WO2008117271A1 - (1r,1'r)-atracurium salts separation process - Google Patents
(1r,1'r)-atracurium salts separation process Download PDFInfo
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- WO2008117271A1 WO2008117271A1 PCT/IL2008/000291 IL2008000291W WO2008117271A1 WO 2008117271 A1 WO2008117271 A1 WO 2008117271A1 IL 2008000291 W IL2008000291 W IL 2008000291W WO 2008117271 A1 WO2008117271 A1 WO 2008117271A1
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- acid
- phase
- salt
- mixture
- cisatracurium
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D217/00—Heterocyclic compounds containing isoquinoline or hydrogenated isoquinoline ring systems
- C07D217/12—Heterocyclic compounds containing isoquinoline or hydrogenated isoquinoline ring systems with radicals, substituted by hetero atoms, attached to carbon atoms of the nitrogen-containing ring
- C07D217/18—Aralkyl radicals
- C07D217/20—Aralkyl radicals with oxygen atoms directly attached to the aromatic ring of said aralkyl radical, e.g. papaverine
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B57/00—Separation of optically-active compounds
Definitions
- the present invention relates to chromatography and more particularly to an improved method of separating the (lR,rR)-atracurium salts isomers by means of high pressure liquid chromatography (HPLC).
- HPLC high pressure liquid chromatography
- Neuromuscular blocking agents e.g., atracurium besylate, pancuronium bromide, rocuronium bromide, vecuronium bromide
- Neuromuscular blocking agents interrupt transmission of nerve impulses at the skeletal neuromuscular junction and are typically divided into two types: competitive, stabilizing blockers (nondepolarizing neuromuscular agents) and noncompetitive, depolarizing agents (depolarizing neuromuscular agents). Both types prevent acetylcholine from triggering the muscle contraction and are typically used as anesthesia adjuvants in the operating theatre for aiding intubation i.e.
- therapy is performed by i.v. administration of a suitable dosage form.
- Atracurium besylate [2,2'-[l,5-pentanediylbis[oxy(3-oxo-3,l- propanediyl)]]bis[ 1 -[(3 ,4-dimethoxyphenyl)methyl]- 1 ,2,3 ,4-tetrahydro-6,7-dimethoxy-2- methyl-isoquinolinium dibenzenesulfonate] was first approved for human medical use in 1982.
- NTMBEX ® is a sterile, non-pyrogenic aqueous solution that is adjusted to pH 3.25 to 3.65 with benzenesulfonic acid.
- the drug is provided in 2.5 ml, 5 ml and 10 ml ampules having a strength of 2 mg/ml cisatracurium besylate.
- a 30 ml vial containing 5 mg/ml cisatracurium besylate is also available.
- Cisatracurium besylate has the structural formula below.
- ( ⁇ )-terahydropapaverine hydrochloride is resolved with N-acetyl-L-leucine to obtain (R)-terahydropapaverine N- acetyl-L-leucinate, which is converted to the free base and reacted with the 1,5- pentamethylene diacrylate in hot glacial acetic acid, purified by column chromatography, and treated with oxalic acid to afford (1R, ⁇ R)-2,2'-(3, 1 l-dioxo-4,10-dioxatridecylene)- bis-( 1 ,2,3 ,4-tetrahydro-6,7-dimethoxy-2-methyl- 1 -veratryliso-quinolinium di oxalate (II), which is treated with methyl benzenesulfonate to obtain the (lR,rR)-atracurium besylate isomer mixture, i.e., (lR-cis-1'R
- the mixture is separated by means of liquid chromatography, using either irregular or spherical silica column in a mixture of dichloromethane and a strong acid, e.g., methanesulfonic acid, or in a mixture of dichloromethane, methanol and a strong acid, e.g., benzenesulfonic acid.
- HPLC methods for separating the isomers of (lR,rR)-atracurium besylate using strong acids may be unsatisfactory for large scale production because stainless steel (commonly used in HPLC instruments) is not compatible with strong acids (such as benzenesulfonic acid) due to an excessive corrosion of stainless steel components resulting in the possible contamination of the product, which is also undesirable, especially on large scale. Accordingly, there is a need for an improved method for separating the isomers of (lR,l'R)-atracurium besylate, particularly a commercially viable method, which employs an aqueous mobile phase and yet avoids problems associated with aqueous mobile phase instability. The present invention provides such methods.
- the present invention provides a chromatographic method for separating the (lR,rR)-atracurium salt (e.g., the besylate salt) isomer mixture, which includes, e.g., Reverse Phase, High Performance Liquid Chromatography (HPLC), to produce highly pure lR-cis,l'R-cis isomer (cisatracurium besylate).
- a chromatographic method for separating the (lR,rR)-atracurium salt e.g., the besylate salt
- HPLC High Performance Liquid Chromatography
- the desired lR-cis,l'R-cis isomer can be separated from the (lR,l'R)-atracurium salt (e.g., the besylate salt) isomer mixture by: loading a solution of (lR,rR)-atracurium salt (e.g., the besylate salt) into an HPLC system equipped with a separating column comprising a suitable Reverse Phase (RP) stationary phase; eluting the column with an eluent, which includes an aqueous phase, an organic solvent or a mixture thereof; collecting at least one fraction comprising the desired product; and isolating the product.
- RP Reverse Phase
- Suitable RP stationary phases can include, for example, Cl stationary phase, C3 stationary phase, C4 stationary phase, C8 stationary phase, C 14 stationary phase, C18 stationary phase, other polymeric packing, e.g., polyamide, polymethacrylate, polystyrene, and the like.
- a preferred method of the invention includes performing HPLC separation using a C18 RP stationary phase, which is eluted with a mobile phase comprising a buffer, that is, a mixture of a weak acid and its conjugate salt (e.g., acetic acid and sodium acetate, citric acid and sodium citrate, or ammonium formate and formic acid) and a solvent such as methanol.
- a weak acid and its conjugate salt e.g., acetic acid and sodium acetate, citric acid and sodium citrate, or ammonium formate and formic acid
- Figure 1 depicts the effect of buffer concentration on the retention of the IR- cis,l'R-cis isomer
- Figure 2 depicts the effect of buffer concentration on the resolution of the IR- cis,l'R-trans and lR-cis, l'R-cis isomers
- Figure 3 A depicts the chromatogram of an atracurium besylate reference sample.
- Figure 3B lists peak data associated with the chromatogram depicted in Fig. 3A.
- Figure 4A depicts the chromatogram of atracurium besylate, sample 1.
- Figure 4B lists peak data associated with the chromatogram depicted in Fig. 4A.
- Figure 5 A depicts the chromatogram of cisatracurium besylate, sample 2.
- Figure 5B lists peak data associated with the chromatogram depicted in Fig. 5A.
- Figure 6A depicts the chromatogram of (lR,l'R)-atracurium besylate obtained according to the gradient detailed in Table 3.
- Figure 6B lists peak data associated with the chromatogram depicted in Fig. 6A.
- Figure 7 depicts the stability of (IR, l'R)-atracurium besylate at different pH values.
- the term "mildly acidic" mobile phase refers to mobile phase containing a solvent and an aqueous phase, which includes a weak organic acid, having pKa value of 2.5 and higher, such as acetic acid.
- the "mildly acidic” mobile phase is distinguishable from the methods described above, using strong acids (having pKa value of 0 and lower) such as benzenesulfonic acid.
- aqueous phase which includes a weak organic acid and its conjugate salt, such as formic acid and ammonium formate
- isomeric purity refers to the area percent of the peak corresponding to the lR-cis,l'R-cis isomer relative to the area percent of the (IR- cis,l'R-cis isomer), (lR-cis,l'R-trans) and (lR-trans,l'R-trans) isomers.
- Isomeric purity may be expressed in terms of the following equation:
- A % area of the lR-cis,l'R-cis isomer
- B % area of the lR-cis,l'R-trans isomer
- C % area of the lR-trans, l'R-trans isomer
- the present invention provides a chromatographic method for separating the isomers of (lR,l'R)-atracurium salt (e.g., the besylate salt), which uses a Reverse Phase HPLC (RP HPLC) method for obtaining a highly pure product, that is lR-cis,l'R- cis isomer salt (e.g., the besylate salt), having isomeric purity higher than 99.5%.
- RP HPLC Reverse Phase HPLC
- separating the desired lR-cis,lR'-cis isomer from a mixture of isomers by a method, which includes: loading a solution of (lR,l'R)-atracurium salt (e.g., the besylate salt) into a Reverse Phase HPLC system, equipped with a suitable separating column comprising a stationary phase; eluting the column with an eluent mobile phase that includes an aqueous phase, an organic solvent or a mixture thereof; collecting at least one fraction comprising the desired product; and isolating the product.
- a method which includes: loading a solution of (lR,l'R)-atracurium salt (e.g., the besylate salt) into a Reverse Phase HPLC system, equipped with a suitable separating column comprising a stationary phase; eluting the column with an eluent mobile phase that includes an aqueous phase, an organic solvent or a mixture thereof; collecting at least one fraction comprising the desired product;
- the lR-cis, 1 'R-cis isomer obtained in accordance with the present invention preferably is substantially free of other geometrical and optical isomers.
- the obtained lR-cis,l'R-cis isomer salt e.g., the besylate salt
- the highly pure lR-cis, l'R-cis isomer is obtained having isomer purity of at least about 98.5%, and preferably having an isomer purity higher than 99.5%.
- a suitable RP stationary phase column can include Cl stationary phase, C3 stationary phase, C4 stationary phase, C 8 stationary phase, C14 stationary phase, C18 stationary phase, other polymeric packing, e.g., polyamide, polymethacrylate, polystyrene, and the like.
- the RP HPLC separation method of the present invention can be utilized on analytical, semi -preparative and preparative scales.
- Preferred organic bonded reverse phases for obtaining the lR-cis-1'R-cis isomer include Cl, C4 and C18 phases.
- the results of exemplary RP methods for isolating the lR-cis-1'R-cis isomer from the (IR, l'R)-atracurium besylate isomer mixture on different stationary phases are provided in Table 1 below.
- the eluent includes an aqueous phase that contains at least one organic solvent.
- the aqueous phase preferably comprises an aqueous mixture of an acid and optionally also an inorganic salt (e.g. NaCl) or an amine (e.g., triethylamine).
- an inorganic salt e.g. NaCl
- an amine e.g., triethylamine
- the aqueous phase further includes a buffer, e.g., a mixture of a weak acid and its conjugate salt (e.g., acetic acid and sodium acetate or citric acid and sodium citrate).
- a buffer e.g., a mixture of a weak acid and its conjugate salt (e.g., acetic acid and sodium acetate or citric acid and sodium citrate).
- Suitable buffers include, for example, mixtures of acetic acid and sodium acetate, citric acid and sodium citrate, formic acid and ammonium formate, and the like.
- the acid can be either an organic or inorganic acid.
- Preferred organic acids include, for example, acetic acid, citric acid, formic acid, camphoric acid, adamantaneacetic acid and the like, and combinations thereof.
- Preferred inorganic acids include, for example, hydrochloric acid, hydrobromic acid, phosphoric acid, boric acid, nitric acid, and the like, and
- Suitable organic solvents which may be included in the aqueous mobile phase in accordance with the present invention, include, for example, acetonitrile, methanol, ethanol, isopropyl alcohol, tetrahydrofuran (THF), and the like, and mixtures thereof.
- the (IR, l'R)-atracurium besylate isomers are separated by eluting with an aqueous phase that contains a salt of an acid, or an acid and a conjugate salt of an acid (e.g., nitric acid and sodium nitrate), at a pH of from about 1.0 to about 5.5, and more preferably at a pH of from about 3.0 to about 3.5.
- Suitable acid salts can include, for example, ammonium formate, sodium formate, ammonium acetate, sodium acetate, sodium nitrate, sodium chloride, potassium chloride, barium chloride, sodium bromide, calcium bromide, monopotassium dihydrogenphosphate, monosodium dihydrogenphosphate, and the like, and combinations thereof.
- Preferred buffer concentrations, for isolating the lR-cis,l'R-cis isomer range from about 20 mM to about 40 mM. In some instances, a buffer concentration in the higher range increases the retention time of the lR-cis, l'R-cis isomer, as depicted in Figure 1, and also improves the isomer's separation, as depicted in Figure 2.
- the cisatracurium salt is substantially stable under the separation conditions of the present invention.
- a desired counter anion may be introduced, e.g., by an ion exchange process, which can include, e.g., adding desired counter anions to the system to exchange with other anions utilized in the separation process, which may associate with one or more of the (lR,l'R)-atracurium isomers. Any suitable ion exchange methods may be utilized as well, e.g., a suitable ion exchange resin.
- the isolation of the cisatracucium from the elution liquid mixture can be carried out by any suitable method such as Solid Phase Extraction (SPE).
- SPE Solid Phase Extraction
- a non-limiting example of a method for isolating the cisatracucium solution from the elution liquid is by SPE.
- the isolation can be effected by successively transferring a cisatracurium besylate sample solution (containing the aqueous phase and the organic solvent) and water through a C18 sorbent, which causes the separation of the cisatracurium besylate from the buffer species.
- the cisatracurium besylate retained by the sorbent can be then removed, e.g., by eluting from the sorbent with methanol.
- the evaluation of the anions is preferably carried out by HPLC, and the cations are preferably evaluated indirectly (since the cations and the anions are removed at about the same rate). Recovery of the isolated material and the anions can be checked after performing each step of the SPE method.
- the present invention provides a SPE method for isolating a product (e.g., an isomer of (lR,l'R)-actracurium besylate) from an HPLC elution liquid mixture, which method preferably includes: successively transferring the sample solution and water through a sorbent; eluting the product from the sorbent with an organic solvent, e.g., methanol; and washing the sorbent with an organic solvent, e.g., methanol.
- a product e.g., an isomer of (lR,l'R)-actracurium besylate
- HPLC elution liquid mixture which method preferably includes: successively transferring the sample solution and water through a sorbent; eluting the product from the sorbent with an organic solvent, e.g., methanol; and washing the sorbent with an organic solvent, e.g., methanol.
- the SPE method of the present invention can be utilized for isolating the IR- cis,l'R-cis isomer from a HPLC elution liquid mixture thereof.
- the method includes: optionally evaporating at least a portion of the organic solvent from an aqueous HPLC elution liquid containing an organic solvent; adding an organic solvent and separating the phases and optionally washing the organic layer; optionally changing the anion using a suitable ion exchange method; and isolating the product from the aqueous phase by spray-drying or freeze-drying.
- the organic solvent added in the SPE method of the present invention can include, for example, ethyl acetate, n-propyl acetate, isopropyl acetate, n-butyl acetate, isobutyl acetate, toluene, chloroform, dichloromethane, and the like, and mixtures thereof.
- a preferred solvent for the SPE method of the present invention is dichloromethane.
- the present invention further provides a pharmaceutical composition comprising substantially pure cisatracurium besylate, which can be obtained in accordance with the present invention, and can be employed, e.g., in surgery as a neuromuscular blocking agent as a formulation for administration, e.g., by injection or infusion.
- Figure 3 depicts the chromatogram of a reference sample obtained by diluting a lyophilized atracurium besylate sample, containing, inter alia, approximately 54% IR- cis,l'R-cis, 34% lR-cis,l'R-trans and 6% lR-trans,l'R-trans isomers (hereinafter the "reference sample”), and a small amount of benzenesulfonic acid in the corresponding aqueous phase, and injecting the mixture into the HPLC system, equipped with a C18 stationary phase according to a gradient method in which the eluent contains a mixture of an aqueous phase and at least one solvent.
- reference sample approximately 54% IR- cis,l'R-cis, 34% lR-cis,l'R-trans and 6% lR-trans,l'R-trans isomers
- FIG 4 depicts the chromatogram of an exemplary starting sample of (lR,rR)-atracurium besylate isomer mixture (hereinafter "sample 1")
- Figure 5 depicts the chromatogram of a cisatracurium besylate (NIMBEX ® ) buffer solution (hereinafter "sample T).
- Cisatracurium besylate was analyzed by High Performance Liquid Chromatography (HPLC). Exemplary HPLC separations were performed, e.g., using the following conditions: Column and packing - Hypersil Hyperprep HS C 18, 250x21.2 mm, 15 ⁇ , P.N. 37115-125; UV detection - UV operated at 280 nm; flow rate: 13 ml/min; Mobile phase: Eluent A: 2OmM NaNO 3 , pH adjusted to 2.0 with HNO 3. Eluent B: methanol. The gradient elution is as detailed in Table 2:
- This example demonstrates a Reverse Phase procedure for isolating cisatracurium besylate on C18 stationary phase using different aqueous phases.
- Atracurium besylate reference sample 10 mg/ml was analyzed on a C 18 stationary phase by gradient elution, using different aqueous phases in the solvent mixtures with methanol.
- Column and packing Alltech, Altima C18, 250x4.6x5 ⁇ , Cat. No. 88056; UV detection: 280 nm; flow rate: 1 ml/min; The results, including the gradient elutions, are detailed in Table 4:
- the (IR, l'R)-atracurium besylate reference sample was separated by semi- preparative Reverse Phase HPLC method as follows: Hypersil Hyperprep HS C 18, 250x21.2 mm, 15 ⁇ Column, conditions: 20 mM NaNO 3 , pH adjusted to 2.0 with HNO 3. Eluent B: methanol. Flow rate: 13 ml/minute. The gradient elution is as detailed in Table 2. [0056] The sample solutions for the preparative HPLC separation were prepared as follows: Solution 1, 827.3 mg of the (lR,l'R)-atracurium besylate reference sample was dissolved in 20 ml Eluent A (concentration: 33.1 mg/ml).
- FIG. 7 A graph depicting the stability of the lR-cis, lR'-trans isomer at different pH values is provided in Fig. 7, which demonstrates that at pH 3, after 20 hours the % area of the IR- cis,l'R-cis isomer is only slightly reduced while at pH 5.5 the % area of the lR-cis, l'R-cis isomer is significantly reduecd.
- X 0 % of cisatracurium at T 0
- X 2] % of cisatracurium at after 24 hours.
- the buffer used was the Na CH 3 COOYCH 3 COOH buffer at 3 different pH values, that is pH values of 3.0, 4.6 and 5.5.
- the values in the table are represented as % of cisatracurium besylate.
- X 0 % of cisatracurium at T 0
- X 6 / 2 6 % of cisatracurium at after 6 or 26 hours.
- This example demonstrates a method for purification of the cisatracurium solution from the buffer's mixture by Solid Phase Extraction (SPE).
- SPE Solid Phase Extraction
- Eluent A 2OmM NaNO 3 aqueous solution, pH adjusted to 2.0 with HNO 3
- Eluent B methanol.
- the gradient was as described in Table 3, and the detection was at 280 nm.
- the flow rate was 14 ml/min and the cistracurium besylate was isolated from the (lR,rR)-atracurium besylate mixture and analyzed using an HPLC system.
- the Fractions were combined correspondingly to the lR-cis,l'R-cis isomer content, as detailed in Table 15.
- the organic phases were collected, dried with MgSO 4 and evaporated to dryness to afford residual semi-solid oil (91 mg), which was dissolved in 18 ml water and the pH was adjusted to ⁇ 3 with benzenesulfonic acid.
- the aqueous solution was placed into the freeze dryer (in tree glass vials) for 40 hours.
- the aqueous solution was lyophilized to afford 72 mg of cisatracurium besylate in 60% yield, having purity of 96.3% (by HPLC).
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Abstract
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Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0808581-1A BRPI0808581A2 (en) | 2007-03-26 | 2008-03-05 | "METHOD FOR SEPARATING HIGH PURITY CISATRACURY FROM A MIXTURE OF (1R, 1'R) - ATTRACURIUM ISOMERS" |
AU2008231470A AU2008231470A1 (en) | 2007-03-26 | 2008-03-05 | (1R,1'R)-atracurium salts separation process |
EP08719916A EP2125743A1 (en) | 2007-03-26 | 2008-03-05 | (1r,1'r)-atracurium salts separation process |
US12/529,771 US20100087650A1 (en) | 2007-03-26 | 2008-03-05 | (1r,1'r)-atracurium salts separation process |
CA002681060A CA2681060A1 (en) | 2007-03-26 | 2008-03-05 | (1r,1'r)-atracurium salts separation process |
IL200782A IL200782A0 (en) | 2007-03-26 | 2009-09-07 | (1 r,1'r)-atracurium salts separation process |
Applications Claiming Priority (2)
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US90808807P | 2007-03-26 | 2007-03-26 | |
US60/908,088 | 2007-03-26 |
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WO2008117271A1 true WO2008117271A1 (en) | 2008-10-02 |
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PCT/IL2008/000291 WO2008117271A1 (en) | 2007-03-26 | 2008-03-05 | (1r,1'r)-atracurium salts separation process |
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US (1) | US20100087650A1 (en) |
EP (1) | EP2125743A1 (en) |
AU (1) | AU2008231470A1 (en) |
BR (1) | BRPI0808581A2 (en) |
CA (1) | CA2681060A1 (en) |
WO (1) | WO2008117271A1 (en) |
Cited By (6)
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US8293912B2 (en) | 2007-05-01 | 2012-10-23 | Chemagis Ltd. | Process for producing cisatracurium compounds and associated intermediates |
US8354537B2 (en) | 2007-10-29 | 2013-01-15 | Chemagis Ltd. | R,R1-atracurium salts |
US8357805B2 (en) | 2007-06-18 | 2013-01-22 | Chemagis Ltd. | (1R,1′R)-atracurium salts separation process |
US8357807B2 (en) | 2007-05-01 | 2013-01-22 | Chemagis Ltd. | Isoquinolinium compounds useful in the preparation of cisatracurium and associated intermediates |
US8461338B2 (en) | 2007-03-08 | 2013-06-11 | Chemagis Ltd. | (1R, 1′R)-atracurium salts separation process |
CN104292161A (en) * | 2014-09-19 | 2015-01-21 | 大道隆达(北京)医药科技发展有限公司 | Refinement method of cisatracurium besylate |
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AU2009241211A1 (en) * | 2008-05-01 | 2009-11-05 | Chemagis Ltd. | Cisatracurium derivatives, preparation and uses thereof |
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- 2008-03-05 EP EP08719916A patent/EP2125743A1/en not_active Withdrawn
- 2008-03-05 US US12/529,771 patent/US20100087650A1/en not_active Abandoned
- 2008-03-05 CA CA002681060A patent/CA2681060A1/en not_active Abandoned
- 2008-03-05 BR BRPI0808581-1A patent/BRPI0808581A2/en not_active IP Right Cessation
- 2008-03-05 WO PCT/IL2008/000291 patent/WO2008117271A1/en active Application Filing
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US8461338B2 (en) | 2007-03-08 | 2013-06-11 | Chemagis Ltd. | (1R, 1′R)-atracurium salts separation process |
US8293912B2 (en) | 2007-05-01 | 2012-10-23 | Chemagis Ltd. | Process for producing cisatracurium compounds and associated intermediates |
US8357807B2 (en) | 2007-05-01 | 2013-01-22 | Chemagis Ltd. | Isoquinolinium compounds useful in the preparation of cisatracurium and associated intermediates |
US8357805B2 (en) | 2007-06-18 | 2013-01-22 | Chemagis Ltd. | (1R,1′R)-atracurium salts separation process |
US8354537B2 (en) | 2007-10-29 | 2013-01-15 | Chemagis Ltd. | R,R1-atracurium salts |
CN104292161A (en) * | 2014-09-19 | 2015-01-21 | 大道隆达(北京)医药科技发展有限公司 | Refinement method of cisatracurium besylate |
CN104292161B (en) * | 2014-09-19 | 2016-06-22 | 大道隆达(北京)医药科技发展有限公司 | A kind of process for purification along atracurium besilate |
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BRPI0808581A2 (en) | 2014-09-16 |
EP2125743A1 (en) | 2009-12-02 |
US20100087650A1 (en) | 2010-04-08 |
CA2681060A1 (en) | 2008-10-02 |
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