 4.05(1H, m), 4.23 (2H, m), 4.82 (lH).
结论: 物理性质测定结果与美罗培南结构吻合。  Conclusion: The results of physical properties are consistent with the structure of meropenem.
二、 杂质研究过程  Second, the impurity research process
1、 初步分离鉴定:  1. Initial separation and identification:
首先利用液质联用系统对各个杂质进行了分离和质谱测定, 参考美国 药典 USP32-NF27中美罗培南 ( Meropenem ) 项下的流动相, 釆用醋酸来 代替磷酸配制流动相, 二者图谱非常一致, 得到了各个杂质的分子量, 初 步确定了结构; 根据液相图谱, 杂质 A和杂质 B的相对保留时间(以美罗 培南的保留时间约 6min为基准) 分别为 0.5和 2.2。  First, the impurities were separated and mass spectrometrically determined by the LC/MS system. Refer to the mobile phase under Meropenem in USP32-NF27, and use acetic acid instead of phosphoric acid to prepare the mobile phase. The spectra are very consistent. The molecular weight of each impurity was obtained, and the structure was initially determined. According to the liquid phase spectrum, the relative retention times of impurity A and impurity B (based on the retention time of meropenem for about 6 min) were 0.5 and 2.2, respectively.
2、 杂质的液相制备: 为了得到较多样品进行进一步验证, 参考初步分离鉴定中的流动相条 件, 利用制备液相色谱, 分离出杂质 A B, 反复多次制备, 得到所有杂 质的盐溶液, 杂质量达到毫克级。 2. Liquid phase preparation of impurities: In order to obtain more samples for further verification, referring to the mobile phase conditions in the preliminary separation and identification, the preparative liquid chromatography is used to separate the impurity AB, and the preparation is repeated several times to obtain a salt solution of all the impurities, and the impurity amount reaches the milligram level.
3、 杂质的化学合成:  3. Chemical synthesis of impurities:
根据杂质的性质, 对杂质 A和 B进行了化学合成, 得到 lg杂质 A, 纯度 >95%; 杂质 B约 50毫克, 纯度 >90%  According to the nature of the impurities, the impurities A and B are chemically synthesized to obtain lg impurity A, purity >95%; impurity B is about 50 mg, purity >90%
1 ) 杂质 A的合成:  1) Synthesis of impurity A:
按照 The Journal of Antibiotics Vol.46 No.5 P831 ~ P832所述方法制备 得到杂质 A, 经结构确认为杂质 A, 并与文献相符。  The impurity A was prepared according to the method described in The Journal of Antibiotics Vol. 46 No. 5 P831 to P832, and confirmed to be an impurity A by the structure, and was in conformity with the literature.
2 ) 杂质 B的合成:  2) Synthesis of impurity B:
按照 Chem. Pharm. Bull. 43(4) P690 (1995)所述方法制备得到杂质 B, 经结构确认为杂质 B, 并与文献相符。  Impurity B was prepared according to the method described in Chem. Pharm. Bull. 43(4) P690 (1995), confirmed by structure as impurity B, and in accordance with the literature.
4、 合成杂质八、 B与产品液相分离杂质 A B对比:  4, synthetic impurities VIII, B and product liquid phase separation impurities A B comparison:
利用合成得到杂质 A B与产品液相分离杂质 A B对比, 首先对紫 外图谱进行了比较, 结果表明分别对应于 A B杂质; 为了进一步验证, 釆用加样法,将化学合成得到的杂质 A和 B分别定性加入实验得到的美罗 培南原料药中, 根据所得液相图谱中相应杂质峰面积增加的情况, 进一步 判定产品中的杂质 A和 B与合成得到的 A B杂质完全一致。  The impurity AB obtained by synthesis is compared with the impurity AB in the liquid phase of the product. First, the UV spectra are compared, and the results indicate that they correspond to AB impurities respectively. For further verification, the impurities A and B obtained by chemical synthesis are respectively added by the addition method. Qualitatively adding the meropenem drug substance obtained by the experiment, according to the increase of the corresponding impurity peak area in the obtained liquid phase spectrum, it is further determined that the impurities A and B in the product are completely consistent with the synthesized AB impurity.
5、 杂质 A B结构确认  5, impurities A B structure confirmation
1 ) 杂质 A物理性质测定结果为:  1) Impurity A Physical property determination results are:
UV (λ mo): ~ 275nm. UV (λ mo ): ~ 275nm.
IR (KBr, cm"1): 3438.8, 2889.2, 2599.9, 1750.5, 1654.8, 1595.0, 1386.7, 1336.6, 1155.3, 781.1. IR (KBr, cm" 1 ): 3438.8, 2889.2, 2599.9, 1750.5, 1654.8, 1595.0, 1386.7, 1336.6, 1155.3, 781.1.
MS (m/z): 401.9 (M+l), 802.6 (2xM+l).  MS (m/z): 401.9 (M+l), 802.6 (2xM+l).
ifi-NMR (D20, δ/ppm): 1.26 (t, J = 7.2, 1.5H, CH3-CH-OH, A); 1.33 (t, J = 6.9, 3H, 1- -CH3, A+A2); 1.49 (d, J = 6.6, 1.5H, CH3-CH-OH, A2); 1.85 ~ 2.15 (m, CH-CH2-CH, A2); 2.3 ~ 2.41 (m, CH3-CH-CH, A2); 2.6 ~ 2.7 (m, S-CH-CH2, A2); 2.8 ~ 3.1 (m, N-CH2-CH, CH-CH-NH, A2); 3.03 (s, 3H, N-CH3, A+A2); 3.1 (s, 3H, N-CH3, A+A2); 3.35-3.45 (m, CH-CH2-CH, A); 3.65 - 3.78 (m, CH3-CH-CH, A); 3.8 ~ 4.0 (m, N-CH2-CH, A, CH2-CH-NH, A+A2); 4.1 ~ 4.3 (m, CH-CH-COOH, A+A2); 4.3 ~ 4.36 (dd, CH-CH-NH, A); 4.47 ~ 4.6 (m, CH3-CH-OH, A+A2). Ifi-NMR (D 2 0, δ/ppm): 1.26 (t, J = 7.2, 1.5H, CH 3 -CH-OH, A); 1.33 (t, J = 6.9, 3H, 1- -CH 3 , A+A2); 1.49 (d, J = 6.6, 1.5H, CH 3 -CH-OH, A2); 1.85 ~ 2.15 (m, CH-CH 2 -CH, A2); 2.3 ~ 2.41 (m, CH 3 -CH-CH, A2); 2.6 ~ 2.7 (m, S-CH-CH 2 , A2); 2.8 ~ 3.1 (m, N-CH 2 -CH, CH-CH-NH, A2); 3.03 (s, 3H, N-CH 3 , A+A2); 3.1 (s, 3H, N-CH 3 , A+A2); 3.35-3.45 (m, CH-CH 2 -CH, A); 3.65 - 3.78 (m, CH 3 -CH-CH, A); 3.8 ~ 4.0 (m, N-CH 2 -CH, A, CH 2 -CH-NH, A+A2); 4.1 ~ 4.3 (m, CH-CH-COOH, A +A2); 4.3 ~ 4.36 (dd, CH-CH-NH, A); 4.47 ~ 4.6 (m, CH 3 -CH-OH, A+A2).
13C-NMR (D20, δ/ppm): 12.88, 15.55, 17.25, 18.21, 22.3, 23.0, 23.74, 37.76, 38.94, 39.77, 41.74, 44.21, 45.11, 45.6, 46.05, 49.36, 52.0, 54.16, 54.62, 55.15, 57.37, 60.23, 61.02, 62.57, 67.0, 71.73, 93.9, 100.48, 124.56, 170.43, 172.84, 174.25, 177.39, 180.82, 182.1. 13 C-NMR (D 2 0, δ/ppm): 12.88, 15.55, 17.25, 18.21, 22.3, 23.0, 23.74, 37.76, 38.94, 39.77, 41.74, 44.21, 45.11, 45.6, 46.05, 49.36, 52.0, 54.16, 54.62, 55.15, 57.37, 60.23, 61.02, 62.57, 67.0, 71.73, 93.9, 100.48, 124.56, 170.43, 172.84, 174.25, 177.39, 180.82, 182.1.
结论: 物理性质测定结果与杂质 A结构吻合, 相关谱图见图 1-5 2 ) 杂质 B物理性质测定结果为:  Conclusion: The physical property determination results are in agreement with the impurity A structure. The correlation spectrum is shown in Figure 1-5. 2) Impurity B Physical property determination results are:
υν (λ H20): 297 Υν (λ H20 ) : 297
IR (KBr, cm"1): 3398.3, 2966.3, 2871.8, 1751.2, 1627.8, 1396.4, 1263.3, 1145.6, 781.1 IR (KBr, cm" 1 ): 3398.3, 2966.3, 2871.8, 1751.2, 1627.8, 1396.4, 1263.3, 1145.6, 781.1
MS (m/z): 767 (M+l)0 MS (m/z): 767 (M+l) 0
ifi-NMR δ/ppm (D20): 1.03 (d, J = 7.2 Hz, 3H, CH3-CH); 1.23 (d, J = 12.3 Hz, 3H, CH3-CH); 1.26 (d, J = 7.5 Hz, 3H, CH3-CH); 1.31 (d, J = 6.3 Hz, 3H, CH3-CH); 1.68 ~ 1.82 (m, 2H, CH-CH2-CH); 2.6 ~ 3.0 (m, 3H, CH-CH-CH); 2.95 (s, 6H, N-CH3); 3.04 (s, 3H, N-CH3); 3.18 (s, 3H, N-CH3); 3.05 - 3.3 (m, 2H, S-CH-CH2); 3.44 (d, 1H, S-CH-CH); 3.48 ~ 3.8 (m, 3H, CH2, CH-CH-CH); 3.9 ~ 4.5 (m, 8H, HO-CH-CH3, CH2); 4.7 ~ 4.85 (m, 1H, CO-CH-N); 5.05 (m, 1H, CO-CH-N)。 Ifi-NMR δ/ppm (D 2 0): 1.03 (d, J = 7.2 Hz, 3H, CH 3 -CH); 1.23 (d, J = 12.3 Hz, 3H, CH 3 -CH); 1.26 (d, J = 7.5 Hz, 3H, CH 3 -CH); 1.31 (d, J = 6.3 Hz, 3H, CH 3 -CH); 1.68 ~ 1.82 (m, 2H, CH-CH 2 -CH); 2.6 ~ 3.0 ( m, 3H, CH-CH-CH); 2.95 (s, 6H, N-CH 3 ); 3.04 (s, 3H, N-CH 3 ); 3.18 (s, 3H, N-CH 3 ); 3.05 - 3.3 (m, 2H, S-CH-CH 2 ); 3.44 (d, 1H, S-CH-CH); 3.48 ~ 3.8 (m, 3H, CH 2 , CH-CH-CH); 3.9 ~ 4.5 (m, 8H, HO-CH-CH 3 , CH2); 4.7 ~ 4.85 (m, 1H, CO-CH-N); 5.05 (m, 1H, CO-CH-N).
13C-NMR δ/ppm (D20): 176.9, 173.9, 173.6, 173.3, 169.4, 168.2, 140.4, 132.3, 115.5, 74.7, 73.7, 69.7, 65.9, 59.2, 58.4, 58.1, 57.7, 56.7, 52.8, 51.6, 50.7, 45.3, 43.4, 40.4, 38.0, 37.9, 37.5, 36.8, 34.8, 34.4, 20.9, 16.9, 15.6, 11.0 结论: 物理性质测定结果与杂质 B结构吻合, 相关谱图见图 6-9 实施例 2 13 C-NMR δ/ppm (D 2 0): 176.9, 173.9, 173.6, 173.3, 169.4, 168.2, 140.4, 132.3, 115.5, 74.7, 73.7, 69.7, 65.9, 59.2, 58.4, 58.1, 57.7, 56.7, 52.8 51.6, 50.7, 45.3, 43.4, 40.4, 38.0, 37.9, 37.5, 36.8, 34.8, 34.4, 20.9, 16.9, 15.6, 11.0 Conclusion: The physical property determination results are in agreement with the impurity B structure, and the correlation spectrum is shown in Figure 6-9. Example 2
将实施例 1得到的美罗培南精制母液 3 21.0kg,加入纳滤设备溶液罐; 控制纳滤设备出口压力 18 X 105Pa开始浓缩, 控制浓缩过程料液温度为 10 °C ~ 25 °C , 耗时 98分钟, 浓缩液从 21.0kg降低到 2.70kg, 得到浓缩废水 18.30kg, 取样浓缩废水检测美罗培南含量, 结果为未检出; 取浓缩液检测 美罗培南含量为 10% 3 21.0 kg of the meropenem refined mother liquor obtained in Example 1 was added to the solution tank of the nanofiltration equipment; the outlet pressure of the nanofiltration equipment was controlled to start concentration at 18 X 10 5 Pa, and the temperature of the liquid in the concentration process was controlled to be 10 ° C to 25 ° C. It took 98 minutes to reduce the concentrate from 21.0kg to 2.70kg, and obtained 18.30kg of concentrated wastewater. The sampled concentrated wastewater was used to detect the meropenem content, and the result was not detected. The concentration of meropenem was 10%.
将 2.70kg浓缩液加入到 152L的已析出粗品的过滤后母液(母液 2 ) 中, 控制温度 10 ~ 15 °C搅拌 30min; 经过滤、 洗晶、 干燥后得到 186g美 罗培南粗品; 取样检测美罗培南粗品杂质、 含量, 其中美罗培南的含量为 97.8%; 有关物质中杂质 A为 0.11%; 杂质 B为 0.38%; 任何未知单个杂 质为 0.12%; 除 A和 B外其它杂质总和为 1.0%  2.70 kg of the concentrate was added to 152 L of the filtered crude mother liquor (mother liquor 2), and the temperature was controlled at 10-15 ° C for 30 min; after filtration, washing and drying, 186 g of crude meropenem was obtained; The crude impurities and content, of which the content of meropenem is 97.8%; the impurity A in the relevant substance is 0.11%; the impurity B is 0.38%; any unknown single impurity is 0.12%; the sum of other impurities except A and B is 1.0%
其中母液 2约含水 16%, THF为 84%; 制备方法参照实施例 13 实施例 3 The mother liquor 2 contains about 16% water and 84% THF. For the preparation method, refer to Example 13. Example 3
将美罗培南粗品 20kg加入到 300kg温度为 20°C的注射用水中, 搅拌 混合均匀, 将混悬物通过换热器瞬间加热到 70°C溶解, 并通过换热器迅速 降到 20 °C , 得溶液 I  Add 20kg of meropenem to 300kg of water for injection at a temperature of 20 °C, stir and mix evenly. The suspension is instantly heated to 70 °C through a heat exchanger and dissolved rapidly to 20 °C through a heat exchanger. Solution I
通过活性炭过滤器在线过滤脱色溶液 I, 得到滤液 II  The decolorization solution I was filtered through an activated carbon filter to obtain a filtrate II.
放出 6.4kg的滤液 II, 设定温度为 5 °C , 加入 25.6L四氢呋喃, 搅拌 20分钟后过滤得到晶种。 降温至 0°C, 将制得的晶种加入剩余的 288kg滤 液 II中, 保持搅拌速度为 120转 /分钟, 养晶 10小时, 过滤, 得到母液 3 , 母液 3进入下一步纳滤浓缩。  6.4 kg of filtrate II was discharged, the temperature was set to 5 ° C, 25.6 L of tetrahydrofuran was added, and after stirring for 20 minutes, it was filtered to obtain a seed crystal. The temperature was lowered to 0 ° C, and the obtained seed crystals were added to the remaining 288 kg of the filtrate II, the stirring speed was maintained at 120 rpm, the crystal was maintained for 10 hours, and filtered to obtain a mother liquid 3 , and the mother liquid 3 was subjected to the next nanofiltration concentration.
滤饼用丙酮淋洗, 滤饼真空 25°C干燥 6小时, 粉碎, 得到美罗培南原 料药 14kg, 收率 70%  The filter cake was rinsed with acetone, and the filter cake was dried at 25 ° C for 6 hours, and pulverized to obtain 14 kg of meropenem raw material, yield 70%.
其中美罗培南的含量为 99.7% (以无水物计); 有关物质中杂质 A为 0.04%; 杂质 B为 0.09%; 任何未知单个杂质为 0.03%; 除 A和 B外其它 杂质总和为 0.05%; 丙酮残留为 20ppm  The content of meropenem is 99.7% (based on anhydrous matter); the impurity A in the relevant substance is 0.04%; the impurity B is 0.09%; any unknown single impurity is 0.03%; the sum of other impurities except A and B is 0.05% ; acetone residue is 20ppm
美罗培南原料药物理性质测定结果为:  The physical properties of the meropenem drug substance are as follows:
元素分析: C17H25N305S'3H20 Elemental analysis: C 17 H 25 N 3 0 5 S'3H 2 0
计算值: C, 46.67%; H, 7.14%; N, 9.60%; S, 7.33%;  Calculated: C, 46.67%; H, 7.14%; N, 9.60%; S, 7.33%;
实测值: C, 46.40%; H, 7.38%; N, 9.66%; S, 7.28%  Found: C, 46.40%; H, 7.38%; N, 9.66%; S, 7.28%
UV 2。謹: 296 UV 2 . Dear: 296
IR^^cm"1: 1755, 1627, 1393, 1252, 1130. IR^^cm" 1 : 1755, 1627, 1393, 1252, 1130.
ifi-NMR (D20, δ/ppm): : 1.21(3H, d, J=7.1 Hz), 1.29 ( 3H, d, J=6.3Hz ) 1.97(1H, m), 2.99(3H, s), 3.06(3H, s), 3.09 (1H, m), 3.38(1H, m), 3.46(2H, m), 3.77(1H, dd, J=11.9和 6.2Hz), 4.05(1H, m), 4.23(2H, m),4.82(lH) Ifi-NMR (D 2 0, δ/ppm): : 1.21 (3H, d, J = 7.1 Hz), 1.29 ( 3H, d, J = 6.3 Hz ) 1.97 (1H, m), 2.99 (3H, s) , 3.06(3H, s), 3.09 (1H, m), 3.38(1H, m), 3.46(2H, m), 3.77(1H, dd, J=11.9 and 6.2Hz), 4.05(1H, m), 4.23(2H, m), 4.82 (lH)
杂质 A B按照实施例 1所述方法分析、 测定, 结果符合。 实施例 4  The impurity A B was analyzed and measured in accordance with the method described in Example 1, and the results were in agreement. Example 4
将实施例 3得到的美罗培南精制母液 3 340kg, 加入纳滤设备溶液罐; 控制纳滤设备出口压强 20 X 105Pa开始浓缩, 控制浓缩过程料液温度为 5 °C ~ 35.0°C , 浓缩液从 340kg降低到 42kg, 得到浓缩废水 298kg, 取样浓 缩废水检测美罗培南含量, 结果为未检出; 取浓缩液检测美罗培南含量为 9% 3 340 kg of the meropenem refined mother liquor obtained in Example 3 was added to the nanofiltration equipment solution tank; the outlet pressure of the nanofiltration equipment was controlled to start concentration at 20 X 10 5 Pa, and the temperature of the concentrated liquid was controlled to be 5 ° C ~ 35.0 ° C, concentrated. The liquid was reduced from 340kg to 42kg, and 298kg of concentrated wastewater was obtained. The sampled concentrated wastewater was used to detect the meropenem content, and the result was not detected. The concentration of meropenem was 9%.
将 42kg浓缩液加入到 398L已析出粗品的过滤后母液(母液 2 ) 中, 控制温度 5 °C搅拌 60min; 通过过滤器过滤、 洗晶、 干燥后得到 3.06kg美 罗培南粗品; 取样检测美罗培南粗品杂质、 含量, 其中美罗培南的含量为 98.0%; 有关物质中杂质 A为 0.20%; 杂质 B为 0.18%; 任何未知单个杂 质为 0.13%; 除 A和 B外其它杂质总和为 1.0% 42 kg of the concentrate was added to 398 L of the filtered mother liquor (mother liquor 2) from which the crude product had been precipitated. The temperature was controlled at 5 °C for 60 min; filtered, washed and dried to obtain 3.06 kg of crude meropenem; the impurities and content of meropenem were sampled and tested, wherein the content of meropenem was 98.0%; the impurity A in the related substance was 0.20. %; impurity B is 0.18%; any unknown single impurity is 0.13%; the sum of other impurities except A and B is 1.0%
其中母液 2约含水 14%, THF+丙酮为 86%; 制备方法参照实施例 13 实施例 5  The mother liquor 2 contains about 14% water and THF+ acetone is 86%; Preparation method refers to Example 13 Example 5
将实施例 4得到的美罗培南粗品 1kg加入到 17kg温度为 5 °C的注射用 水中, 搅拌混合均勾, 将混悬物通过换热器瞬间加热到 60°C溶解, 并通过 换热器迅速降到 10°C , 得溶液 I  1 kg of the crude meropenem obtained in Example 4 was added to 17 kg of water for injection at a temperature of 5 ° C, stirred and mixed, and the suspension was instantaneously heated to 60 ° C by a heat exchanger to dissolve, and quickly passed through a heat exchanger. Drop to 10 ° C, get solution I
通过活性炭过滤器在线过滤脱色溶液 I, 得到滤液 II  The decolorization solution I was filtered through an activated carbon filter to obtain a filtrate II.
放出 1.8kg的滤液 II, 设定温度为 20°C , 加入 10.8L丙酮, 搅拌 15 分钟后过滤得到晶种。 降温至 5 °C , 将制得的晶种加入剩余的 16.2kg滤液 II中, 保持搅拌速度为 110转 /分钟, 养晶 5小时, 过滤, 得到母液 3 , 母 液 3进入下一步纳滤浓缩。  1.8 kg of the filtrate II was discharged, the temperature was set to 20 ° C, 10.8 L of acetone was added, and the mixture was stirred for 15 minutes, and then filtered to obtain a seed crystal. The temperature was lowered to 5 ° C, and the obtained seed crystals were added to the remaining 16.2 kg of the filtrate II, the stirring speed was maintained at 110 rpm, the crystals were maintained for 5 hours, and filtered to obtain a mother liquor 3, and the mother liquor 3 was subjected to the next nanofiltration concentration.
滤饼用丙酮淋洗, 滤饼真空 20°C干燥 10小时, 粉碎, 得到美罗培南 原料药 690g, 收率 69%  The filter cake was rinsed with acetone, and the filter cake was dried at 20 ° C for 10 hours, and pulverized to obtain merapene 6.2 g, a yield of 69%.
其中美罗培南的含量为 99.8% (以无水物计); 有关物质中杂质 A为 0.05%; 杂质 B为 0.07%; 任何未知单个杂质为 0.03%; 除 A和 B外其它 杂质总和为 0.08%; 丙酮残留未检出。  The content of meropenem is 99.8% (calculated as anhydrate); the impurity A in the relevant substance is 0.05%; the impurity B is 0.07%; any unknown single impurity is 0.03%; the sum of other impurities except A and B is 0.08% ; Acetone residue was not detected.
美罗培南原料药物理性质测定结果为:  The physical properties of the meropenem drug substance are as follows:
元素分析: C17H25N305S'3H20 Elemental analysis: C 17 H 25 N 3 0 5 S'3H 2 0
计算值: C, 46.67%; H, 7.14%; N, 9.60%; S, 7.33%;  Calculated: C, 46.67%; H, 7.14%; N, 9.60%; S, 7.33%;
实测值: C, 46.43%; H, 7.32%; N, 9.56%; S, 7.38%  Found: C, 46.43%; H, 7.32%; N, 9.56%; S, 7.38%
UV 2。謹: 296 UV 2 . Dear: 296
IR^^cm"1: 1755, 1627, 1393, 1252, 1130. IR^^cm" 1 : 1755, 1627, 1393, 1252, 1130.
ifi-NMR (D20, δ/ppm): : 1.21(3H, d, J=7.1 Hz), 1.29 ( 3H, d, J=6.3Hz ) 1.97(1H, m), 2.99(3H, s), 3.06(3H, s), 3.09 (1H, m), 3.38(1H, m), 3.46(2H, m), 3.77(1H, dd, J=11.9和 6.2Hz), 4.05(1H, m), 4.23(2H, m),4.82(lH) Ifi-NMR (D 2 0, δ/ppm): : 1.21 (3H, d, J = 7.1 Hz), 1.29 ( 3H, d, J = 6.3 Hz ) 1.97 (1H, m), 2.99 (3H, s) , 3.06(3H, s), 3.09 (1H, m), 3.38(1H, m), 3.46(2H, m), 3.77(1H, dd, J=11.9 and 6.2Hz), 4.05(1H, m), 4.23(2H, m), 4.82 (lH)
杂质 A B依照实施例 1所述方法分析、 测定, 结果符合。 实施例 6  The impurity A B was analyzed and measured in accordance with the method described in Example 1, and the results were in agreement. Example 6
将实施例 5得到的美罗培南精制母液 3 18.8kg,加入纳滤设备溶液罐, 控制纳滤设备出口压力 5 X 105Pa开始浓缩, 控制浓缩过程料液温度为 10 °C ~ 30°C , 浓缩液从 18.8kg降低到 3.76kg, 得到浓缩废水 15kg, 取样浓 缩废水检测美罗培南含量, 结果为未检出; 取浓缩液检测美罗培南含量为 5% The 18.5 kg of the meropenem refined mother liquor obtained in Example 5 was added to the nanofiltration equipment solution tank. Control the outlet pressure of the nanofiltration equipment 5 X 10 5 Pa to start concentration, control the concentration of the liquid in the concentration process to 10 °C ~ 30 °C, reduce the concentrate from 18.8kg to 3.76kg, obtain 15kg of concentrated wastewater, and sample the concentrated wastewater to detect meropenem The content was not detected; the concentration of meropenem was 5%.
将 3.76kg浓缩液加入到 30L的已析出粗品的过滤后母液(母液 2 )中, 控制温度 5 ~ 10°C搅拌 30min; 经过滤、 洗晶、 干燥后得到 148.6g美罗培 南粗品; 取样检测美罗培南粗品杂质、 含量, 结果合格。  3.76kg of concentrated liquid was added to 30L of the filtered crude mother liquor (mother liquor 2), and the temperature was controlled at 5 ~ 10 °C for 30min; after filtration, washing and drying, 148.6g of crude meropenem was obtained; The crude impurities and content of Luo Peinan were qualified.
其中母液 2约含水 15%, THF+曱基乙基酮为 85%; 制备方法参照实 施例 13 实施例 7  The mother liquor 2 contains about 15% water and THF + mercaptoethyl ketone is 85%; Preparation method refers to Example 13 Example 7
将美罗培南粗品 30kg加入到 600kg温度为 10°C的注射用水中, 搅拌 混合均匀, 将混悬物通过换热器瞬间加热到 65 °C溶解, 并通过换热器迅速 降到 15 °C , 得溶液 I  Add 30kg of meropenem to 600kg of water for injection at a temperature of 10 °C, stir and mix evenly. The suspension is heated to 65 °C through a heat exchanger and dissolved rapidly to 15 °C through a heat exchanger. Solution I
通过活性炭过滤器在线过滤脱色溶液 I, 得到滤液 II  The decolorization solution I was filtered through an activated carbon filter to obtain a filtrate II.
放出 9.5kg的滤液 II, 设定温度为 5 °C , 加入 28.5L四氢呋喃, 搅拌 20分钟后过滤得到晶种。 降温至 0°C , 将制得的晶种加入剩余的 620.5kg 滤液 I中,保持搅拌速度为 120转 /分钟,养晶 10小时,过滤,得到母液 3 , 母液 3进入下一步纳滤浓缩。  9.5 kg of the filtrate II was discharged, the temperature was set to 5 ° C, 28.5 L of tetrahydrofuran was added, and the mixture was stirred for 20 minutes, and then filtered to obtain a seed crystal. The temperature was lowered to 0 ° C, and the prepared seed crystals were added to the remaining 620.5 kg of filtrate I, maintained at a stirring speed of 120 rpm, crystallized for 10 hours, filtered to obtain a mother liquor 3, and the mother liquor 3 was subjected to a next nanofiltration concentration.
滤饼用丙酮淋洗, 滤饼真空 25°C干燥 6小时, 粉碎, 得到美罗培南原 料药 21kg, 收率 70%  The filter cake was rinsed with acetone, and the filter cake was dried at 25 ° C for 6 hours, and pulverized to obtain 21 kg of meropenem raw material, yield 70%.
其中美罗培南的含量为 99.7% (以无水物计); 有关物质中杂质 A为 0.05%; 杂质 B为 0.06%; 任何未知单个杂质为 0.02%; 除 A和 B外其它 杂质总和为 0.06%; 丙酮残留为 60ppm  The content of meropenem is 99.7% (calculated as anhydrous matter); the impurity A in the relevant substance is 0.05%; the impurity B is 0.06%; any unknown single impurity is 0.02%; the sum of other impurities except A and B is 0.06% ; acetone residue is 60ppm
美罗培南原料药物理性质测定结果为:  The physical properties of the meropenem drug substance are as follows:
元素分析: C17H25N305S'3H20 Elemental analysis: C 17 H 25 N 3 0 5 S'3H 2 0
计算值: C, 46.67%; H, 7.14%; N, 9.60%; S, 7.33%;  Calculated: C, 46.67%; H, 7.14%; N, 9.60%; S, 7.33%;
实测值: C, 46.45%; H, 7.22%; N, 9.54%; S, 7.39%  Found: C, 46.45%; H, 7.22%; N, 9.54%; S, 7.39%
UV 2。謹: 296 UV 2 . Dear: 296
IR^^cm"1: 1755, 1627, 1393, 1252, 1130. IR^^cm" 1 : 1755, 1627, 1393, 1252, 1130.
ifi-NMR (D20, δ/ppm): : 1.21(3H, d, J=7.1 Hz), 1.29 ( 3H, d, J=6.3Hz ) 1.97(1H, m), 2.99(3H, s), 3.06(3H, s), 3.09 (1H, m), 3.38(1H, m), 3.46(2H, m), 3.77(1H, dd, J=11.9和 6.2Hz), 4.05(1H, m), 4.23(2H, m),4.82(lH)。 杂质 A、 B依照实施例 1所述方法分析、 测定, 结果符合。 实施例 8 Ifi-NMR (D 2 0, δ/ppm): : 1.21 (3H, d, J = 7.1 Hz), 1.29 ( 3H, d, J = 6.3 Hz ) 1.97 (1H, m), 2.99 (3H, s) , 3.06(3H, s), 3.09 (1H, m), 3.38(1H, m), 3.46(2H, m), 3.77(1H, dd, J=11.9 and 6.2Hz), 4.05(1H, m), 4.23 (2H, m), 4.82 (lH). The impurities A and B were analyzed and measured in accordance with the method described in Example 1, and the results were in agreement. Example 8
将实施例 7得到的美罗培南精制母液 3 600kg, 加入纳滤设备溶液罐, 控制纳滤设备出口压力 20 X 105Pa开始浓缩, 控制浓缩过程料液温度为 10 °C ~ 25 °C , 浓缩到 51kg, 得到浓缩废水 542L, 取样浓缩废水检测美罗培 南含量, 结果为未检出; 取浓缩液检测美罗培南含量为 15%。 3 600 kg of the meropenem refined mother liquor obtained in Example 7 was added to the nanofiltration equipment solution tank, and the outlet pressure of the nanofiltration equipment was controlled to start concentration at 20 X 10 5 Pa, and the temperature of the concentrated liquid was controlled to be 10 ° C ~ 25 ° C, concentrated. At 51 kg, 542 L of concentrated wastewater was obtained, and the content of meropenem was detected by sampling and concentrating wastewater, and the result was not detected; the concentration of meropenem was 15%.
将 51kg浓缩液加入到装有 1700L未析出粗品的过滤后母液(母液 1 ) 的粗品结晶罐中, 一同执行粗品生产, 加入 2120L四氢呋喃结晶, 控制温 度 5 ~ 10°C搅拌 30min;经过滤、洗晶、干燥后得到 24.05kg美罗培南粗品; 取样检测美罗培南粗品杂质、 含量, 其中美罗培南的含量为 98.4%; 有关 物质中杂质 A为 0.24%; 杂质 B为 0.14%; 任何未知单个杂质为 0.10%; 除 A和 B外其它杂质总和为 0.58%。  51 kg of the concentrate was added to a crude crystallizing tank containing 1700 L of the filtered mother liquor (mother liquor 1) which was not precipitated, and the crude product was continuously produced. 2120 L of tetrahydrofuran crystals were added, and the temperature was controlled at 5 to 10 ° C for 30 min; filtered and washed. After crystal and drying, 24.05kg of meropenem crude product was obtained; the impurities and content of meropenem crude were sampled and tested, wherein the content of meropenem was 98.4%; the impurity A in the related substance was 0.24%; the impurity B was 0.14%; any unknown single impurity was 0.10. %; The sum of other impurities except A and B is 0.58%.
其中母液 1的制备方法参照实施例 13。 实施例 9  The preparation method of the mother liquid 1 is as described in Example 13. Example 9
将美罗培南粗品 60kg加入到 600kg温度为 20°C的注射用水中, 搅拌 混合均匀, 将混悬物通过换热器瞬间加热到 50°C溶解, 并通过换热器迅速 降到 10°C , 得溶液 I。  60 kg of meropenem crude was added to 600 kg of water for injection at a temperature of 20 ° C, stirred and mixed uniformly, and the suspension was instantaneously heated to 50 ° C through a heat exchanger to dissolve, and rapidly lowered to 10 ° C through a heat exchanger. Solution I was obtained.
通过活性炭过滤器在线过滤脱色溶液 I, 得到滤液 II。  The decolorizing solution I was filtered in-line through an activated carbon filter to obtain a filtrate II.
降温至 5 °C , 加入 3kg晶种, 保持搅拌速度为 110转 /分钟, 养晶 20 小时, 过滤, 得到母液 3 , 母液 3进入下一步纳滤浓缩。  The temperature was lowered to 5 °C, 3 kg of seed crystals were added, the stirring speed was maintained at 110 rpm, the crystals were maintained for 20 hours, and filtered to obtain a mother liquor 3, and the mother liquor 3 was subjected to the next nanofiltration concentration.
滤饼用丙酮淋洗, 滤饼真空 25°C干燥 6小时, 粉碎, 得到美罗培南原 料药 41.4kg, 收率 69%。  The filter cake was rinsed with acetone, and the filter cake was dried at 25 ° C for 6 hours, and pulverized to obtain 41.4 kg of meropenem raw material, yield 69%.
其中美罗培南的含量为 99.5% (以无水物计); 有关物质中杂质 A为 0.07%; 杂质 B为 0.09%; 任何未知单个杂质为 0.02%; 除 A和 B外其它 杂质总和为 0.06%; 丙酮残留为 50ppm。  The content of meropenem is 99.5% (based on anhydrous matter); the impurity A in the relevant substance is 0.07%; the impurity B is 0.09%; any unknown single impurity is 0.02%; the sum of other impurities except A and B is 0.06% The acetone residue is 50 ppm.
美罗培南原料药物理性质测定结果显示与美罗培南结构相符。  The physical properties of the meropenem drug substance showed that it was consistent with the meropenem structure.
杂质 A、 B依照实施例 1所述方法分析、 测定, 结果符合。 实施例 10  The impurities A and B were analyzed and measured in accordance with the method described in Example 1, and the results were in agreement. Example 10
将实施例 9得到的美罗培南精制母液 3 600kg, 加入纳滤设备溶液罐, 控制纳滤设备出口压力 20 X 105Pa开始浓缩, 控制浓缩过程料液温度为 10 °C ~ 25 °C , 浓缩到 40kg, 得到浓缩废水 560L, 取样浓缩废水检测美罗培 南含量, 结果为未检出; 取浓缩液检测美罗培南含量为 20%。 3 600 kg of the meropenem refined mother liquor obtained in Example 9 was added to the nanofiltration equipment solution tank, and the outlet pressure of the nanofiltration equipment was controlled to start concentration at 20 X 10 5 Pa, and the temperature of the liquid in the concentration process was controlled to be 10 °C ~ 25 °C, concentrated to 40kg, 560L of concentrated wastewater was obtained, and the content of meropenem was detected by sampling and concentrating wastewater. The result was not detected; the concentration of meropenem was 20%.
将 40kg浓缩液加入到装有 1700L未析出粗品的过滤后母液(母液 1 ) 的粗品结晶罐中,一同执行粗品生产,加入 3560L丙酮结晶,控制温度 5 ~ 10°C搅拌 30min; 经过滤、 洗晶、 干燥后得到 29.6kg美罗培南粗品; 取样 检测美罗培南粗品杂质、 含量, 其中美罗培南的含量为 98.2%; 有关物质 中杂质 A为 0.28%; 杂质 B为 0.30%; 任何未知单个杂质为 0.11%; 除 A 和 B外其它杂质总和为 0.64%。  Add 40kg of concentrated liquid to the crude crystallizing tank containing 1700L of the filtered mother liquor (mother liquor 1) without precipitation, carry out the crude product production together, add 3560L acetone crystal, control the temperature 5 ~ 10 °C and stir for 30min; After crystallizing and drying, 29.6 kg of crude meropenem was obtained. The impurities and content of meropenem were determined by sampling. The content of meropenem was 98.2%; the impurity A in the related substance was 0.28%; the impurity B was 0.30%; any unknown single impurity was 0.11. %; The sum of other impurities except A and B is 0.64%.
其中母液 1的制备方法参照实施例 13。 实施例 11  The preparation method of the mother liquid 1 is as described in Example 13. Example 11
将实施例 10得到的美罗培南粗品 1kg加入到 13kg温度为 70°C的注射 用水中, 2分钟内搅拌溶解, 并在 4分钟内迅速降到 25 °C。  1 kg of the crude meropenem obtained in Example 10 was added to 13 kg of water for injection at 70 ° C, dissolved by stirring for 2 minutes, and rapidly lowered to 25 ° C in 4 minutes.
加入 10g医用活性炭脱色 5分钟, 过滤, 得到滤液 II。  10 g of medical activated carbon was added for decolorization for 5 minutes, and filtered to obtain a filtrate II.
降温至 2°C , 加入 20g晶种, 保持搅拌速度为 100转 /分钟, 养晶 7小 时, 过滤, 母液进入下一步纳滤浓缩。  Cool down to 2 ° C, add 20 g of seed crystals, keep stirring at 100 rpm, crystallize for 7 hours, filter, and the mother liquor is concentrated in the next nanofiltration.
滤饼用丙酮淋洗, 滤饼真空 25°C干燥 6小时, 粉碎, 得到美罗培南原 料药 670g, 收率 67%。  The filter cake was rinsed with acetone, and the cake was dried under vacuum at 25 ° C for 6 hours, and pulverized to obtain 670 g of meropenem prodrug, and the yield was 67%.
其中美罗培南的含量为 99.4% (以无水物计); 有关物质中杂质 A为 0.08%; 杂质 B为 0.13%; 任何未知单个杂质为 0.03%; 除 A和 B外其它 杂质总和为 0.07%; 丙酮残留为 10ppm。  The content of meropenem is 99.4% (based on anhydrous matter); the impurity A in the relevant substance is 0.08%; the impurity B is 0.13%; any unknown single impurity is 0.03%; the sum of other impurities except A and B is 0.07% The acetone residue is 10 ppm.
美罗培南原料药物理性质测定结果显示与美罗培南结构相符。  The physical properties of the meropenem drug substance showed that it was consistent with the meropenem structure.
杂质 A、 B依照实施例 1所述方法分析、 测定, 结果符合。 实施例 12  The impurities A and B were analyzed and measured in accordance with the method described in Example 1, and the results were in agreement. Example 12
将实施例 11得到的美罗培南精制母液 3 13kg, 加入纳滤设备溶液罐, 控制纳滤设备出口压力 15 x l05Pa; 开始浓缩, 控制浓缩过程料液温度为 10°C ~ 25 °C , 浓缩到 1.85kg, 得到浓缩废水 11.15kg, 取样浓缩废水检测 美罗培南含量, 结果为未检出; 取浓缩液检测美罗培南含量为 7%。 3 13 kg of the meropenem refined mother liquor obtained in Example 11 was added to the nanofiltration equipment solution tank, and the outlet pressure of the nanofiltration equipment was controlled to be 15 x 10 5 Pa; the concentration was started, and the temperature of the concentrated liquid was controlled to be 10 ° C to 25 ° C. Concentrated to 1.85 kg, 11.15 kg of concentrated wastewater was obtained, and the content of meropenem was detected by sampling and concentrating wastewater, and the result was not detected; the concentration of meropenem was 7%.
将 1.85kg浓缩液加入到装有 1700L未析出粗品的过滤后母液(母液 1 ) 的粗品结晶罐中,一同执行粗品生产,加入 2625L曱醇结晶,控制温度 5 ~ 10°C搅拌 30min; 经过滤、 洗晶、 干燥后得到 19.7kg美罗培南粗品; 取样 检测美罗培南粗品杂质、 含量, 结果合格。 其中母液 1由实施例 13制备得到 实施例 13 1.85 kg of the concentrate was added to a crude crystallization tank containing 1700 L of the filtered mother liquor (mother liquor 1) without precipitation, and the crude product was continuously produced, and 2,625 L of sterol crystals were added thereto, and the temperature was controlled at 5 to 10 ° C for 30 minutes; After washing and drying, 19.7 kg of crude meropenem was obtained; the impurities and content of crude meropenem were sampled and tested, and the results were satisfactory. The mother liquor 1 was prepared from Example 13 to obtain Example 13
Figure imgf000024_0001
Figure imgf000024_0001
将保护美罗培南 (Ia )33.0kg (或者保护美罗培南 HLPC含量为 33.0kg 的浓缩液)、 THF 880L、水 700L、 3,5,-二曱基吡啶 14.5kg、 10%钯碳 5.28kg 一并加入到 2000L的高压反应釜中, 除去空气, 通入氢气, 室温反应 6小 时, 反应毕, 过滤洗涤回收钯碳, 得到 1700L未析出粗品的过滤后母液, 其中 THF约 880L, 水约 700L, 其他约 120L; 此母液可作为未析出粗品 的过滤后母液用, 简称母液 1 ; It will protect 33.0kg of meropenem (I a ) (or a concentrate with a merocene HLPC content of 33.0kg), THF 880L, water 700L, 3,5,-dimercaptopyridine 14.5kg, 10% palladium carbon 5.28kg And added to a 2000L high pressure reaction vessel, the air is removed, hydrogen is introduced, and the reaction is carried out for 6 hours at room temperature. After the reaction is completed, the palladium carbon is recovered by filtration and washing to obtain 1700 L of the filtered mother liquid without precipitation of crude product, wherein the THF is about 880 L and the water is about 700 L. Other about 120L; this mother liquor can be used as the filtered mother liquor without precipitation of crude product, referred to as mother liquor 1;
此母液中加入 2625L四氢呋喃, 控制温度 10-15 °C搅拌 30min, 过滤, 洗涤, 产品干燥, 得美罗培南 (化合物 I )粗品 19.5kg, 质量收率 59%; 其中美罗培南的含量为 97.8%; 有关物质中杂质 A为 0.20%; 杂质 B为 0.40%; 任何未知单个杂质为 0.13%; 除 A和 B外其它杂质总和为 1.2%。  The mother liquor was added with 2625 L of tetrahydrofuran, the temperature was controlled at 10-15 ° C for 30 min, filtered, washed, and the product was dried to obtain 19.5 kg of crude meropenem (Compound I), the mass yield was 59%; wherein the content of meropenem was 97.8%; The impurity A in the relevant substance was 0.20%; the impurity B was 0.40%; any unknown single impurity was 0.13%; the sum of the other impurities except A and B was 1.2%.
得到已析出粗品的过滤后母液 4300L, 其中含水约 700L, THF 约 3600L; 即约含水 16%, THF为 84%, 此母液可作为已析出粗品的过滤后 母液用, 简称母液 2。  4300 L of the filtered mother liquor having a precipitated crude product was obtained, wherein the water content was about 700 L and the THF was about 3600 L; that is, about 16% of water and 84% of THF. This mother liquor can be used as a filtered mother liquor which has been precipitated as a crude product, referred to as mother liquor 2 .
其中 2625L四氢呋喃中的四氢呋喃可换成丙酮、异丙醇、 曱醇、 乙醇、 曱基乙基酮的一种或多种; 母液 2 中有机溶剂体积之和与水的体积比为 3: 1 ~ 6: 1即可。  The tetrahydrofuran in 2625L tetrahydrofuran can be replaced by one or more of acetone, isopropanol, decyl alcohol, ethanol, mercaptoethyl ketone; the volume ratio of the volume of the organic solvent in the mother liquor 2 to water is 3: 1 ~ 6: 1 can be.
其中 2625L四氢呋喃中的四氢呋喃可换成丙酮、异丙醇、曱醇、 乙醇、 曱基乙基酮的一种或多种, 也可制备得到质量合格的美罗培南粗品。 实施例 14  Among them, the tetrahydrofuran in 2625L of tetrahydrofuran can be replaced by one or more of acetone, isopropanol, decyl alcohol, ethanol and mercaptoethyl ketone, and the crude meropenem can be prepared. Example 14
将按照实施例 1所述方法制备得到的 500g无菌美罗培南原料药、104g 无菌碳酸钠粉碎, 检测符合无菌及粒度要求, 釆用高效混合机混合均匀, 将包装容器进行无菌处理, 灌装, 按照美国药典 USP32-NF27注射用美罗 培南项下方法检测合格, 包装入库。 实施例 15 The 500 g of sterile meropenem drug substance prepared by the method described in Example 1 and 104 g of sterile sodium carbonate were pulverized, and the test was carried out according to the requirements of sterility and particle size, and the mixture was uniformly mixed with a high-efficiency mixer, and the packaging container was aseptically processed. Filling, according to the United States Pharmacopoeia USP32-NF27 injection with meropenem under the test method qualified, packaged into the warehouse. Example 15
将按照实施例 Ί 所述方法制备得到的 1000g 无菌美罗培南原料药、 222g无菌碳酸钠粉碎,检测符合无菌及粒度要求, 釆用高效混合机混合均 匀, 将包装容器进行无菌处理, 灌装, 按照美国药典 USP32-NF27注射用 美罗培南项下方法检测合格, 包装入库。 实施例 16  1000g of sterile meropenem drug substance prepared by the method described in Example 、, 222g of sterile sodium carbonate pulverized, tested to meet the requirements of sterility and particle size, and uniformly mixed with a high-efficiency mixer, and the packaging container is aseptically processed. Filling, according to the United States Pharmacopoeia USP32-NF27 injection with meropenem under the test method qualified, packaged into the warehouse. Example 16
将按照实施例 9 所述方法制备得到的 2000g 无菌美罗培南原料药、 390g无菌碳酸钠粉碎,检测符合无菌及粒度要求, 釆用高效混合机混合均 匀, 将包装容器进行无菌处理, 灌装, 按照美国药典 USP32-NF27注射用 美罗培南项下方法检测合格, 包装入库。 对比实施例 1  The 2000 g of sterile meropenem drug substance prepared by the method described in Example 9 and 390 g of sterile sodium carbonate were pulverized, and the test was carried out according to the requirements of sterility and particle size, and the mixture was uniformly mixed with a high-efficiency mixer, and the packaging container was aseptically processed. Filling, according to the United States Pharmacopoeia USP32-NF27 injection with meropenem under the test method qualified, packaged into the warehouse. Comparative Example 1
将 5g美罗培南粗品于 30 °C溶于 50ml水中 ,水浴冷却,析出少量晶体, 加入 250ml丙酮, 搅拌一' 时, 过滤得到晶体, 用 90ml丙酮洗涤, 减压 室温干燥二小时得到约 4.7g美罗培南三水合物晶体。  5 g of meropenem was dissolved in 50 ml of water at 30 ° C, cooled in a water bath, a small amount of crystals were precipitated, and 250 ml of acetone was added. When stirred, the crystals were obtained by filtration, washed with 90 ml of acetone, and dried under reduced pressure at room temperature for two hours to obtain about 4.7 g. Robinan trihydrate crystals.
其中美罗培南的含量为 98.4% (以无水物计); 有关物质中杂质 A为 0.19%; 杂质 B为 0.27%; 任何未知单个杂质为 0.10%; 除 A和 B外其它 杂质总和为 0.26%; 丙酮残留为 599ppm。  The content of meropenem is 98.4% (based on anhydrous matter); the impurity A in the relevant substance is 0.19%; the impurity B is 0.27%; any unknown single impurity is 0.10%; the sum of other impurities except A and B is 0.26% The acetone residue was 599 ppm.
按照实施例 14 所述方法制备其美罗培南原料药与碳酸钠的重量比为 The weight ratio of the meropenem drug substance to sodium carbonate prepared according to the method described in Example 14 was
1000:208的药物组合物。 对比实施例 2 1000:208 pharmaceutical composition. Comparative Example 2
将美罗培南粗品 200克溶解于 20L温度 20 °C的水中,形成溶液,将活 性炭 10克加入该溶液中, 并搅拌溶液约一小时。 经过滤除去活性炭后, 用水冲洗过滤液, 形成水溶液, 再由操作压力每平方英寸 120磅及操作温 度 10 °C至 20 °C的逆渗透浓缩装置浓缩该水溶液, 生成 6.7L浓缩体。 浓缩 体冷却到 0 °C至 10 °C , 添加 1克晶种至浓缩体, 稍后添加 20.1L温度 0 °C 至 10 °C的四氢呋喃作为浓缩体的溶剂, 然后经 6小时搅拌, 搅拌至温度为 0 °C至 5 °C , 收集沉淀的晶体, 并由丙酮冲洗以及经 3小时 30 °C的干燥, 得到美罗培南原料药 165g。  200 g of crude meropenem was dissolved in 20 L of water at 20 ° C to form a solution, 10 g of activated charcoal was added to the solution, and the solution was stirred for about one hour. After removing the activated carbon by filtration, the filtrate was washed with water to form an aqueous solution, and the aqueous solution was concentrated by a reverse osmosis concentration apparatus operating at a pressure of 120 psig and an operating temperature of 10 ° C to 20 ° C to obtain 6.7 L of a concentrate. The concentrate is cooled to 0 ° C to 10 ° C, 1 g of seed crystals is added to the concentrate, and 20.1 L of tetrahydrofuran at a temperature of 0 ° C to 10 ° C is added as a solvent for the concentrate, followed by stirring for 6 hours, and stirring. The temperature was from 0 ° C to 5 ° C, and the precipitated crystals were collected, washed with acetone and dried at 30 ° C for 3 hours to obtain 165 g of meropenem.
按照中国药典 2010年版二部检测,其中美罗培南的含量为 98.9% (以 无水物计); 有关物质中主峰前和后的最大杂质分别为 0.13%、 0.23% , 其 他单个杂质 0.08%; 各杂质总和 0.52%, THF有机残留 998ppm。 按照实施例 14 所述方法制备其美罗培南原料药与碳酸钠的重量比为According to the Chinese Pharmacopoeia 2010 edition of the second test, the content of meropenem is 98.9% (in terms of anhydrous matter); the maximum impurities before and after the main peak in the relevant substances are 0.13%, 0.23%, respectively. He has a single impurity of 0.08%; the sum of each impurity is 0.52%, and the organic residue of THF is 998 ppm. The weight ratio of the meropenem drug substance to sodium carbonate prepared according to the method described in Example 14 was
1000:208的药物组合物。 稳定性试验 1000:208 pharmaceutical composition. Stability test
下面通过稳定性考察结果来说明本发明所提供的原料药及制剂的有 益效果。  Next, the beneficial effects of the drug substance and the preparation provided by the present invention will be explained by the results of the stability investigation.
1. 美罗培南原料药加速试验稳定性考察  1. Investigation on the stability of melopenem drug substance accelerated test
包装: 铝桶; 存储条件: 温度 40。C±2。C , 湿度 75% RH±5% RH 美罗培南原料药 1 ~ 6个月加速试验稳定性考察结果见表 1。  Packing: Aluminum drum; Storage conditions: Temperature 40. C±2. C, Humidity 75% RH±5% RH Meropenem drug substance 1 ~ 6 months Accelerated test stability test results are shown in Table 1.
表 1. 美罗培南原料药加速试验稳定性结果  Table 1. Stability results of melopenem drug substance accelerated test
项目 指标 0-月 1-月 2-月 3-月 4-月 5-月 6-月 实施例 1样品有关物质 Item Indicator 0-Month 1-Month 2-Month 3-Month 4-Month 6-Month Example 1 Sample related substances
杂质 A < 0.25% 0.06% 0.12% 0.12% 0.14% 0.14% 0.15% 0.15% 杂质 B < 0.25% 0.11% 0.08% 0.05% 0.06% 0.06% 0.06% 0.04% 任何未知单个杂质: < 0.05% 0.02% 0.03% 0.04% 0.02% 0.03% 0.03% 0.02% 除 A和 B外其它杂质总和: < 0.2% 0.05% 0.05% 0.10% 0.09% 0.08% 0.11% 0.06% 实施例 1样品 与 5号标准  Impurity A < 0.25% 0.06% 0.12% 0.12% 0.14% 0.14% 0.15% 0.15% Impurity B < 0.25% 0.11% 0.08% 0.05% 0.06% 0.06% 0.06% 0.04% Any unknown single impurity: < 0.05% 0.02% 0.03% 0.04% 0.02% 0.03% 0.03% 0.02% Except for the sum of other impurities except A and B: < 0.2% 0.05% 0.05% 0.10% 0.09% 0.08% 0.11% 0.06% Example 1 sample and No. 5 standard
溶液颜色 比色液比较 < Y5 < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 =Υ4 不得更深 Solution color colorimetric liquid comparison < Y5 < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 = Υ4 Not deeper
实施例 3样品有关物质  Example 3 Sample related substances
杂质 A < 0.25% 0.04% 0.13% 0.15% 0.14% 0.14% 0.16% 0.15% 杂质 B < 0.25% 0.09% 0.08% 0.08% 0.06% 0.06% 0.06% 0.04% 任何未知单个杂质: < 0.05% 0.03% 0.03% 0.02% 0.02% 0.03% 0.03% 0.02% 除 A和 B外其它杂质总和: < 0.2% 0.05% 0.05% 0.08% 0.09% 0.08% 0.11% 0.07% 实施例 3样品 与 5号标准  Impurity A < 0.25% 0.04% 0.13% 0.15% 0.14% 0.14% 0.16% 0.15% Impurity B < 0.25% 0.09% 0.08% 0.08% 0.06% 0.06% 0.06% 0.04% Any unknown single impurity: < 0.05% 0.03% 0.03% 0.02% 0.02% 0.03% 0.03% 0.02% Except for the sum of other impurities except A and B: < 0.2% 0.05% 0.05% 0.08% 0.09% 0.08% 0.11% 0.07% Example 3 sample and No. 5 standard
溶液颜色 比色液比较 < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 =Υ4 不得更深 Solution color colorimetric liquid comparison < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 = Υ4 Not deeper
实施例 7样品有关物质  Example 7 Sample related substances
杂质 A < 0.25% 0.05% 0.12% 0.13% 0.11% 0.13% 0.16% 0.15% 杂质 B < 0.25% 0.06% 0.08% 0.08% 0.05% 0.05% 0.06% 0.04% 任何未知单个杂质: < 0.05% 0.02% 0.03% 0.02% 0.01% 0.02% 0.02% 0.02% 除 A和 B外其它杂质总和: < 0.2% 0.06% 0.06% 0.07% 0.07% 0.08% 0.11% 0.06% 实施例 7样品 与 5号标准  Impurity A < 0.25% 0.05% 0.12% 0.13% 0.11% 0.13% 0.16% 0.15% Impurity B < 0.25% 0.06% 0.08% 0.08% 0.05% 0.05% 0.06% 0.04% Any unknown single impurity: < 0.05% 0.02% 0.03% 0.02% 0.01% 0.02% 0.02% 0.02% The sum of other impurities except A and B: < 0.2% 0.06% 0.06% 0.07% 0.07% 0.08% 0.11% 0.06% Example 7 sample and No. 5 standard
溶液颜色 比色液比较 < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 Υ4-Υ5 不得更深 Solution color colorimetric liquid comparison < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 < Υ5 Υ4-Υ5 Not deeper
对比实施例 1有关物质 USP32-NF2 Comparative Example 1 Related Substances USP32-NF2
杂质 A 7 0.19%  Impurity A 7 0.19%
0.19% 0.20% 0.21% 0.21% 0.21% 0.23% 杂质 B < 0.3% 0.27%  0.19% 0.20% 0.21% 0.21% 0.21% 0.23% Impurity B < 0.3% 0.27%
0.27% 0.28% 0.29% 0.29% 0.30% 0.32% 任何未知单个杂质: < 0.3% 0.10%  0.27% 0.28% 0.29% 0.29% 0.30% 0.32% Any unknown single impurity: < 0.3% 0.10%
0.12% 0.12% 0.14% 0.15% 0.14% 0.15% 除 A和 B外其它杂质总和: < 0.1% 0.26%  0.12% 0.12% 0.14% 0.15% 0.14% 0.15% The sum of other impurities except A and B: < 0.1% 0.26%
0.27% 0.26% 0.28% 0.29% 0.31% 0.33% 0.27% 0.26% 0.28% 0.29% 0.31% 0.33%
< 0.3% 对比实施例 1样品 与 5号标准 < 0.3% Comparative Example 1 sample and No. 5 standard
溶液颜色 比色液比较 Y2-Y3 Y4-Y5 Y4-Y5 Y4-Y5 = Y5 = Y5 >Y5 不得更深 Solution color Comparison of colorimetric liquid Y2-Y3 Y4-Y5 Y4-Y5 Y4-Y5 = Y5 = Y5 >Y5 Must not be deeper
对比实施例 2有关物质 (中国药典 Comparative Example 2 related substances (Chinese Pharmacopoeia)
主峰前最大杂质 2010版) The largest impurity before the main peak 2010 edition)
0.13% 0.15% 0.16% 0.16% 0.17% 0.18% 0.18% 主峰后最大杂质 <0.3%  0.13% 0.15% 0.16% 0.16% 0.17% 0.18% 0.18% Maximum impurity after main peak <0.3%
0.23% 0.23% 0.24% 0.26% 0.27% 0.28% 0.31% 其他单个杂质 <0.3%  0.23% 0.23% 0.24% 0.26% 0.27% 0.28% 0.31% Other single impurities <0.3%
0.08% 0.12% 0.15% 0.13% 0.15% 0.14% 0.16% 各杂质总和 <0.1%  0.08% 0.12% 0.15% 0.13% 0.15% 0.14% 0.16% The sum of each impurity <0.1%
0.52% 0.55% 0.61% 0.64% 0.68% 0.71% 0.80% 0.52% 0.55% 0.61% 0.64% 0.68% 0.71% 0.80%
<1.0% <1.0%
对比实施例 2样品 与 5号标准 Comparative Example 2 Sample and Standard 5
溶液颜色 比色液比较 = Y3 = Y5 Y4-Y5 Y4-Y5 = Y5 = Y5 >Υ5 不得更深 Solution color colorimetric liquid comparison = Y3 = Y5 Y4-Y5 Y4-Y5 = Y5 = Y5 >Υ5 Not deeper
由结果可知, 对比实施例 1、 2 中杂质含量高, 丙酮或四氢呋喃有机 残留高的美罗培南原料药在温度 40。C±2。C、 湿度 75% RH±5% RH加速试 验条件下放置 6个月, 有关物质、 溶液颜色均不符合要求, 稳定性试验不 合格, 无法保证长期存放后的用药安全; 而本发明提供的原料药, 以上市 包装在加速试验条件下杂质、 溶液颜色仍然符合规定, 稳定性很好, 能够 保证产品有效、 安全, 所以作为原料药制备注射剂用于静脉给药安全性更 高, 疗效更好。  From the results, it was found that the meropenem drug substance having a high impurity content in Comparative Examples 1 and 2 and having a high organic residue of acetone or tetrahydrofuran was at a temperature of 40. C±2. C, humidity 75% RH ± 5% RH accelerated test conditions for 6 months, the relevant substances, the color of the solution does not meet the requirements, the stability test is unqualified, can not guarantee the safety of medication after long-term storage; and the raw materials provided by the present invention The medicine, in the packaged packaging under the accelerated test conditions, the impurities and the color of the solution still meet the requirements, the stability is very good, and the product can be ensured to be effective and safe. Therefore, the preparation of the injection as a raw material medicine for intravenous administration has higher safety and better curative effect.
本发明提供的美罗培南原料药的其他检测项, 如比旋度、 酸度、 澄清 度、 细菌内毒素、 无菌、 水分、 可见异物、 不溶性微粒、 有机残留、 炽灼 残渣、 重金属、 结晶水、 无水含量等加速试验稳定性结果也符合要求。  Other detection items of the meropenem drug substance provided by the present invention, such as specific rotation, acidity, clarity, bacterial endotoxin, sterility, moisture, visible foreign matter, insoluble particles, organic residues, pyrophoric residues, heavy metals, crystal water, Accelerated test stability results such as anhydrous content also meet the requirements.
本发明其他实施例提供的美罗培南原料药上述各项指标加速试验稳 定性结果也同样符合要求。  The results of the accelerated test stability of the above-mentioned various indicators of the meropenem drug substance provided by other embodiments of the present invention also meet the requirements.
2. 美罗培南原料药长期试验稳定性考察  2. Stability study of long-term test of meropenem drug substance
包装: 铝桶; 存储条件: 温度 25。C±2。C , 湿度 60% RH±5% RH 美罗培南原料药 1 ~ 24个月长期试验稳定性考察结果见表 2。  Packing: Aluminum drum; Storage conditions: Temperature 25. C±2. C, Humidity 60% RH±5% RH Meropenem drug substance 1 ~ 24 months long-term test stability test results are shown in Table 2.
表 2. 美罗培南原料药长期试验稳定性结果  Table 2. Stability results of long-term trials of meropenem drug substance
项目 指标 0-月 3-月 6-月 9-月 12-月 18-月 24-月 实施例 1样品有关物质  Item Indicator 0-Month 3-Month 6-Month 9-Month 12-Month 18-Month 24-Month Example 1 Sample related substances
杂质 A < 0.25% 0.06% 0.08% 0.12% 0.13% 0.14% 0.14% 0.15% 杂质 B < 0.25% 0.11% 0.06% 0.07% 0.06% 0.06% 0.07% 0.08% 任何未知单个杂质: < 0.05% 0.02% 0.03% 0.02% 0.02% 0.03% 0.03% 0.04% 除 A和 B外其它杂质总和: < 0.2% 0.05% 0.07% 0.08% 0.08% 0.08% 0.10% 0.11% 实施例 3样品有关物质  Impurity A < 0.25% 0.06% 0.08% 0.12% 0.13% 0.14% 0.14% 0.15% Impurity B < 0.25% 0.11% 0.06% 0.07% 0.06% 0.06% 0.07% 0.08% Any unknown single impurity: < 0.05% 0.02% 0.03% 0.02% 0.02% 0.03% 0.03% 0.04% The sum of other impurities except A and B: < 0.2% 0.05% 0.07% 0.08% 0.08% 0.08% 0.10% 0.11% Example 3 Sample related substances
杂质 A < 0.25% 0.04% 0.08% 0.11% 0.12% 0.13% 0.14% 0.15% 杂质 B < 0.25% 0.09% 0.08% 0.08% 0.06% 0.06% 0.08% 0.09% 任何未知单个杂质: < 0.05% 0.03% 0.03% 0.02% 0.02% 0.03% 0.03% 0.02% 除 A和 B外其它杂质总和: < 0.2% 0.05% 0.07% 0.07% 0.09% 0.08% 0.11% 0.07% 实施例 7样品有关物质  Impurity A < 0.25% 0.04% 0.08% 0.11% 0.12% 0.13% 0.14% 0.15% Impurity B < 0.25% 0.09% 0.08% 0.08% 0.06% 0.06% 0.08% 0.09% Any unknown single impurity: < 0.05% 0.03% 0.03% 0.02% 0.02% 0.03% 0.03% 0.02% The sum of other impurities except A and B: < 0.2% 0.05% 0.07% 0.07% 0.09% 0.08% 0.11% 0.07% Example 7 sample related substances
杂质 A < 0.25% 0.05% 0.09% 0.11% 0.11% 0.12% 0.14% 0.14% 杂质 B < 0.25% 0.06% 0.08% 0.08% 0.05% 0.05% 0.06% 0.04% 任何未知单个杂质: < 0.05% 0.02% 0.03% 0.02% 0.01% 0.02% 0.02% 0.03% 除 A和 B外其它杂质总和: < 0.2% 0.06% 0.09% 0.07% 0.07% 0.08% 0.09% 0.06% 由结果可知, 以上市包装在温度 25。C±2。C、 湿度 60% RH±5% RH长 期试验条件下放置 24个月, 杂质仍然符合规定, 稳定性很好,所以作为原 料药制备注射剂用于静脉给药安全性更高, 疗效更好。 Impurity A < 0.25% 0.05% 0.09% 0.11% 0.11% 0.12% 0.14% 0.14% Impurity B < 0.25% 0.06% 0.08% 0.08% 0.05% 0.05% 0.06% 0.04% Any unknown single impurity: < 0.05% 0.02% 0.03% 0.02% 0.01% 0.02% 0.02% 0.03% Sum of other impurities except A and B: < 0.2% 0.06% 0.09% 0.07% 0.07% 0.08% 0.09% 0.06% It can be seen that the package is packaged at a temperature of 25. C±2. C. Humidity 60% RH±5% RH is placed under long-term test conditions for 24 months. The impurities are still in compliance with the regulations and the stability is very good. Therefore, the preparation of injection as a raw material medicine is safer and more effective for intravenous administration.
本发明提供的美罗培南原料药的其他检测项, 如比旋度、 酸度、 澄清 度、 颜色、 细菌内毒素、 无菌、 水分、 可见异物、 不溶性微粒、 有机残留、 炽灼残渣、重金属、 结晶水、无水含量等长期试验稳定性结果也符合要求。  Other detection items of the meropenem drug substance provided by the present invention, such as specific rotation, acidity, clarity, color, bacterial endotoxin, sterility, moisture, visible foreign matter, insoluble particles, organic residue, ignition residue, heavy metal, crystallization Long-term test stability results such as water and anhydrous content also meet the requirements.
本发明其他实施例提供的美罗培南原料药上述各项指标长期试验稳 定性结果也同样符合要求。  The long-term test stability results of the above-mentioned various indicators of the meropenem drug substance provided by other embodiments of the present invention also meet the requirements.
3. 注射用美罗培南药物组合物长期试验稳定性考察  3. Long-term stability study of meropenem pharmaceutical composition for injection
存储条件: 温度 25。C±2。C, 湿度 60% RH士 5% RH  Storage conditions: Temperature 25. C±2. C, humidity 60% RH 5% RH
注射用美罗培南药物组合物 1 ~ 36个月长期试验稳定性考察结果见表 表 3. 注射用美罗培南药物组合物长期试验稳定性结果  The results of the long-term stability study of the meropenem pharmaceutical composition for injection for 1 to 36 months are shown in Table 3. The long-term stability of the pharmaceutical composition for injection of meropenem
Figure imgf000028_0001
Figure imgf000028_0001
由结果可知, 对比实施例 1、 2 中杂质含量高, 丙酮或四氢呋喃有机 残留高的美罗培南原料药制备的组合物在温度 25。C±2。C、 湿度 60% RH±5% RH长期试验条件下放置 24个月及 36个月,溶液颜色不符合要求, 稳定性试验不合格, 无法保证长期存放后的用药安全; 而本发明提供的注 射用美罗培南药物组合物在长期试验条件下溶液颜色仍然符合规定, 稳定 性很好, 作为注射剂用于静脉给药安全性更高, 疗效更好。  From the results, it was found that the compositions prepared in the comparative examples 1 and 2 having a high impurity content and having a high residual organic residue of acetone or tetrahydrofuran were at a temperature of 25. C±2. C, humidity 60% RH ± 5% RH placed under long-term test conditions for 24 months and 36 months, the color of the solution does not meet the requirements, the stability test is unqualified, can not guarantee the safety of medication after long-term storage; and the injection provided by the present invention The long-term test conditions of the meropenem pharmaceutical composition are still in compliance with the regulations, and the stability is very good. The use as an injection for intravenous administration is safer and more effective.
本发明提供的注射用美罗培南药物组合物的其他检测项, 如性状、 鉴 别、 碱度、 澄清度、 有关物质、 干燥失重、 含量均匀度、 细菌内毒素、 无 菌、可见异物、 不溶性微粒、含量测定等长期试验稳定性结果也符合要求, 所以能够保证产品有效、 安全。  Other detection items of the meropenem pharmaceutical composition for injection provided by the present invention, such as traits, identification, alkalinity, clarity, related substances, loss on drying, content uniformity, bacterial endotoxin, sterility, visible foreign matter, insoluble particles, Long-term test stability results such as content determination also meet the requirements, so the product can be guaranteed to be effective and safe.

Claims

权 利 要 求 Rights request
1. 一种美罗培南原料药, 其特征在于, 以重量百分比计, 所述原料药 中美罗培南的含量为 98.5%~ 101.0%, 以无水物计算; 所述原料药的有关 物质中杂质 A、 杂质 B均不大于 0.25%; 任何未知单个杂质不大于 0.05%; 除 A和 B外其它杂质总和不大于 0.2%; 丙酮残留不大于 400ppm, 优选不 大于 lOOppm; A meropenem drug substance, characterized in that, in weight percentage, the content of meropenem in the drug substance is 98.5% to 101.0%, calculated as an anhydrate; the impurity A in the related substance of the drug substance , impurity B is not more than 0.25%; any unknown single impurity is not more than 0.05%; the sum of other impurities except A and B is not more than 0.2%; acetone residue is not more than 400ppm, preferably not more than lOOppm;
其中所述杂质 A为:  Wherein the impurity A is:
Figure imgf000029_0001
所述杂质 B为
Figure imgf000029_0001
The impurity B is
Figure imgf000029_0002
Figure imgf000029_0002
2.—种美罗培南原料药的制备方法, 所述制备方法包括: 将美罗培南 粗品经精制、 过滤得到母液 3及美罗培南原料药, 母液 3经过纳滤膜浓缩 后, 将所得浓缩液加入到后续粗品制备中氢化、 过滤后已析出粗品的母液2. A method for preparing a meropenem bulk drug, the preparation method comprising: purifying and filtering a crude meropenem to obtain a mother liquor 3 and a meropenem drug substance, and the mother liquor 3 is concentrated through a nanofiltration membrane, and the obtained concentrate is added to The crude mother liquor is precipitated after hydrogenation in the subsequent crude preparation and filtration.
(母液 2)或未析出粗品的母液(母液 1 ) 中, 结晶得到美罗培南粗品。 In the mother liquor (mother liquor 2) or the mother liquor (mother liquor 1) in which no crude product was precipitated, the crude product of meropenem was obtained by crystallization.
3. 根据权利要求 2所述的制备方法, 其特征在于, 在 5x l05Pa~20 X 105Pa、 ύ选 15χ 105Pa~20 x 105 Pa的压力和 5~35°C、 优选 10~25°C 的温度下进行母液 3的纳滤浓缩。 3. The production method according to claim 2, characterized in 5x l0 5 Pa ~ 20 X 10 5 Pa, ύ selected pressure 15χ 10 5 Pa ~ 20 x 10 5 Pa and 5 ~ 35 ° C, preferably The nanofiltration of mother liquor 3 was concentrated at a temperature of 10 to 25 °C.
4. 根据权利要求 2或 3 所述的制备方法, 其特征在于, 所述母液 3 与所得浓缩液的重量比为 5:1 ~ 15:1, 优选 7:1 ~ 10:1; 所得浓缩液中美罗 培南的含量为 5 ~ 20%, 优选 7 ~ 15%。  The preparation method according to claim 2 or 3, wherein the weight ratio of the mother liquid 3 to the obtained concentrate is 5:1 to 15:1, preferably 7:1 to 10:1; The content of Sino-American ropamine is 5-20%, preferably 7-15%.
5. 根据权利要求 2所述的制备方法, 其特征在于, 所述结晶得到美罗 培南粗品的体系中有机溶剂的总体积与水的体积比为 3:1 ~ 6:1; 有机溶剂 选自丙酮、 四氢呋喃、 异丙醇、 曱醇、 乙醇和曱基乙基酮中的一种或多种。 The preparation method according to claim 2, wherein the total volume of the organic solvent in the system for obtaining the crude meropenem is 3:1 to 6:1; the organic solvent is selected from the group consisting of acetone One or more of tetrahydrofuran, isopropanol, decyl alcohol, ethanol, and mercaptoethyl ketone.
6. 根据权利要求 2所述的方法, 所述制备方法包括以下步骤: 6. The method of claim 2, the method of preparation comprising the steps of:
1 )使美罗培南粗品溶解在温度为 50°C ~ 80°C的水中, 再将所得溶液 的温度降至 10°C ~ 30°C得溶液 I;  1) Dissolving the crude meropenem in water at a temperature of 50 ° C ~ 80 ° C, and then reducing the temperature of the resulting solution to 10 ° C ~ 30 ° C to obtain a solution I;
2 )将经步骤 1 )得到的溶液 I经活性炭脱色后过滤, 以得到滤液 II; 以及  2) The solution I obtained in the step 1) is decolorized by activated carbon and filtered to obtain a filtrate II;
3 )将经步骤 2 )得到的滤液 II的温度降至 0°C ~ 20°C以结晶, 过滤后 得到母液 3和滤饼, 所述滤饼经洗晶、 干燥后得到美罗培南原料药; 以及 3) The temperature of the filtrate II obtained in the step 2) is lowered to 0 ° C ~ 20 ° C to crystallize, and after filtration, the mother liquid 3 and the filter cake are obtained, and the filter cake is washed and dried to obtain a meropenem raw material drug; as well as
4 )将经步骤 3 )得到的母液 3通过纳滤浓缩后, 加入到下一批粗品制 备中氢化、 过滤后已析出粗品的母液(母液 2 ) 或未析出粗品的母液(母 液 1 ) 中, 结晶得到美罗培南粗品。 4) The mother liquor 3 obtained in the step 3) is concentrated by nanofiltration, and then added to the mother liquor (mother liquor 2) which has been subjected to hydrogenation in the next batch of crude product preparation, and which has been precipitated after filtration, or the mother liquor (mother liquor 1) in which the crude product is not precipitated. Crystallization gives crude meropenem.
7. 根据权利要求 6所述的方法, 其特征在于, 步骤 1 ) 中以重量百分 比计, 美罗培南粗品中 C17H25N305S的含量不少于 92%, 按无水物计算; 杂质 A、 杂质 B均不大于 0.8%; 任何未知单个杂质不大于 0.3%; 除 A和 B外其它杂质总和不大于 3.0%; The method according to claim 6, wherein in step 1), the content of C 17 H 25 N 3 5 5 S in the crude product of meropenem is not less than 92% by weight percentage, calculated according to the anhydrous substance. ; impurity A, impurity B are not more than 0.8%; any unknown single impurity is not more than 0.3%; the sum of other impurities except A and B is not more than 3.0%;
其中所述杂质 A为:  Wherein the impurity A is:
Figure imgf000030_0001
所述杂质 B为
Figure imgf000030_0001
The impurity B is
Figure imgf000030_0002
优选地, 以重量百分比计, 所述美罗培南粗品中 C17H25N305S的含量 不少于 95%, 以无水物计算; 杂质 A、 杂质 B均不大于 0.6%; 任何未知 单个杂质不大于 0.3%; 除 A和 B外其它杂质总和不大于 2.0%;
Figure imgf000030_0002
Preferably, the content of C 17 H 25 N 3 5 5 S in the crude meropenem is not less than 95%, calculated as an anhydrate; the impurity A and the impurity B are not more than 0.6%; any unknown a single impurity is not more than 0.3%; the sum of other impurities except A and B is not more than 2.0%;
步骤 1 )中所述使美罗培南粗品溶解在温度为 50°C ~ 80°C的水中包括: 将所述美罗培南粗品加入到 10 ~ 20倍重量、 优选 15 ~ 20倍重量的 5 ~ 20 °〇的注射用水中, 搅拌混合均匀, 然后将所得混悬液加热到 50°C ~ 80°C、 优选 60°C ~80°C溶解;其中所述溶解的时间小于 4分钟,优选小于 1分钟; 优选地, 将所得溶液的温度降至 10°C ~25°C; 其中降温的时间小于 4 分钟, 优选小于 1分钟。 Dissolving the crude meropenem in water at a temperature of 50 ° C to 80 ° C in the step 1) includes: adding the crude meropenem to 10 to 20 times by weight, preferably 15 to 20 times by weight of 5 to 20 ° Mix well with water for injection, and then heat the resulting suspension to 50 ° C ~ 80 ° C, Preferably, it dissolves at 60 ° C to 80 ° C; wherein the dissolution time is less than 4 minutes, preferably less than 1 minute; preferably, the temperature of the resulting solution is lowered to 10 ° C to 25 ° C; wherein the cooling time is less than 4 minutes , preferably less than 1 minute.
8. 根据权利要求 6或 7所述的制备方法, 其特征在于, 步骤 2 )包括, 将溶液 I在 15°C ~25°C下经釆用美罗培南粗品重量 1~ 20%的活性炭脱色 1 ~ 30分钟、 优选 1 ~ 10分钟后过滤, 以得到滤液 II;  The preparation method according to claim 6 or 7, wherein the step 2) comprises: dissolving the solution I at a temperature of 15 ° C to 25 ° C with a weight of 1 to 20% of the crude product of meropenem 1 ~ 30 minutes, preferably 1 ~ 10 minutes after filtration, to obtain filtrate II;
或者, 步骤 2) 中, 溶液通过活性炭过滤器在线过滤脱色。  Alternatively, in step 2), the solution is decolorized by in-line filtration through an activated carbon filter.
9. 根据权利要求 6至 8中任一项所述的制备方法, 其特征在于, 步骤 3) 包括, 将滤液 II的温度降至 0°C ~5°C以结晶, 并养晶 2~20小时, 优 选 5~10小时; 过滤后得到母液 3和滤饼, 所述滤饼用丙酮淋洗以洗晶, 在 20°C ~40°C、优选 25°C ~30°C下真空干燥 3 ~ 10小时、优选 5~6小时, 从而得到美罗培南原料药;  The preparation method according to any one of claims 6 to 8, wherein the step 3) comprises: lowering the temperature of the filtrate II to 0 ° C to 5 ° C for crystallization, and maintaining the crystal 2 to 20 Hour, preferably 5~10 hours; after filtration, the mother liquor 3 and the filter cake are obtained, and the filter cake is washed with acetone to wash the crystal, and vacuum dried at 20 ° C ~ 40 ° C, preferably 25 ° C ~ 30 ° C 3 ~ 10 hours, preferably 5 to 6 hours, thereby obtaining a meropenem drug substance;
优选地, 所述养晶为搅拌养晶, 其中搅拌速度为 100~200转 /分钟, 优选 110 ~ 130转 /分钟。  Preferably, the crystal is a stirred crystal, wherein the stirring speed is 100 to 200 rpm, preferably 110 to 130 rpm.
10. 根据权利要求 6至 9中任一项所述的制备方法, 其特征在于, 步 骤 3)还包括, 在结晶前向步骤 2)得到的滤液 II中添加晶种;  The preparation method according to any one of claims 6 to 9, wherein the step 3) further comprises: adding a seed crystal to the filtrate II obtained in the step 2) before crystallization;
其中添加晶种的温度为 0°C ~20°C, 优选 0°C ~5°C; 添加的晶种与美 罗培南粗品的质量比为 1%:1 ~ 10%:1, 优选 1%:1 ~2%:1。  The temperature at which the seed crystal is added is 0 ° C ~ 20 ° C, preferably 0 ° C ~ 5 ° C; the mass ratio of the added seed crystal to the crude product of meropenem is 1%: 1 ~ 10%: 1, preferably 1%: 1 ~ 2%: 1.
11. 根据权利要求 6至 10中任一项所述的制备方法, 其特征在于, 步 骤 3) 中在结晶前, 取滤液 II的 1%~ 10% (重量比), 向其中加入有机溶 剂结晶形成晶种, 将所得晶种加入到剩余的滤液 II中以进行结晶;  The preparation method according to any one of claims 6 to 10, wherein in step 3), 1% to 10% by weight of the filtrate II is taken before crystallization, and an organic solvent is added thereto. Forming a seed crystal, adding the obtained seed crystal to the remaining filtrate II for crystallization;
其中所述有机溶剂选自丙酮、 四氢呋喃、 异丙醇、 曱醇、 乙醇和曱基 乙基酮中的一种或多种, 优选丙酮和 /或四氢呋喃; 所述部分滤液 II 与有 机溶剂的重量 (kg) :体积 (L) 比为 1:2~1:6, 晶种制备温度为 5°C ~20 °C, 优选 10°C ~ 15°C。  Wherein the organic solvent is selected from one or more of acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol and mercaptoethyl ketone, preferably acetone and/or tetrahydrofuran; the weight of the partial filtrate II and the organic solvent (kg): The volume (L) ratio is 1:2 to 1:6, and the seed crystal preparation temperature is 5 ° C to 20 ° C, preferably 10 ° C to 15 ° C.
12. 根据权利要求 6至 11中任一项所述的制备方法, 其特征在于, 步 骤 4 ) 中, 在 5 X 105Pa ~20 X 105Pa、 优选 15 105 Pa ~ 20 χ 105 Pa的压力 和 5~35°C、 优选 10~25°C的温度下进行母液 3的纳滤浓缩, 使得所述母 液 3与所得浓缩液的重量比为 5:1 ~ 15:1、 优选 7:1 ~ 10:1; 所得浓缩液中 美罗培南含量为 5~20重量%, 优选 7~15重量%。 The preparation method according to any one of claims 6 to 11, wherein in step 4), at 5 X 10 5 Pa ~ 20 X 10 5 Pa, preferably 15 10 5 Pa ~ 20 χ 10 5 The pressure of Pa and the nanofiltration concentration of the mother liquor 3 are carried out at a temperature of 5 to 35 ° C, preferably 10 to 25 ° C, so that the weight ratio of the mother liquor 3 to the obtained concentrate is 5:1 to 15:1, preferably 7 : 1 to 10:1; The meropenem content in the obtained concentrate is 5 to 20% by weight, preferably 7 to 15% by weight.
13. 根据权利要求 6至 12中任一项所述的制备方法, 其特征在于, 步 骤 4) 中所述结晶得到美罗培南粗品的体系中的有机溶剂的总体积与水的 体积比为 3:1~6:1; 有机溶剂选自丙酮、 四氢呋喃、 异丙醇、 曱醇、 乙醇 和曱基乙基酮中的一种或多种; 优选地, 结晶温度为 5 °C ~ 15 °C ; The preparation method according to any one of claims 6 to 12, wherein the volume ratio of the total volume of the organic solvent to the water in the system for obtaining the crude product of meropenem in the step 4) is 3: 1~6:1; organic solvent is selected from acetone, tetrahydrofuran, isopropanol, decyl alcohol, ethanol And one or more of mercaptoethyl ketone; preferably, the crystallization temperature is from 5 ° C to 15 ° C ;
进一步优选地, 通过下述方法制备美罗培南粗品过程中的母液 1和母 液 2:  Further preferably, the mother liquor 1 and the mother liquor 2 in the crude meropenem process are prepared by the following method:
将保护美罗培南(或者保护美罗培南浓缩液)、 THF、 水、 3,5,-二曱基 吡啶、 10%钯碳一并加入到高压反应釜中, 除去空气, 通入氢气, 室温反 应毕, 过滤洗涤回收钯碳, 得到母液 1 ;  Add meropenem (or protect meropenem concentrate), THF, water, 3,5,-dimercaptopyridine, 10% palladium carbon to the autoclave, remove the air, pass hydrogen, and react at room temperature. , washing and recovering palladium carbon to obtain mother liquor 1;
此母液中加入所述有机溶剂, 控制温度 10-15 °C搅拌, 过滤, 洗涤, 产品干燥, 得美罗培南 (化合物 I )粗品及母液 2。  The organic solvent is added to the mother liquor, the temperature is controlled at 10-15 ° C, the mixture is filtered, washed, and the product is dried to obtain a crude product of meropenem (Compound I) and a mother liquor 2 .
14. 根据权利要求 2至 13中任一项所述的制备方法, 其特征在于, 所 述方法制备得到的原料药中美罗培南的含量为 98.5% ~ 101.0%, 以无水物 计算; 所述原料药的有关物质中杂质 、 杂质 B均不大于 0.25%; 任何未 知单个杂质不大于 0.05%; 除 A和 B外其它杂质总和不大于 0.2%; 丙酮 残留不大于 400ppm, 优选不大于 100ppm。  The preparation method according to any one of claims 2 to 13, wherein the content of meropenem in the raw material prepared by the method is 98.5% ~ 101.0%, calculated as an anhydrate; The impurities and impurities B in the relevant substances of the raw material drug are not more than 0.25%; any unknown single impurity is not more than 0.05%; the sum of other impurities except A and B is not more than 0.2%; the acetone residue is not more than 400 ppm, preferably not more than 100 ppm.
15. 一种美罗培南药物组合物, 其含有根据权利要求 1所述的美罗培 南原料药和药学上可接受的辅料;  A pharmaceutical composition of meropenem comprising the meropenem bulk drug according to claim 1 and a pharmaceutically acceptable excipient;
优选地, 所述药学上可接受的辅料为无菌碳酸钠, 其中美罗培南原料 药与无菌碳酸钠的重量比为 1000: 195 ~ 1000: 222;  Preferably, the pharmaceutically acceptable excipient is sterile sodium carbonate, wherein the weight ratio of meropenem to sterile sodium carbonate is 1000: 195 ~ 1000: 222;
进一步优选地, 所述药物组合物为注射剂。  Further preferably, the pharmaceutical composition is an injection.
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