CN104922065B - Stable flurbiprofen axetil pharmaceutical composition - Google Patents

Stable flurbiprofen axetil pharmaceutical composition Download PDF

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CN104922065B
CN104922065B CN201510319464.3A CN201510319464A CN104922065B CN 104922065 B CN104922065 B CN 104922065B CN 201510319464 A CN201510319464 A CN 201510319464A CN 104922065 B CN104922065 B CN 104922065B
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phosphatidyl
flurbiprofen axetil
oil
pharmaceutical composition
choline
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CN104922065A (en
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林静文
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Jiangsu Huiju Pharmaceutical Co ltd
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Beijing Landan Pharmaceutical Technology Co ltd
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Abstract

The invention provides a stable flurbiprofen axetil pharmaceutical composition, which contains flurbiprofen axetil, phosphatidylcholine, phosphatidylethanolamine, oil for injection and water for injection; wherein the weight percentage of each component is as follows: 0.1-1% w/v of flurbiprofen axetil, 0.4-1.6% w/v of phosphatidylcholine, less than or equal to 0.18% w/v of phosphatidylethanolamine, and 10-30% w/v of oil for injection. The composition has improved stability, contains reduced levels of flurbiprofen as a hydrolyzed impurity, and has an extended shelf life of from 18 months to 24 months compared to commercially available products.

Description

A kind of Flurbiprofen axetil pharmaceutical composition of stabilization
Technical field
The present invention relates to a kind of Flurbiprofen axetil pharmaceutical composition of stabilization and preparation method thereof, and in particular to its effectively into Divide the stability and its emulsion stability of flurbiprofen axetil.
Background technology
Flurbiprofen axetil is the pro-drug of Flurbiprofen, the analgesia available for Post operation and various cancers.Flurbiprofen Ester injection is a kind of nonsteroidal targeted analgesics, and prostate is reduced by suppressing Cycloxygenase (COX) in spinal cord and periphery The synthesis of element, reduce hyperalgesic state caused by operation wound.Fat emulsion formulation drug effect is stronger, works rapider, when continuing Between it is longer, and be not easy to cause the adverse reactions such as mucosal lesion.It is used for Postoperative Analgesia After, and advantage is that no CNS inhibition is made With not influenceing the revival in narcosis patient, can use immediately after surgery.Presently commercially available Flurbiprofen ester formulation only has Florfenicol residues (trade name Furbiprofen axetil).
But existing flurbiprofen axetil fat emulsion can be because process conditions, storage bar during preparing, storing Part and influence its stability, national drug standards YBH15412004 require florfenicol residues in 0~20 DEG C of closed guarantor Deposit, avoid freezing, the term of validity 18 months.Flurbiprofen axetil fat emulsion in high-temperature sterilization or placement process it is possible that Particle diameter is unstable or even demulsifying phenomenon, so as to influence its stability and security;Meanwhile its main ingredient flurbiprofen axetil is esters Compound, facile hydrolysis generates impurity Flurbiprofen during storage, so as to cause active constituent content to reduce, on impurity content Rise, influence its validity and security.Various researchs have been carried out in order to improve the stability of flurbiprofen axetil fat emulsion.Example Such as, patent CN102988291B improves its stability by changing preparation technology, and supplementary material mixed process is entered at normal temperatures OK.Patent CN102188393B and CN104188905A are to solve the problems, such as the above by changing prescription, but from injection From the aspect of the Clinical practice security of agent, although the species for increasing auxiliary material may improve the vitro stability of preparation, together When also increase internal potential safety hazard.
In view of the foregoing, the present invention develops the good good flurbiprofen axetil of emulsion stability simultaneously of medicine stability Pharmaceutical composition.
The content of the invention
The invention provides a kind of Flurbiprofen axetil pharmaceutical composition of stabilization with and preparation method thereof, be related to its effectively into Divide the stability of flurbiprofen axetil and the stability of fat emulsion.
The invention provides a kind of Flurbiprofen axetil pharmaceutical composition of stabilization, containing flurbiprofen axetil, phosphatidyl choline, Phosphatidyl-ethanolamine, oil for injection, the percentage of appearance again of water for injection, wherein each component are as follows:
The percentage of appearance again of above-mentioned Flurbiprofen axetil pharmaceutical composition, wherein phosphatidyl-ethanolamine is preferably 0.15%- 0.18%w/v.
Above-mentioned Flurbiprofen axetil pharmaceutical composition, the percentage of appearance again of phosphatidyl-ethanolamine are further preferably less than 0.15%w/v, and contain the phosphatidyl glycerol that appearance percentage is 0.02-0.2%w/v again.More preferably phosphatidyl-ethanolamine 0.06%~0.14%w/v, 0.05~0.1%w/v of phosphatidyl glycerol.
The phosphatidyl choline is the phosphatidyl choline and its salt of natural origin, such as the phosphorus extracted in soybean or yolk Phosphatidylcholine and its salt, the phosphatidyl choline and its salt or their any combination of synthesis;The phosphatidyl choline choosing of the synthesis From DSPC (DSPC), dioleyl phosphatidyl choline (DOPC), Dioctonoyl pnosphotidyl choline (DPPC), L-Dimyristoylphosphatidylcholine (DMPC), DDPC DDPC, dilauroyl phosphatidyl courage Alkali (DLPC), two mustard phosphatidyl cholines (DEPC), 1- stearyl -2- oleolyl phosphatidyl cholines (SOPC), 1- palms Acyl group -2- oleolyl phosphatidyl cholines (POPC), 1- myristoyl -2- oleolyl phosphatidyl cholines (MOPC), 1- stearoyls Base -2- palmityls phosphatidyl choline (SPPC), 1- stearyl -2- myristoyls phosphatidyl cholines (SMPC), 1- palms Acyl group -2- stearoyl phosphatidyls choline (PSPC), 1- palmityl -2- myristoyls phosphatidyl cholines (PMPC), 1- meat Cardamom acyl group -2- stearoyl phosphatidyls choline (MSPC), 1- myristoyl -2- palmityls phosphatidyl cholines (MPPC) or It is combined.
The phosphatidyl glycerol be natural origin phosphatidyl glycerol and its salt, the phosphatidyl glycerol and its salt of synthesis or it Any combination;The phosphatidyl glycerol of the synthesis is selected from DSPG (DSPG), dioleoyl phosphatide Acyl glycerine (DOPG), DPPG (DPPG), DMPG (DMPG), 1- palmityls Base -2- oleolyl phosphatidyls glycerine (POPG), two mustard acyl phosphatidyl glycerols (DEPG), PE (DLPG) or It is combined.
The phosphatidyl-ethanolamine be natural origin phosphatidyl-ethanolamine and its salt, the phosphatidyl-ethanolamine of synthesis and its Salt or their any combination;The phosphatidyl-ethanolamine of the synthesis is selected from DSPE (DSPE), and two Oleolyl phosphatidyl monoethanolamine (DOPE), DPPE (DPPE), two myristoyl phosphatidyl ethanols Amine (DMPE), two mustard acyl phosphatidyl-ethanolamines (DEPE), two lauroyl phosphatidyl-ethanolamines (DLPE) or its combination.
In above-mentioned Flurbiprofen axetil pharmaceutical composition, the oil for injection be selected from refined soybean oil, safflower oil, cottonseed oil, Olive oil, coconut oil, castor oil, fish oil, medium chain mono, medium chain triglyceride dibasic acid esters, medium chain triglyceride, ethyl oleate, second Acylated monoglyceride, propane diols dibasic acid esters, glyceryl linoleate, polyethylene glycol glyceryl laurate ester or its combination;Preferably olive Oil and medium chain triglyceride, both weight ratios are 1:1.
Above-mentioned Flurbiprofen axetil pharmaceutical composition, it is characterised in that be also selected from hydrogen comprising pH adjusting agent, the pH adjusting agent Sodium oxide molybdena, hydrochloric acid, phosphoric acid, phosphate, citric acid, citrate, acetic acid, acetate or its combination.
Above-mentioned Flurbiprofen axetil pharmaceutical composition, it is characterised in that also comprising isotonic regulator, the isotonic regulator choosing From glycerine, glucose, mannitol, propane diols or its combination.
The preparation method of above-mentioned Flurbiprofen axetil pharmaceutical composition, comprises the following steps:
(1) preparation of oil phase:Flurbiprofen axetil, phosphatidyl choline, phosphatidyl-ethanolamine, phosphatide are added into oil for injection The stirring of acyl glycerine makes its dissolving, as oil phase;
(2) preparation of colostrum:Step (1) oil phase is added in the water for injection containing isotonic regulator, high speed shear point Dissipate, form colostrum;
(3) it is high-pressure homogenising:Step (2) colostrum is high-pressure homogenising, obtains smart breast;
(4) filter, embedding, sterilize (F0>12), produce.
Flurbiprofen axetil fat emulsion prepared by the present invention is contrasted with commercially available flurbiprofen axetil fat emulsion, can To obtain the more excellent flurbiprofen axetil Fat Emulsion of stability, reduce the degraded of flurbiprofen axetil, impurity Flurbiprofen Content is lower, while can extend the shelf-life of flurbiprofen axetil fat emulsion, and 24 months were extended to from 18 months.
Embodiment
Comparative example 1
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil is taken, is heated to 65 DEG C, adds phosphatidyl choline, phosphatidyl-ethanolamine and flurbiprofen axetil, stirring is molten Solution, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
Comparative example 2
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil is taken, is heated to 65 DEG C, adds phosphatidyl choline, phosphatidyl-ethanolamine and flurbiprofen axetil, stirring is molten Solution, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
Comparative example 3
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil is taken, is heated to 65 DEG C, phosphatidyl choline, phosphatidyl-ethanolamine, phosphatidyl glycerol and fluorine is added and compares Lip river Fragrant ester, stirring and dissolving, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
Comparative example 4
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil is taken, is heated to 65 DEG C, adds phosphatidyl choline, phosphatidyl glycerol and flurbiprofen axetil, stirring is molten Solution, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
Embodiment 1
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil is taken, is heated to 65 DEG C, adds phosphatidyl choline, phosphatidyl-ethanolamine and flurbiprofen axetil, stirring is molten Solution, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
Embodiment 2
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil is taken, is heated to 65 DEG C, adds phosphatidyl choline, phosphatidyl-ethanolamine and flurbiprofen axetil, stirring is molten Solution, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
Embodiment 3
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil is taken, is heated to 65 DEG C, phosphatidyl choline, phosphatidyl-ethanolamine, phosphatidyl glycerol and fluorine is added and compares Lip river Fragrant ester, stirring and dissolving, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
Embodiment 4
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil is taken, is heated to 65 DEG C, adds phosphatidyl choline, phosphatidyl glycerol and flurbiprofen axetil, stirring is molten Solution, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
Test case 1
0 day under the conditions of the sample of embodiment 1~4 and comparative example 1~4 is respectively placed in into 60 DEG C, 5 days, determine within 10 days The content of milk particle particle diameter and hydrolysis impurity Flurbiprofen.
It is as shown in table 1 to influence result of the test:
Table 1
It is can be found that according to comparative example 1-2 and embodiment 1-2 test result:The content of hydrolysis impurity Flurbiprofen is with PE Increase and be in increased trend, when PE holds percentage and is more than 0.18%w/v again, the increase of Flurbiprofen content becomes apparent (increased to 1.81%) when being 0.91%, 10 days during 1 Flurbiprofen content of comparative example 0 day, therefore PE is held to percentage control again In below 0.18%w/v, the content of hydrolysis impurity Flurbiprofen can be effectively reduced.Can according to the test result of average grain diameter To find, when PE, which holds percentage, is less than 0.15%w/v again, the average grain diameter of milk particle is more than 300nm (comparative example 2, average grain diameter It is 348.5nm at 0 day, is 356.7nm at 30 days).According to hydrolysis impurity and the testing result of average grain diameter, PE holds percentage again Preferably 0.15-0.18%w/v.
According to comparative example 3 and the average grain diameter of embodiment 3 and Flurbiprofen testing result, 0.02% can will be defined under PG w/v;According to comparative example 4 and embodiment 4 it can be found that with the increase of PG amounts, stablizing effect does not increase and average grain diameter is omited There is increase, therefore 0.2%w/v will be defined on PG.
Test case 2
By comparative example 1, embodiment 2, the sample obtained by embodiment 3 is placed 24 months under the conditions of 18 DEG C, determination sample The content of average grain diameter and hydrolysis impurity Flurbiprofen at 0,3,6,9,12,18,24 month, as a result as shown in table 2.
Table 2
It can be obtained by the result of table 2, at 24 months, the flurbiprofen axetil Fat Emulsion obtained by embodiment 2 and embodiment 3 was being put Particle diameter is stable during putting, and the content of hydrolysis impurity Flurbiprofen is significantly lower than comparative example 1.
Embodiment 5
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) olive oil is taken, is heated to 65 DEG C, adds phosphatidyl choline, DSPE and flurbiprofen axetil, stirring and dissolving, as Oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
After tested, Flurbiprofen content is 0.15%, and the average grain diameter of milk particle is 315.7nm.
Embodiment 6
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) olive oil and medium chain triglyceride are taken, is heated to 65 DEG C, phosphatidyl choline, DSPE, DSPG and fluorine is added and compares Lip river Fragrant ester, stirring and dissolving, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
After tested, Flurbiprofen content is 0.18%, and the average grain diameter of milk particle is 220.8nm.
Embodiment 7
General step prepared by emulsion is described as follows:
(1) water for injection is taken, is heated to 65 DEG C, glycerine dissolving is added, as aqueous phase;
(2) soybean oil and medium chain triglyceride are taken, is heated to 65 DEG C, adds phosphatidyl choline, phosphatidyl-ethanolamine, phosphatide Acyl glycerine and flurbiprofen axetil, stirring and dissolving, as oil phase;
(3) under high speed shear, oil phase is added in 65 DEG C of aqueous phase, high speed shear speed 10000rpm, the time 10min, form colostrum;
(4) disodium hydrogen phosphate citrate buffer (disodium hydrogen phosphate and citric acid mol ratio 4:1) colostrum pH value 6.0 is adjusted ~6.5, add to the full amount of water for injection;
(5) colostrum is transferred in high pressure homogenizer and emulsified, homogenization pressure 1000bar, 3 circulations;
(6) filter:By smart breast through 0.45 μm of filtering with microporous membrane, embedding;
(7) moist heat sterilization (F0>12), produce.
After tested, Flurbiprofen content is 0.30%, and the average grain diameter of milk particle is 239.8nm.
Sample obtained by embodiment 5-7 shows that its milk particle particle diameter is stable through study on the stability result, and Flurbiprofen content is obvious Less than the Flurbiprofen in the sample of same period comparative example 1.

Claims (10)

1. a kind of Flurbiprofen axetil pharmaceutical composition, contain flurbiprofen axetil, phosphatidyl choline, phosphatidyl-ethanolamine, injection Oil, water for injection;The percentage of appearance again of wherein each component is as follows:
2. a kind of Flurbiprofen axetil pharmaceutical composition, contain flurbiprofen axetil, phosphatidyl choline, phosphatidyl-ethanolamine, phosphatidyl Glycerine, oil for injection, water for injection;The percentage of appearance again of wherein each component is as follows:
3. Flurbiprofen axetil pharmaceutical composition according to claim 2, it is characterised in that appearance hundred again of phosphatidyl-ethanolamine Divide 0.06~0.14%w/v of ratio, it is 0.05-0.1%w/v that phosphatidyl glycerol holds percentage again.
4. Flurbiprofen axetil pharmaceutical composition according to claim 1 or 2, it is characterised in that described phosphatidyl choline For the phosphatidyl choline and its salt of natural origin, the phosphatidyl choline and its salt or their any combination of synthesis;It is described natural The phosphatidyl choline that the phosphatidyl choline in source extracts in soybean or yolk, the phosphatidyl choline of the synthesis are selected from two Stearoyl phosphatidyl choline, dioleyl phosphatidyl choline, Dioctonoyl pnosphotidyl choline, two myristoyl phosphatidyls Choline, DDPC DDPC, DLPC, two mustard phosphatidyl cholines, 1- stearoyls Base -2- oleolyl phosphatidyl cholines, 1- palmityl -2- oleolyl phosphatidyl cholines, 1- myristoyl -2- oleolyl phosphatidyls Phatidylcholine, 1- stearyl -2- palmityl phosphatidyl cholines, 1- stearyl -2- myristoyl phosphatidyl cholines, 1- palm fibres Palmitic acid acyl group -2- stearoyl phosphatidyl choline, 1- palmityl -2- myristoyl phosphatidyl cholines, 1- myristoyls -2- Stearoyl phosphatidyl choline, 1- myristoyls -2- palmityls phosphatidyl choline or its combination.
5. Flurbiprofen axetil pharmaceutical composition according to claim 1 or 2, it is characterised in that described phosphatidyl ethanol Amine be natural origin phosphatidyl-ethanolamine and its salt, the phosphatidyl-ethanolamine and its salt or their any combination of synthesis;Institute The phosphatidyl-ethanolamine for stating synthesis is selected from DSPE, DOPE, two palmityls Base phosphatidyl-ethanolamine, two myristoyl phosphatidyl-ethanolamines, two mustard acyl phosphatidyl-ethanolamines, two lauroyl phosphatidyl ethanols Amine or its combination.
6. Flurbiprofen axetil pharmaceutical composition according to claim 2, it is characterised in that described phosphatidyl glycerol is day Phosphatidyl glycerol and its salt, the phosphatidyl glycerol of synthesis and its salt or their any combination in right source;The phosphorus of the synthesis Phosphatidyl glycerol is selected from DSPG, DOPG, DPPG, two meat Cardamom acyl group phosphatidyl glycerol, 1- palmityl -2- oleolyl phosphatidyl glycerine, two mustard acyl phosphatidyl glycerols, two lauroyl phosphorus Phosphatidyl glycerol or its combination.
7. Flurbiprofen axetil pharmaceutical composition according to claim 1 or 2, it is characterised in that described injection grease separation Autofining soybean oil, safflower oil, cottonseed oil, olive oil, coconut oil, castor oil, fish oil, medium chain mono, medium chain triglyceride are double Ester, medium chain triglyceride, ethyl oleate, acetylated monoglyceride, propane diols dibasic acid esters, glyceryl linoleate, polyethylene glycol bay Acid glyceride or its combination.
8. Flurbiprofen axetil pharmaceutical composition according to claim 7, it is characterised in that described oil for injection is olive Oil and medium chain triglyceride, both weight ratios are 1:1.
9. Flurbiprofen axetil pharmaceutical composition according to claim 1 or 2, it is characterised in that also comprising pH adjusting agent, institute State pH adjusting agent and be selected from sodium hydroxide, hydrochloric acid, phosphoric acid, phosphate, citric acid, citrate, acetic acid, acetate or its combination.
10. Flurbiprofen axetil pharmaceutical composition according to claim 1 or 2, it is characterised in that also comprising isotonic regulation Agent, the isotonic regulator are selected from glycerine, glucose, mannitol, propane diols or its combination.
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CN104644554A (en) * 2015-03-05 2015-05-27 北京蓝丹医药科技有限公司 Etomidate pharmaceutical composition and preparation method thereof

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Publication number Priority date Publication date Assignee Title
US11839590B2 (en) 2018-10-10 2023-12-12 Grand life science (wuhan) co., LTD Flurbiprofen axetil emulsion for injection and preparation method thereof

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