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ORGANIC SPECTROSCOPY

Read all about Organic Spectroscopy on ORGANIC SPECTROSCOPY INTERNATIONAL 

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DR ANTHONY MELVIN CRASTO Ph.D

DR ANTHONY MELVIN CRASTO Ph.D

DR ANTHONY MELVIN CRASTO, Born in Mumbai in 1964 and graduated from Mumbai University, Completed his Ph.D from ICT, 1991,Matunga, Mumbai, India, in Organic Chemistry, The thesis topic was Synthesis of Novel Pyrethroid Analogues, Currently he is working with AFRICURE PHARMA, ROW2TECH, NIPER-G, Department of Pharmaceuticals, Ministry of Chemicals and Fertilizers, Govt. of India as ADVISOR, earlier assignment was with GLENMARK LIFE SCIENCES LTD, as CONSUlTANT, Retired from GLENMARK in Jan2022 Research Centre as Principal Scientist, Process Research (bulk actives) at Mahape, Navi Mumbai, India. Total Industry exp 32 plus yrs, Prior to joining Glenmark, he has worked with major multinationals like Hoechst Marion Roussel, now Sanofi, Searle India Ltd, now RPG lifesciences, etc. He has worked with notable scientists like Dr K Nagarajan, Dr Ralph Stapel, Prof S Seshadri, etc, He did custom synthesis for major multinationals in his career like BASF, Novartis, Sanofi, etc., He has worked in Discovery, Natural products, Bulk drugs, Generics, Intermediates, Fine chemicals, Neutraceuticals, GMP, Scaleups, etc, he is now helping millions, has 9 million plus hits on Google on all Organic chemistry websites. His friends call him Open superstar worlddrugtracker. His New Drug Approvals, Green Chemistry International, All about drugs, Eurekamoments, Organic spectroscopy international, etc in organic chemistry are some most read blogs He has hands on experience in initiation and developing novel routes for drug molecules and implementation them on commercial scale over a 32 PLUS year tenure till date Feb 2023, Around 35 plus products in his career. He has good knowledge of IPM, GMP, Regulatory aspects, he has several International patents published worldwide . He has good proficiency in Technology transfer, Spectroscopy, Stereochemistry, Synthesis, Polymorphism etc., He suffered a paralytic stroke/ Acute Transverse mylitis in Dec 2007 and is 90 %Paralysed, He is bound to a wheelchair, this seems to have injected feul in him to help chemists all around the world, he is more active than before and is pushing boundaries, He has 100 million plus hits on Google, 2.5 lakh plus connections on all networking sites, 100 Lakh plus views on dozen plus blogs, 227 countries, 7 continents, He makes himself available to all, contact him on +91 9323115463, email amcrasto@gmail.com, Twitter, @amcrasto , He lives and will die for his family, 90% paralysis cannot kill his soul., Notably he has 38 lakh plus views on New Drug Approvals Blog in 227 countries......https://newdrugapprovals.wordpress.com/ , He appreciates the help he gets from one and all, Friends, Family, Glenmark, Readers, Wellwishers, Doctors, Drug authorities, His Contacts, Physiotherapist, etc He has total of 32 International and Indian awards

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Practical Process Research and development; Development..Optimizing the Reaction by Minimizing Impurities


 

Chapter 8 – Optimizing the Reaction by Minimizing Impurities

  • Process Solutions L.L.C., Nicasio, California

The goals of process optimization change with the successful development of a project from early process research through scale-up into dedicated manufacturing. This general order of optimization may differ according to the nature of the process being considered; for instance, a process generating an inordinate amount of waste may be optimized to decrease waste before scaling up to the pilot plant. The initial goal of all process research and development is to maximize the amount of product generated under the reaction conditions. This is done by driving the reaction to completion, that is, by consuming any starting material that is charged in limiting amounts and by generating product with a minimal amount of by-products. Once the in-process yield has been optimized, the maximum yield of isolated product is expected. Rapid optimization is possible by judiciously changing solvents, reagents, catalysts, and ligands; investigations in this area allow the chemist considerable room for creativity and simplifying a process. Such changes may generate different impurities in the isolated intermediates, and it may be necessary to examine the tolerance of subsequent processes for the new impurities.

I consult to the pharmaceutical and fine chemical industries on developing and trouble-shooting processes to efficiently prepare drug substances and intermediates on large scale.  Anticipating and avoiding problems are key for effective and efficient scale-up.  For 17 years I have been consulting and presenting short courses internationally on process chemistry R & D for “small molecules” (over 1400 participants from more than 160 companies).  Prior to consulting I worked at Bristol-Myers Squibb for 17 years.  During that time I had extensive hands-on experience with chemical process development in the lab, pilot plant, and manufacturing sites, including 12 manufacturing start-ups and process development for four major drugs and many new drug candidates.  I wrote Practical Process Research & Development (Academic Press, 2000; 2nd edition 2012).

Practical Process Research & Development describes the development of chemical processes for the pharmaceutical and fine chemicals industries.  It provides a comprehensive, step-by-step approach to process R & D, and it is designed for those who want insights into generating rugged, practical, cost-effective processes.  Guidelines for industrial process R & D are rarely taught in academia, although this book has been used as a textbook.  It is primarily used by those in industry.

The second edition updates the first edition and includes topics not covered in the first editionPPR&D 2nd ed Japanese cover, such as genotoxins, biocatalysis, green solvents, predicting effective solvent combinations, and process validation.  Almost 85% of the references cited were published after the first edition was published, and virtually all examples in the Figures are new.  Trevor Laird kindly wrote a forward for this edition.

The second edition has been translated into Japanese and graced with a handsome cover.  Noriaki Murase was the translation supervisor, and the translators were Shohei Imachi, Koreaki Imura, Dai Tatsuta, Taro Tsukude, Toyoharu Numata, Yujiro Furuya, Akira Manaka, and Noriaki Murase. Sayaka Nukatsuka was the editor. I am very grateful to these people for their hard work to translate my book.

I am grateful to Barry Sharpless and Jerry Moniot for writing forwards to the first edition  I am also grateful to the following people for their translations of the first edition of my book.  Noriaki Murase, Yoshinori Murata, Toyoharu Numata, Mio Sakai, and Tatsuo Ueki translated Practical Process Research & Development into Japanese.  Kwang-Hyun Ahn, Yeung-Ho Park, and Sung-Kwan Hwang  translated Practical Process Research & Development into Korean.  Zhinong Gao and Wenhao Hu translated Practical Process Research & Development into Chinese.


 

In the foreword to Neal Anderson’s second edition of Practical process research and development, Trevor Laird states that, in his opinion, this is the best book on process chemistry. Having just co-edited a book with similar subject matter, I agree that this is one of the best available, and would add that it is an exceptionally clear, well written and researched book. This edition is also special for its chronological flow from discovery to production. The author achieves this by having a good understanding of the subject from the process chemist perspective, though consequently the complementary area of process engineering is less well covered.
The book communicates the excitement of this highly creative subject, but also the responsibility that lies with every process development job. This is a timely update with discussions covering contemporary issues such as product safety, process waste, catalysis, continuous operations, optimisation and validation. The updated introduction has a fascinating discussion of recent events that are shaping the direction of the pharma industry. And new chapters on Process safety, Effects of water, Organometallic reactions and Work-up are highly pertinent and will be recognised by all those involved in process development day-to-day. I like the fact that green chemistry and chirality are woven into chapters, reflecting their status within the field.
The book is packed with useful facts and information making it very dense, yet its structure makes it easy to read and find them. Many of the figures and schemes provide contemporary illustrative examples, and the use of text boxes to highlight key facts facilitates browsing. I already recommend the first edition as essential reading to process chemistry and engineering students and academic staff, and am certain this second edition will rapidly establish itself with this audience and those in the wider process chemical industry. Congratulations to Anderson, and thank you; the hard work that has clearly gone into this book has been very worthwhile.
free look
Below my own thoughts of process chemist
  • Evaluate the existing synthesis and identify steps, or sequences in the route that may pose a problem for large scale synthesis
  • Propose alternatives to any problematic steps or sequences and then implement these alternatives bases upon laboratory experimentation using Ph.D. level chemists with process research expertise
  • Ensure the synthesis is suitable for the immediate needs of the project, which maybe for only a few kilograms of API
  • Ensure the synthesis is suitable for long term, large scale manufacturing
  • Optimize reagent charges, operating temperatures, concentrations, work-up conditions and volumes, and solvent use in general
  • Identify which steps can be combined to result in a “through process” and implement the through process
  • Optimize purification schemes by identifying key crystalline intermediates and remove chromatographies from the synthesis
  • Optimize recrystallization parameters to ensure consistently high purity with similar impurity profiles from batch to batch, with low mother liquor losses
  • Institute appropriate analytical controls for in-process assays, end of reaction specifications, and acceptable intermediate or API purity
  • The process research team works closely with the analytical team to integrate the chemistry and analytical controls into the process at an early stage of the development cycle. The process research is then documented into a JACS style development report that outlines the chemistry and synthetic approaches that were tried as part of the synthetic development effort. This development report also includes a detailed experimental with supporting analytical data for the successful chemistry that results from our effort.The experimental that is part of these development reports is much more detailed than any journal publication. When coupled with our analytical and cGMP capabilities, the process research we provide is an essential groundwork for any compound that is just advancing from nomination at the discovery phase into clinical trial development. The process we develop provides the foundation of the ultimate manufacturing process, and should not need any changes (at a later date), to the synthetic strategy or bond forming steps used to prepare the API.

Critical Assessment of Pharmaceutical Processes, A Rationale for Changing the Synthetic Route


Changing the Synthetic Route - Chemical Reviews  ACS Publications -    --

Critical Assessment of Pharmaceutical ProcessesA Rationale for Changing the Synthetic Route

AstraZeneca, Process R&D, Avlon/Charnwood, Avlon Works, Severn Road, Hallen, Bristol BS10 7ZE, U.K., GlaxoSmithKline, Synthetic Chemistry, Old Powder Mills, Tonbridge, Kent TN11 9AN, U.K., and Pfizer, Chemical R&D, PGR&D, Ramsgate Road, Sandwich, Kent CT13 9NJ, U.K.
Chem. Rev., 2006, 106 (7), pp 3002–3027
DOI: 10.1021/cr050982w
Publication Date (Web): March 8, 2006

Table of Contents

  • 1. Introduction
  • 2. Criteria for Process Assessment
    • 2.1. Safety Issues2.1.1. Potential Safety Issues and Their Significance
  • 2.1.2. Prediction and Assessment of Safety Issues
  • 2.1.3. Options To Manage Safety Issues
  • 2.1.4. Designing a Safer New Route
    • 2.2. Environmental Issues
  • 2.2.1. Potential Environmental Issues and Their Significance
  • 2.2.2. Prediction and Assessment of Environmental Issues
  • 2.2.3. Options To Manage Environmental Issues
  • 2.2.4. Designing a New “Greener” Route
    • 2.3. Legal Issues
  • 2.3.1. Potential Legal Issues and Their Significance
  • 2.3.2. Prediction and Assessment of Legal Issues Associated with Regulated Substances
  • 2.3.3. Prediction and Assessment of Legal Issues Associated with Patent Infringement
  • 2.3.4. Options To Manage Patent Issues
  • 2.3.5. Designing a New Route with Freedom To Operate
    • 2.4. Economic Issues
  • 2.4.1. Potential Economic Issues and Their Significance
  • 2.4.2. Prediction and Assessment of Economic Issues
  • 2.4.3. Options To Manage Economic Issues
  • 2.4.4. Designing a Cost-Effective New Route
    • 2.5. Control Issues
  • 2.5.1. Potential Control Issues and Their Significance
  • 2.5.2. Prediction and Assessment of Control Issues
  • 2.5.3. Options To Manage Control Issues
  • 2.5.4. Designing a New Route with Adequate Control Measures
    • 2.6. Throughput Issues
  • 2.6.1. Potential Throughput Issues and Their Significance
  • 2.6.2. Prediction and Assessment of Throughput Issues
  • 2.6.3. Options To Manage Throughput Issues
  • 2.6.4. Designing a New Route with High Throughput
  • 3. Interrelationships between Process Issues
  • 4. Conclusions
  • 5. Acknowledgments
  • 6. References

Pemirolast


Pemirolast.png

Pemirolast (INN) is a mast cell stabilizer used as an anti-allergic drug therapy. It is marketed under the tradenames Alegysal and Alamast.

9-methyl-3-(1H-tetrazol-5-yl)-4H-pyrido-[1, 2-a]-pyrimidin-4-one

It has also been studied for the treatment of asthma.

https://www.google.com/patents/US9006431

Pemirolast is an orally-active anti-allergic drug which is used in the treatment of conditions such as asthma, allergic rhinitis and conjunctivitis. See, for example, U.S. Pat. No. 4,122,274, European Patent Applications EP 316 174 and EP 1 285 921, Yanagihara et al, Japanese Journal of Pharmacology, 51, 93 (1989) and Drugs of Today, 28, 29 (1992). The drug is presently marketed in e.g. Japan as the potassium salt under the trademark ALEGYSAL™.

Commercial pemirolast potassium has the disadvantage that it is known to give rise to sharp plasma concentration peaks in humans (see, for example, Kinbara et al, “Plasma Level and Urinary Excretion of TBX in Humans”, Japanese Pharmacology & Therapeutics, 18(3) (1990), and “Antiallergic agent—ALEGYSAL tablet 5 mg—ALEGYSAL tablet 10 mg—ALEGYSAL dry syrup”, Pharmaceutical Interview Form (IF), Revised in October 2007 (7th version), Standard Commodity Classification No.: 87449). The latter document also reports that the potassium salt of pemirolast is hygroscopic, which is believed to give rise to chemical instability, and possesses a bitter taste.

U.S. Pat. No. 4,122,274 describes a process for the production of salts of pemirolast, including potassium salts and (at Example 14) a sodium salt. As described herein, this technique produces a sodium salt that is physically unstable. Sodium salts of pemirolast are also mentioned (but a synthesis thereof not described) in international patent applications WO 2008/074975 and WO 2008/075028.

COMPARATIVE EXAMPLE 5Recrystallisation of Pemirolast Sodium According to the Method of U.S. Pat. No. 4,122,274

In U.S. Pat. No. 4,122,274, it is stated that the crude title product (pemirolast sodium) was recrystallised from water:ethanol to give pure title product. It is not clear from this level of detail what the ratio of water:ethanol employed was, so several experiments were performed with a view to reproducing the prior art technique.

  • (i) Crude sodium salt of pemirolast (480 mg; from Example 4, method (I) above) was recrystallised from water and ethanol (95%) in a 1:1 ratio. The Na salt of pemirolast (480 mg, 1.92 mmol) was dissolved in H2O (8 mL) at 70° C. and EtOH 95% (8 mL) was added. The clear solution was allowed to reach room temperature and the solid material formed was filtered off, washed with a small amount of ethanol and dried in vacuum to give 316 mg of pure sodium salt.
  • (ii) Crude sodium salt of pemirolast (500 mg; from Example 4, method (II) above) was dissolved in water (4.9 mL) at 70° C. Thereafter EtOH 95% (ca. 4.0 mL) was added at 70° C. until a solid started to form. Another 0.1 mL of water was added to get everything into solution. The solid material formed upon cooling was collected by filtration and dried under vacuum to give 348 mg of pure sodium salt.
  • (iii) Crude sodium salt of pemirolast (300 mg; from Example 4, method (II) above) was recrystallised from water:ethanol (1:1 ratio; 10 mL) at 70° C. The solid material formed upon cooling was collected by filtration and dried under vacuum to give 174 mg of pure sodium salt.
  • (iv) Crude sodium salt of pemirolast (300 mg; from Example 4, method (II) above) was recrystallised from water:ethanol (9:1 ratio, 4 mL) at 70° C. The solid material formed upon cooling was collected by filtration and dried under vacuum to give 219 mg of pure sodium salt.

All four samples of pure pemirolast sodium salt had the same physico-chemical properties (Raman spectra and NMR):

1H NMR (D2O) δ: 8.86-8.80 (m, 1H, CH), 8.57 (s, 1H, CH), 7.68-7.59 (m, 1H, CH), 7.22-7.13 (m, 1H, CH), 2.39 (s, 3H, CH3).

The PXRD pattern (measured in respect of Example 5(i) above) is shown in FIG. 3. It was concluded from this that this form of the sodium salt is an amorphous material mixed with a crystalline fraction.

The Raman spectrum was recorded directly after recrystallisation. All samples were then stored under ambient conditions on a shelf in a fume hood. About a month later, a Raman spectrum was recorded, which was significantly different to that recorded earlier. This is shown in FIG. 4, where the lower spectrum accords to the earlier measurement and the upper spectrum accords to the later measurement. In the light of these results, it was concluded that the prior art amorphous form of pemirolast sodium is physically unstable.

The amorphous material was also prepared by drying of the form obtained in accordance with Example 11 below at 40° C. and reduced pressure for 40 hours to yield 12 g of a pale yellow cotton-like amorphous solid.

………………………..

http://www.lookchem.com/Chempedia/Chemical-Technology/Organic-Chemical-Technology/18815.html

1) Firstly, 2-Amino-3-methylpyridine (I) is condensed with ethoxymethylenemalonodinitrile (II) to afford the monocyclic intermediate (III), which is in tautomeric equilibrium with the pyridopyrimidine derivative (IV). Next, the reaction of (IV) with aluminum azide (AlCl3.NaN3) in refluxing THF yields 4-imino-9-methyl-3-(1H-tetrazol-5-yl)-4H-pyrido[1,2-a]pyrimidine (V). Finally, this compound is first hydrolyzed with 1N HCl and then treated with KOH.
2) Compound (IV) can be converted to the final product by a one-pot reaction: (VI) is treated first with NaN3 in refluxing acetic acid, then hydrolyzed with HCl and finally treated with KOH.

………….

EXAMPLE 1

A suspension of 9-methyl-3-(1 H-tetrazol-5-yl)-4H-pyrido-[1,2-a]-pyrimidin-4-one (68.5 g; 0.3 mols) in methanol (420 ml) and water (210 ml) heated at 50° C. is added with a 40% N-methylamine aqueous solution (30 ml, 0.35 mols) to pH=10. The solution is heated at 68-70° C., and acidified with formic acid (21 ml) to pH=3. After completion of the addition the mixture is kept at 68-70° C. for about 15 minutes and then cooled to 20-25° C. The precipitate is filtered, washed with methanol and dried under vacuum at 40° C. to give 9-methyl-3-(1 H-tetrazol-5-yl)-4H-pyrido-[1,2-a]-pyrimidin-4-one with >99.8% HPLC purity (63 g, 92% yield).

EXAMPLE 2

9-Methyl-3-(1 H-tetrazol-5-yl)-4H-pyrido-[1,2-a]-pyrimidin-4-one (63 g, 0.28 mols) is suspended in methanol (1000 ml). The resulting suspension is kept at 45° C. and slowly added with a 45% potassium hydroxide aqueous solution to pH 9-9.5. The suspension is stirred at 45° C. for about 15 minutes and then cooled to 20° C. The precipitate is filtered, washed with methanol and dried under vacuum at 80° C., to obtain Pemirolast Potassium (71.9 g; 0.27 mols, 96% yield) with HPLC purity >99.8%. 1H NMR(D2O, TMS) d (ppm): 2.02 (s, 3H); 6.83 (t, 1H); 7.22 (d, 1H); 8.18 (s, 1H); 8.47 (d, 1H).

References

  • Tinkelman DG, Berkowitz RB (February 1991). “A pilot study of pemirolast in patients with seasonal allergic rhinitis”. Ann Allergy 66 (2): 162–5. PMID 1994787.
  • Kawashima T, Iwamoto I, Nakagawa N, Tomioka H, Yoshida S (1994). “Inhibitory effect of pemirolast, a novel antiallergic drug, on leukotriene C4 and granule protein release from human eosinophils”. Int. Arch. Allergy Immunol. 103 (4): 405–9. doi:10.1159/000236662. PMID 8130655.
  • Abelson MB, Berdy GJ, Mundorf T, Amdahl LD, Graves AL (October 2002). “Pemirolast potassium 0.1% ophthalmic solution is an effective treatment for allergic conjunctivitis: a pooled analysis of two prospective, randomized, double-masked, placebo-controlled, phase III studies”. J Ocul Pharmacol Ther 18 (5): 475–88. doi:10.1089/10807680260362759. PMID 12419098.
  • Kemp JP, Bernstein IL, Bierman CW et al. (June 1992). “Pemirolast, a new oral nonbronchodilator drug for chronic asthma”. Ann Allergy 68 (6): 488–91. PMID 1610024.
Pemirolast
Pemirolast.png
Systematic (IUPAC) name
9-methyl-3-(1H-tetrazol-5-yl)-4H-pyrido[1,2-a]pyrimidin-4-one
Clinical data
Trade names Alamast
AHFS/Drugs.com monograph
Pregnancy
category
  • US: C (Risk not ruled out)
Legal status
  • (Prescription only)
Routes of
administration
Oral, ophthalmic
Identifiers
CAS Registry Number 69372-19-6 Yes
ATC code None
PubChem CID: 57697
IUPHAR/BPS 7329
DrugBank DB00885 
ChemSpider 51990 
UNII 2C09NV773M 
KEGG D07476 Yes
ChEMBL CHEMBL1201198 
Chemical data
Formula C10H8N6O
Molecular mass 228.21 g/mol
US4122274 * May 25, 1977 Oct 24, 1978 Bristol-Myers Company 3-Tetrazolo-5,6,7,8-substituted-pyrido[1,2-a]pyrimidin-4-ones
EP0316174A1 Nov 10, 1988 May 17, 1989 Tokyo Tanabe Company Limited Aqueous preparation of 9-methyl-3-(1H-tetrazol-5-yl)-4H-Pyrido[1,2-a]pyrimidin-4-one potassium salt
EP1285921A1 Jun 25, 2002 Feb 26, 2003 Dinamite Dipharma S.p.A. A process for the preparation of high purity pemirolast
JPH0374385A Title not available
WO2008074975A1 Nov 16, 2007 Jun 26, 2008 Cardoz Ab New combination for use in the treatment of inflammatory disorders
WO2008075028A1 Dec 18, 2007 Jun 26, 2008 Cardoz Ab New combination for use in the treatment of inflammatory disorders
US4122274 May 25, 1977 Oct 24, 1978 Bristol-Myers Company 3-Tetrazolo-5,6,7,8-substituted-pyrido[1,2-a]pyrimidin-4-ones
US5254688 * Jun 19, 1991 Oct 19, 1993 Wako Pure Chemical Industries, Ltd. Process for producing pyrido[1,2-a]pyrimidine derivative
DE243821C Title not available
EP0462834A1 Jun 20, 1991 Dec 27, 1991 Wako Pure Chemical Industries, Ltd Process for producing pyrido [1,2-a]pyrimidine derivative
WO1993025557A1 Jun 7, 1993 Dec 23, 1993 Smithkline Beecham Plc Process for the preparation of clavulanic acid

Pemirolast Potassium (BMY 26517) cas100299-08-9is a histamine H1 antagonist and mast cell stabilizer that acts as an antiallergic agent.
Target: Histamine H1 Receptor
Pemirolast potassium (BMY 26517) is a new oral, nonbronchodilator antiallergy medication that is being evaluated for the therapy of asthma [1]. Pemirolast potassium (BMY 26517) inhibits chemical mediator release from tissue mast cells and is also shown to inhibit the release of peptides including substance P, Pemirolast potassium (BMY 26517) reduces kaolin intake by inhibition of substance P release in rats [2]. Pemirolast potently attenuates paclitaxel hypersensitivity reactions through inhibition of the release of sensory neuropeptides in rats [3]. Pemirolast potassium is used for the treatment of allergic conjunctivitis and prophylaxis for pulmonary hypersensitivity reactions to drugs such as paclitaxel [4].

Molecular formula: C10H7KN6O

Molecular Weight: 266.30

External links

Necessity of Establishing Chemical Integrity of Polymorphs of Drug Substance Using a Combination of NMR, HPLC, Elemental Analysis, and Solid-State Characterization Techniques: Case Studies


Abstract Image

Necessity of Establishing Chemical Integrity of Polymorphs of Drug Substance Using a Combination of NMR, HPLC, Elemental Analysis, and Solid-State Characterization Techniques: Case Studies

Chemical Process Research Laboratory, USV Limited, Arvind Vithal Gandhi Chowk, BSD Marg, Govandi, Mumbai – 400 088, India
Org. Process Res. Dev., 2013, 17 (3), pp 519–532
DOI: 10.1021/op300229k
Polymorphism is a solid-state phenomenon; hence, solid-state techniques such as XRPD, DSC, and FT-IR are used for characterization. Many a time, only XRPD is used. These techniques ignore the most important aspects, i.e., chemical purity and the chemical integrity of the polymorph, which can be confirmed by techniques such as 1H NMR, HPLC, and elemental analysis. The aim of this article is to emphasize how techniques such as 1H NMR, elemental analysis, and HPLC purity in addition to other solid-state characterization techniques would help to prove that the drug really exists in different polymorphic forms. H1NMR, HPLC, and elemental analysis reveal the formation of different compounds and not polymorphs in the case of pioglitazone·HCl and glyburide. In the cases of irbesartan and ropinirole·HCl use of a single solid-state characterization technique such as XRPD is not enough for establishing the existence of different polymorphic forms.

Moexipril


Moexipril2DACS.svg

Moexipril

Moexipril
CAS 103775-10-6
(3S)-2-[(2S)-2-[[(1S)-1-(Ethoxycarbonyl)-3-phenylpropyl]amino]-1-oxopropyl]-1,2,3,4-tetrahydro-6,7-dimethoxy-3-isoquinolinecarboxylic acid
Manufacturers’ Codes: RS-10085
CI-925
RS-10085-197
SPM-925
RS-10085 (free base)
Molecular Formula: C27H34N2O7
Molecular Weight: 498.57
Percent Composition: C 65.04%, H 6.87%, N 5.62%, O 22.46%
Literature References: Angiotensin converting enzyme (ACE) inhibitor; dimethoxy analog of quinapril, q.v. Prepn: M. L. Hoefle, S. Klutchko, EP 49605eidem, US 4344949 (both 1982 to Warner-Lambert); S. Klutchko et al., J. Med. Chem. 29, 1953 (1986). Pharmacology: O. Edling et al., J. Pharmacol. Exp. Ther. 275, 854 (1995). GC-MS determn in plasma: W. Hammes et al., J. Chromatogr. B 670, 81 (1995). Clinical trials in hypertension: W. B. White et al., J. Hum. Hypertens. 8, 917 (1994); M. Stimpel et al., Cardiology 87, 313 (1996).
 
Derivative Type: Hydrochloride
CAS Registry Number: 82586-52-5
Manufacturers’ Codes: CI-925; RS-10085-197; SPM-925
Trademarks: Fempress (Schwarz); Perdix (Schwarz); Univasc (Schwarz)
Molecular Formula: C27H34N2O7.HCl
Molecular Weight: 535.03
Percent Composition: C 60.61%, H 6.59%, N 5.24%, O 20.93%, Cl 6.63%
Properties: Crystals from ethanol + ethyl ether, mp 141-161°. [a]D23 +34.2° (c = 1.1 in ethanol).
Melting point: mp 141-161°
Optical Rotation: [a]D23 +34.2° (c = 1.1 in ethanol)
Derivative Type: Diacid hydrochloride
CAS Registry Number: 82586-57-0
Additional Names: Moexiprilat hydrochloride
Molecular Formula: C25H30N2O7.HCl
Molecular Weight: 506.98
Percent Composition: C 59.23%, H 6.16%, N 5.53%, O 22.09%, Cl 6.99%
Properties: Prepd as the monohydrate; crystals from THF + ethanol, mp 145-170°. [a]D23 +37.8° (c = 1.1 in methanol).
Melting point: mp 145-170°
Optical Rotation: [a]D23 +37.8° (c = 1.1 in methanol)
Therap-Cat: Antihypertensive.
Keywords: ACE-Inhibitor; Antihypertensive; N-Carboxyalkyl (peptide/lactam) Derivatives.
Moexipril hydrochloride is a potent orally active nonsulfhydryl angiotensin converting enzyme inhibitor (ACE inhibitor)[1] which is used for the treatment of hypertension and congestive heart failure. Moexipril can be administered alone or with otherantihypertensives or diuretics.[2] It works by inhibiting the conversion of angiotensin I to angiotensin II.[3] Moexipril is available from Schwarz’Pharma under the trade name Univasc.[3][4]
Originally developed at Pfizer (formerly Warner-Lambert), moexipril hydrochloride was licensed to Schwarz Pharma at the end of 1989, when it was still a phase II clinical development project. Manufacturing rights to the drug were subsequently licensed to Orgamol (acquired by BASF in 2005) in Switzerland. Bayer currently distributes the product in Italy, and Hanmi has launched it in the Republic of Korea.

Pharmacology

Moexipril is available as a prodrug moexipril hydrochloride, and is metabolized in the liver to form the pharmacologically active compound moexiprilat. Formation of moexiprilat is caused by hydrolysis of an ethyl ester group.[5] Moexipril is incompletely absorbed after oral administration, and its bioavailability is low.[6] The long pharmacokinetic half-life and persistent ACE inhibition of moexipril allows once-daily administration.[7]

Moexipril is highly lipophilic,[2] and is in the same hydrophobic range as quinapril, benazepril, and ramipril.[7] Lipophilic ACE inhibitors are able to penetrate membranes more readily, thus tissue ACE may be a target in addition to plasma ACE. A significant reduction in tissue ACE (lung, myocardium, aorta, and kidney) activity has been shown after moexipril use.[8]

It has additional PDE4-inhibiting effects.[9]

Side effects

Moexipril is generally well tolerated in elderly patients with hypertension.[10] Hypotension, dizziness, increased cough, diarrhea, flu syndrome, fatigue, and flushing have been found to affect less than 6% of patients who were prescribed moexipril.[3][10]

Mechanism of action

As an ACE inhibitor, moexipril causes a decrease in ACE. This blocks the conversion of angiotensin I to angiotensin II. Blockage of angiotensin II limits hypertension within the vasculature. Additionally, moexipril has been found to possess cardioprotective properties. Rats given moexipril one week prior to induction of myocardial infarction, displayed decreased infarct size.[11] The cardioprotective effects of ACE inhibitors are mediated through a combination of angiotensin II inhibition and bradykininproliferation.[8][12] Increased levels of bradykinin stimulate in the production of prostaglandin E2[13] and nitric oxide,[12] which cause vasodilation and continue to exert antiproliferative effects.[8] Inhibition of angiotensin II by moexipril decreases remodeling effects on the cardiovascular system. Indirectly, angiotensin II stimulates of the production of endothelin 1 and 3 (ET1, ET3)[14] and the transforming growth factor beta-1 (TGF-β1),[15] all of which have tissue proliferative effects that are blocked by the actions of moexipril. The antiproliferative effects of moexipril have also been demonstrated by in vitro studies where moexipril inhibits the estrogen-stimulated growth of neonatal cardiac fibroblasts in rats.[12] Other ACE inhibitors have also been found to produce these actions, as well.

WO 2014202659

http://www.google.com/patents/WO2014202659A1?cl=en

US4344949

http://www.google.co.in/patents/US4344949

References

  1.  Hochadel, Maryanne, ed. (2006). The AARP Guide to Pills. Sterling Publishing Company. p. 640. ISBN 978-1-4027-1740-6. Retrieved2009-10-09.
  2.  Belal, F.F, K.M. Metwaly, and S.M. Amer. “Development of Membrane Electrodes for the Specific Determination of Moexipril Hydrochloride in Dosage Forms and Biological Fluids.” Portugaliae Electrochimica Acta. 27.4 (2009): 463-475.
  3.  Rodgers, Katie, Michael C Vinson, and Marvin W Davis. “Breakthroughs: New drug approvals of 1995 — part 1.” Advanstar Communications, Inc. 140.3 (1996): 84.
  4.  Dart, Richard C. (2004). Medical toxicology. Lippincott Williams & Wilkins. p. 647. ISBN 978-0-7817-2845-4. Retrieved 2009-10-09.
  5.  Kalasz, H, G. Petroianu, K. Tekes, I. Klebovich, K. Ludanyi, et al. “Metabolism of moexipril to moexiprilat: determination of in vitro metabolism using HPLC-ES-MS.” Medicinal Chemistry. 3 (2007): 101-106.
  6. Jump up^ Chrysant, George S, PK Nguyen. “Moexipril and left ventricular hypertrophy.” Vascular Health Risk Management. 3.1 (2007): 23-30.
  7.  Cawello W, H. Boekens, J. Waitzinger, et al. “Moexipril shows a long duration of action related to an extended pharmacokinetic half-life and prolonged ACE-inhibition.” Int J Clin Pharmacol Ther. 40 (2002): 9-17.
  8. ^ Jump up to:a b c Chrysant, SG. “Vascular remodeling: the role of angiotensin-converting enzyme inhibitors.” American Heart Journal. 135.2 (1998): 21-30.
  9. Jump up^ Cameron, RT; Coleman, RG; Day, JP; Yalla, KC; Houslay, MD; Adams, DR; Shoichet, BK; Baillie, GS (May 2013). “Chemical informatics uncovers a new role for moexipril as a novel inhibitor of cAMP phosphodiesterase-4 (PDE4)”. Biochemical Pharmacology 85 (9): 1297–1305. doi:10.1016/j.bcp.2013.02.026. PMC 3625111. PMID 23473803.
  10.  White, WB, and M Stimpel. “Long-term safety and efficacy of moexipril alone and in combination with hydrochlorothiazide in elderly patients with hypertension.” Journal of human hypertension. 9.11 (1995): 879-884.
  11. Rosendorff, C. “The Renin-Angiotensin System and Vascular Hypertrophy.” Journal of the American College of Cardiology. 28 (1996): 803-812.
  12.  Hartman, J.C. “The role of bradykinin and nitric oxide in the cardioprotective action of ACE inhibitors.” The Annals of Thoracic Surgery. 60.3 (1995): 789-792.
  13.  Jaiswal, N, DI Diz, MC Chappell, MC Khosia, CM Ferrario. “Stimulation of endothelial cell prostaglandin production by angiotensin peptides. Characterization of receptors.” Hypertension. 19.2 (1992): 49-55.
  14.  Phillips, PA. “Interaction between endothelin and angiotensin II.” Clinical and Experimental Pharmacology and Physiology. 26.7. (1999): 517-518.
  15.  Youn, TJ, HS Kim, BH Oh. “Ventricular remodeling and transforming growth factor-beta 1 mRNA expression after nontransmural myocardial infarction in rats: effects of angiotensin converting enzyme inhibition and angiotensin II type 1 receptor blockade.” Basic research in cardiology. 94.4 (1999): 246-253.

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Systematic (IUPAC) name
(3S)-2-[(2S)-2-{[(2S)-1-ethoxy-1-oxo-4-phenylbutan-2-yl]amino}propanoyl]-6,7-dimethoxy-1,2,3,4-tetrahydroisoquinoline-3-carboxylic acid
Clinical data
Trade names Univasc
AHFS/Drugs.com monograph
MedlinePlus a695018
Pregnancy
category
  • US: D (Evidence of risk)
Legal status
Routes of
administration
Oral
Pharmacokinetic data
Bioavailability 13-22%
Protein binding 90%
Metabolism Hepatic (active metabolite, moexiprilat)
Biological half-life 1 hour; 2-9 hours (active metabolite)
Excretion 50% (faeces), 13% (urine)
Identifiers
CAS Registry Number 103775-10-6 Yes
ATC code C09AA13
PubChem CID: 91270
IUPHAR/BPS 6571
DrugBank DB00691 
ChemSpider 82418 
UNII WT87C52TJZ 
KEGG D08225 Yes
ChEMBL CHEMBL1165 
Chemical data
Formula C27H34N2O7
Molecular mass 498.568 g/mol

9-(5-oxotetrahydrofuran-2-yl)nonanoic acid methyl ester


9-(5-Oxotetrahydrofuran-2-yl)nonanoic acid methyl ester

353
Name 9-(5-Oxotetrahydrofuran-2-yl)nonanoic acid methyl ester
Synonyms
Name in Chemical Abstracts 2-Furannonanoic acid, tetrahydro-5-oxo-, methyl ester
CAS No 22623-86-5
Molecular formula C14H24O4
Molecular mass 256.35
SMILES code O=C1OC(CC1)CCCCCCCCC(=O)OC

1H NMR

1H NMR

1H-NMR: 9-(5-Oxotetrahydrofuran-2-yl)nonanoic acid methyl ester
500 MHz, CDCl3
delta [ppm] mult. atoms assignment
1.24-1.45 m 10 H 4-H, 5-H, 6-H, 7-H, 8-H
1.57 m 2 H 3-H
1.70 m 1 H 9-H
1.82 m 1 H 9-H
2.27 t 2 H 2-H
2.30 m 2 H 3-H (ring)
2.50 m 2 H 4-H (ring)
3.67 s 3 H O-CH3
4.48 m 1 H 2-H (ring)

NMR XXX

13C NMR

13C NMR

13C-NMR: 9-(5-Oxotetrahydrofuran-2-yl)nonanoic acid methyl ester
125.7 MHz, CDCl3
delta [ppm] assignment
24.9 C3
25.2 C9
28.0-29.2 C4, C5, C6, C7, C8, C3 (ring)
34.0 C2
35.5 C4 (ring)
51.4 O-CH3
81.0 C2 (ring)
174.2 C1 (O-C(=O)-)
177.2 C5 (O-C(=O)-, ring)
76.5-77.5 CDCl3

13C XXX

IR

IR

IR: 9-(5-Oxotetrahydrofuran-2-yl)nonanoic acid methyl ester
[Film, T%, cm-1]
[cm-1] assignment
2931, 2856 aliph. C-H valence
1776 C=O valence, lactone
1737 C=O valence, ester
Cu
10-Undecenoic acid methyl esterIodoacetic acid ethyl esterreacts to9-(5-Oxotetrahydrofuran-2-yl)nonanoic acid methyl esterIodoethane

Synthesis of 9-(5-oxotetrahydrofuran-2-yl)nonanoic acid methyl ester

Reaction type: addition to alkenes, radical reaction, ring closure reaction
Substance classes: alkene, halogencarboxylic acid ester, lactone
Techniques: working with cover gas, stirring with magnetic stir bar, heating under reflux, evaporating with rotary evaporator, filtering, recrystallizing, heating with oil bath
Degree of difficulty: Easy

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Operating scheme

Operating schemeInstructions

http://www.oc-praktikum.de/nop/en/instructions/pdf/4005_en.pdf

Instruction (batch scale 100 mmol)

Equipment 250 mL two-neck flask, protective gas supply, reflux condenser, heatable magnetic stirrer, magnetic stir bar, rotary evaporator, Buechner funnel, suction flask, desiccator, oil bath Substances undecenoic acid methyl ester (bp 248 °C) 19.8 g (22.3 mL, 100 mmol) iodoacetic acid ethyl ester (bp 73-74 °C/ 21 hPa) 27.8 g (15.4 mL, 130 mmol) copper powder (finely powdered, >230 mesh ASTM) 30.5 g (480 mmol) tert-butyl methyl ether (bp 55 °C) 130 mL petroleum ether (bp 60-80 °C) 300 mL Reaction In a 250 mL two-neck flask with magnetic stir bar and a reflux condenser connected with a protective gas piping 19.8 g (22.3 mL, 100 mmol) undecenoic acid methyl ester and 27.8 g (15.4 mL, 130 mmol) iodoacetic acid ethyl ester are mixed with 30.5 g (480 mmol) copper powder under a protective gas atmosphere. Afterwards the reaction mixture is stirred at 130 °C oil bath temperature under protective gas for 4 hours. (Reaction monitoring see Analytics.)

Work up The reaction mixture is cooled down to room temperature, 30 mL tert-butyl methyl ether are added, the mixture is stirred for 5 minutes and filtered off. The copper powder on the filter is washed four times with 25 mL tert-butyl methyl ether each. Filtrates and wash solutions are combined, the solvent is evaporated at the rotary evaporator. A yellow oil remains as crude product. Crude yield: 25.4 g.

The crude product is dissolved in 300 mL petroleum ether under reflux. The solution is allowed to cool down to room temperature, then it is stored in the refrigerator over night for complete crystallization. The crystalline product is sucked off over a Buechner funnel and dried in the vacuum desiccator. The mother liquor is stored again in the refrigerator for a check of complete crystallization. Yield: 19.5 g (76.1 mmol, 76%); white solid, mp 34 °C Comments In order to achieve a quantitative reaction within 4 hours, a fivefold excess of copper is used.

Waste management Recycling The copper powder can be used three times.

Waste disposal Waste Disposal evaporated tert-butyl methyl ether (might contain iodoethane) organic solvents, containing halogen mother liquor from recrystallization organic solvents, containing halogen copper powder solid waste, free from mercury, containing heavy metals

Time 6-7 hours

Break After heating and before recrystallizing

Degree of difficulty Easy

Analytics Reaction monitoring with TLC Sample preparation: Using a Pasteur pipette, two drops of the reaction mixture are taken and diluted with 0.5 mL diethyl ether. TLC-conditions: adsorbant: TLC-aluminium foil (silica gel 60) eluent: petroleum ether (60/80) : acetic acid ethyl ester = 7 : 3 visualisation: The TLC-aluminium foil is dipped in 2 N H2SO4 and then dried with a hot air dryer. Reaction monitoring with GC Sample preparation: Using a Pasteur pipette, one drop of the reaction mixture is taken and diluted with 10 mL dichloromethane. From this solution, 0.2 µL are injected. 10 mg from the solid product are dissolved in 10 mL dichloromethane. From this solution, 0.2 µL are injected. GC-conditions: column: DB-1, 28 m, internal diameter 0.32 mm, film 0.25 µm inlet: on-column-injection carrier gas: hydrogen (40 cm/s) oven: 90 °C (5 min), 10 °C/min to 240 °C (40 min) detector: FID, 270 °C Percent concentration was calculated from peak areas.

Chromatogram

crude product chromatogram

GC: crude product
column DB-1, L=28 m, d=0.32 mm, film=0.25 µm
inlet on column injection, 0.2 µL
carrier gas H2, 40 cm/s
oven 90°C (5 min), 10°C/min –> 240°C (40 min)
detector FID, 270°C
integration percent concentration calculated from relative peak area

pure product chromatogram

GC: pure product
column DB-1, L=28 m, d=0.32 mm, film=0.25 µm
inlet on column injection, 0.2 µL
carrier gas H2, 40 cm/s
oven 90°C (5 min), 10°C/min –> 240°C (40 min)
detector FID, 270°C
integration percent concentration calculated from relative peak area

Substances required

Batch scale: 0.01 mol 0.1 mol 10-Undecenoic acid methyl ester
Educts Amount Risk Safety
10-Undecenoic acid methyl ester
19.8 g H- EUH- P-
Iodoacetic acid ethyl ester
GHS06 GHS05 Danger
27.8 g H300 H314 EUH- P264 P280 P305 + 351 + 338 P310
Reagents Amount Risk Safety
Copper powder
GHS09 Warning
30.5 g H400 EUH- P273
Solvents Amount Risk Safety
tert-Butyl methyl ether
GHS02 GHS07 Danger
130 mL H225 H315 P210
Petroleum ether (60-80)
GHS02 GHS08 GHS07 GHS09 Danger
300 mL H225 H304 H315 H336 H411 EUH- P210 P261 P273 P301 + 310 P331
Others Amount Risk Safety
Sulfuric acid 2N
GHS05 Danger
H314 H290 EUH- P280 P301 + 330 + 331 P305 + 351 + 338 P309 + 310
Solvents for analysis Amount Risk Safety
Petroleum ether (60-80)
GHS02 GHS08 GHS07 GHS09 Danger
H225 H304 H315 H336 H411 EUH- P210 P261 P273 P301 + 310 P331
Acetic acid ethyl ester
GHS02 GHS07 Danger
H225 H319 H336 EUH066 P210 P261 P305 + 351 + 338
Dichloromethane
GHS08 GHS07 Warning
H351 H315 H319 H335 H336 H373 P261 P281 P305 + 351 + 338

Substances produced

Batch scale: 0.01 mol 0.1 mol 10-Undecenoic acid methyl ester
Products Amount Risk Safety
9-(5-Oxotetrahydrofuran-2-yl)nonanoic acid methyl ester

Equipment

Batch scale: 0.01 mol 0.1 mol 10-Undecenoic acid methyl ester
two-necked flask 250 mL two-necked flask 250 mL protective gas piping protective gas piping
reflux condenser reflux condenser heatable magnetic stirrer with magnetic stir bar heatable magnetic stirrer with magnetic stir bar
rotary evaporator rotary evaporator suction filter suction filter
suction flask suction flask exsiccator with drying agent exsiccator with drying agent
oil bath oil bath

Simple evaluation indices

Batch scale: 0.01 mol 0.1 mol 10-Undecenoic acid methyl ester
Atom economy 53.9 %
Yield 76 %
Target product mass 19.5 g
Sum of input masses 370 g
Mass efficiency 53 mg/g
Mass index 19 g input / g product
E factor 18 g waste / g product

………………

………

Aseptic Manufacturing Operation: Chinese Company Zhuhai United Laboratories does not comply with EU GMP


DR ANTHONY MELVIN CRASTO Ph.D's avatarDRUG REGULATORY AFFAIRS INTERNATIONAL

see   http://www.gmp-compliance.org/enews_04887_Aseptic-Manufacturing-Operation-Chinese-Company-Zhuhai-United-Laboratories-does-not-comply-with-EU-GMP_9345,S-WKS_n.html

While the focus of attention has been on Indian manufacturers during the last 2 years now also Chinese manufacturers are in the spot light. On 15 June 2015 the National Agency for Medicines and Medical Devices of Romania entered a GMP Non-Compliance Report for Zhuhai United Laboratories into EudraGMDP. Read more about the GMP deviations observed at Zhuhai United.

While the focus of attention has been on Indian manufacturers during the last 2 years now also Chinese manufacturers are again in the spot light. Just recently the EU found serious GMP deviations at an API manufacturer (Huzhou Sunflower Pharmaceuticals) and on 15 June 2015 the National Agency for Medicines and Medical Devices of Romania entered a GMP Non-Compliance Report for Zhuhai United Laboratories Co., LTD located at Sanzao Science &Technology Park, National Hi-Tech Zone, Zhuhai, Guangdong, 519040, China into EudraGMDP.

According to the report issued by the…

View original post 253 more words

Inna Ben-Anat, Global QbD Director of Teva Pharmaceuticals


DR ANTHONY MELVIN CRASTO Ph.D's avatarDRUG REGULATORY AFFAIRS INTERNATIONAL

Meet Inna Ben-Anat, Global QbD Director of Teva Pharmaceuticals. Inna is a key thought leader in Quality by Design for generics.

https://www.linkedin.com/pub/inna-ben-anat/6/47a/670

Ben-Anat, InnaASSOCIATE DIRECTOR, HEAD OF QDD STRATEGY | TEVA PHARMACEUTICALSAssociate Director, Head of QbD Strategy Chemical Engineer with a degree in Quality Assurance and Reliability (Technion-Israel Institute of Technology). QbD Strategy Leader at Teva (USA). Headed the implementation of a global QbD training programme. More than 12 years of pharmaceutical development experience.

Inna Ben-Anat

Inna Ben-Anat is a Quality by Design (QbD) Strategy Leader in Teva Pharmaceuticals USA. In this role, Inna has implemented global QbD training program, and is supporting R&D teams in developing Quality by Design strategies, optimizing formulations and processes and assisting develop product specifications. Additionally, Inna supports Process Engineering group with process optimization during scale-up and supports Operations in identification and resolution of any technical issues. Inna has extensive expertise in process development, design…

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Determining Criticality-Process Parameters and Quality Attributes


DR ANTHONY MELVIN CRASTO Ph.D's avatarDRUG REGULATORY AFFAIRS INTERNATIONAL

Determining Criticality-Process Parameters and Quality Attributes Part I: Criticality as a Continuum

A practical roadmap in three parts that applies scientific knowledge, risk analysis, experimental data, and process monitoring throughout the three phases of the process validation lifecycle.
 

As the pharmaceutical industry tries to embrace the methodologies of quality by design (QbD) provided by the FDA’s process validation (PV) guidance (1) and International Conference on Harmonization (ICH) Q8/Q9/Q10 (2-4), many companies are challenged by the evolving concept of criticality as applied to quality attributes and process parameters. Historically, in biopharmaceutical development, criticality has been a frequently arbitrary categorization between important high-risk attributes or parameters and those that carry little or no risk. This binary designation was usually determined during early development for the purposes of regulatory filings, relying heavily on scientific judgment and limited laboratory studies.

Figure 1: Process validation lifecycle.

With the most recent ICH and FDA guidances…

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Alternative solvents can make preparative liquid chromatography greener


Green Chem., 2015, Advance Article
DOI: 10.1039/C5GC00887E, Paper
Yao Shen, Bo Chen, Teris A. van Beek

Alternative solvents can make preparative liquid chromatography greener

Yao Shen,*ab   Bo Chenb and   Teris A. van Beeka  
*Corresponding authors
aLaboratory of Organic Chemistry, Wageningen University, Dreijenplein 8, 6703 HB Wageningen, The Netherlands
E-mail: lvy33@163.com
bKey Laboratory of Phytochemical R&D of Hunan Province, Hunan Normal University, Changsha, PR China
Greener ethanol, acetone and ethyl acetate provided better chromatographic resolution in preparative RP-HPLC than the traditional methanol, acetonitrile and tetrahydrofuran.

Alternative solvents can make preparative liquid chromatography greener

To make preparative Reversed-Phase High Performance Liquid Chromatography (RP-pHPLC) greener, alternative solvents were considered among others in terms of toxicity, cost, safety, workability, chromatographic selectivity and elution strength. The less toxic solvents ethanol, acetone and ethyl acetate were proposed as possible greener replacements for methanol, acetonitrile and tetrahydrofuran (THF).

For testing their feasibility, five ginkgo terpene trilactones were used as model analytes. The best “traditional” eluent, i.e., methanol–THF–water (2 : 1 : 7) was used as the benchmark. A generic two-step chromatographic optimization procedure by UHPLC consisting of (1) a simplex design using the Snyder solvent triangle and (2) HPLC modelling software was used.

In the first step, two ternary mixtures were found (acetone–ethyl acetate–water (20.25 : 3.75 : 76) and ethanol–ethyl acetate–water (9.5 : 7.5 : 83)), which already gave better results than the benchmark. The second step in which the influence of the gradient time, temperature and ratio of the two best ternary isocratic solvents was studied, led to an optimal 10.5 min gradient and a minimum resolution of 5.76.

In the final step, scale-up from 2.1 to 22 mm i.d. pHPLC columns proceeded successfully. When 0.5 g of the sample was injected, baseline separation was maintained. Chromatographic and absolute purities for products exceeded 99.5% and 95% respectively. This example shows that using less toxic and cheaper solvents for pHPLC can go hand in hand with higher productivity and less waste.

SEE

http://www.rsc.org/suppdata/c5/gc/c5gc00887e/c5gc00887e1.pdf