WO2008053221A2 - Process for preparing indol- 5 -oxy- quinazoline derivatives and intermediates - Google Patents
Process for preparing indol- 5 -oxy- quinazoline derivatives and intermediates Download PDFInfo
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- WO2008053221A2 WO2008053221A2 PCT/GB2007/004176 GB2007004176W WO2008053221A2 WO 2008053221 A2 WO2008053221 A2 WO 2008053221A2 GB 2007004176 W GB2007004176 W GB 2007004176W WO 2008053221 A2 WO2008053221 A2 WO 2008053221A2
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- 0 Cc1cc(c(F)c(cc2)Oc3c(cc(c(O*)c4)OC)c4ncn3)c2[n]1 Chemical compound Cc1cc(c(F)c(cc2)Oc3c(cc(c(O*)c4)OC)c4ncn3)c2[n]1 0.000 description 4
- BHHVNHQWMNILEO-IMVHTWTDSA-N Cc1cc(c(F)c(cc2)O/C3=C/C=C\C=C/C=C\C=C/C3=C)c2[nH]1 Chemical compound Cc1cc(c(F)c(cc2)O/C3=C/C=C\C=C/C=C\C=C/C3=C)c2[nH]1 BHHVNHQWMNILEO-IMVHTWTDSA-N 0.000 description 1
- LQLKYGWCSLKJER-UHFFFAOYSA-N Cc1cc(c(F)c(cc2)OC3CCCCCCCCCCC3)c2[nH]1 Chemical compound Cc1cc(c(F)c(cc2)OC3CCCCCCCCCCC3)c2[nH]1 LQLKYGWCSLKJER-UHFFFAOYSA-N 0.000 description 1
- BNDMWBMVOITFQA-UHFFFAOYSA-O Cc1cc(c(F)c(cc2)Oc3c(cc(c(O)c4)[OH+]C)c4ncn3)c2[nH]1 Chemical compound Cc1cc(c(F)c(cc2)Oc3c(cc(c(O)c4)[OH+]C)c4ncn3)c2[nH]1 BNDMWBMVOITFQA-UHFFFAOYSA-O 0.000 description 1
- PAQYIEZTLSDLQO-UHFFFAOYSA-N c1c(cncn2)c2cnc1 Chemical compound c1c(cncn2)c2cnc1 PAQYIEZTLSDLQO-UHFFFAOYSA-N 0.000 description 1
- PLZDHJUUEGCXJH-UHFFFAOYSA-N c1c2ncncc2cnc1 Chemical compound c1c2ncncc2cnc1 PLZDHJUUEGCXJH-UHFFFAOYSA-N 0.000 description 1
- BWESROVQGZSBRX-UHFFFAOYSA-N c1cc(ncnc2)c2nc1 Chemical compound c1cc(ncnc2)c2nc1 BWESROVQGZSBRX-UHFFFAOYSA-N 0.000 description 1
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- C07D209/00—Heterocyclic compounds containing five-membered rings, condensed with other rings, with one nitrogen atom as the only ring hetero atom
- C07D209/02—Heterocyclic compounds containing five-membered rings, condensed with other rings, with one nitrogen atom as the only ring hetero atom condensed with one carbocyclic ring
- C07D209/04—Indoles; Hydrogenated indoles
- C07D209/08—Indoles; Hydrogenated indoles with only hydrogen atoms or radicals containing only hydrogen and carbon atoms, directly attached to carbon atoms of the hetero ring
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- A—HUMAN NECESSITIES
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- A61P17/00—Drugs for dermatological disorders
- A61P17/06—Antipsoriatics
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- A—HUMAN NECESSITIES
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- A61P29/00—Non-central analgesic, antipyretic or antiinflammatory agents, e.g. antirheumatic agents; Non-steroidal antiinflammatory drugs [NSAID]
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- A61P35/00—Antineoplastic agents
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P9/00—Drugs for disorders of the cardiovascular system
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P9/00—Drugs for disorders of the cardiovascular system
- A61P9/10—Drugs for disorders of the cardiovascular system for treating ischaemic or atherosclerotic diseases, e.g. antianginal drugs, coronary vasodilators, drugs for myocardial infarction, retinopathy, cerebrovascula insufficiency, renal arteriosclerosis
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C201/00—Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
- C07C201/06—Preparation of nitro compounds
- C07C201/12—Preparation of nitro compounds by reactions not involving the formation of nitro groups
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C205/00—Compounds containing nitro groups bound to a carbon skeleton
- C07C205/45—Compounds containing nitro groups bound to a carbon skeleton the carbon skeleton being further substituted by at least one doubly—bound oxygen atom, not being part of a —CHO group
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C205/00—Compounds containing nitro groups bound to a carbon skeleton
- C07C205/49—Compounds containing nitro groups bound to a carbon skeleton the carbon skeleton being further substituted by carboxyl groups
- C07C205/56—Compounds containing nitro groups bound to a carbon skeleton the carbon skeleton being further substituted by carboxyl groups having nitro groups bound to carbon atoms of six-membered aromatic rings and carboxyl groups bound to acyclic carbon atoms of the carbon skeleton
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D207/00—Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom
- C07D207/02—Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom
- C07D207/04—Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having no double bonds between ring members or between ring members and non-ring members
- C07D207/06—Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having no double bonds between ring members or between ring members and non-ring members with radicals, containing only hydrogen and carbon atoms, attached to ring carbon atoms
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- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D239/00—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings
- C07D239/70—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings condensed with carbocyclic rings or ring systems
- C07D239/72—Quinazolines; Hydrogenated quinazolines
- C07D239/86—Quinazolines; Hydrogenated quinazolines with hetero atoms directly attached in position 4
- C07D239/88—Oxygen atoms
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- C07D—HETEROCYCLIC COMPOUNDS
- C07D403/00—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, not provided for by group C07D401/00
- C07D403/02—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, not provided for by group C07D401/00 containing two hetero rings
- C07D403/12—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, not provided for by group C07D401/00 containing two hetero rings linked by a chain containing hetero atoms as chain links
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- C07D—HETEROCYCLIC COMPOUNDS
- C07D487/00—Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, not provided for by groups C07D451/00 - C07D477/00
- C07D487/02—Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, not provided for by groups C07D451/00 - C07D477/00 in which the condensed system contains two hetero rings
- C07D487/10—Spiro-condensed systems
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/55—Design of synthesis routes, e.g. reducing the use of auxiliary or protecting groups
Definitions
- the present invention relates to chemical processes for the manufacture of certain quinazoline derivatives, or pharmaceutically acceptable salts thereof.
- the invention also relates to processes for the manufacture of certain intermediates useful in the manufacture of the quinazoline derivatives and to processes for the manufacture of the quinazoline derivatives utilising said intermediates.
- the present invention relates to chemical processes and intermediates useful in the manufacture of the compound 4-(4-fluoro-2-methylindol-lH-5-yloxy)-6- methoxy-7-[3-(pyrrolidin-l-yl)propoxy]quinazoline.
- This compound falls within the disclosure of WO 00/47212 and is exemplified in Example 240 therein.
- Normal angiogenesis plays an important role in a variety of processes including embryonic development, wound healing and several components of female reproductive function.
- Undesirable or pathological angiogenesis has been associated with disease states including diabetic retinopathy, psoriasis, cancer, rheumatoid arthritis, atheroma, Kaposi's sarcoma and haemangioma (Fan et al, 1995, Trends Pharmacol. Sci. 16: 57-66; Folkman, 1995, Nature Medicine 1 : 27-31).
- vascular permeability is thought to play a role in both normal and pathological physiological processes (Cullinan-Bove et al, 1993, Endocrinology 133: 829-837; Senger et al, 1993, Cancer and Metastasis Reviews, 12: 303-324).
- Several polypeptides with in vitro endothelial cell growth promoting activity have been identified including, acidic and basic fibroblast growth factors (aFGF & bFGF) and vascular endothelial growth factor (VEGF).
- aFGF & bFGF acidic and basic fibroblast growth factors
- VEGF vascular endothelial growth factor
- VEGF is an important stimulator of both normal and pathological angiogenesis (Jakeman et al, 1993, Endocrinology, 133: 848-859; Kolch et al, 1995, Breast Cancer Research and Treatment, 36:139-155) and vascular permeability
- Receptor tyrosine kinases are important in the transmission of biochemical signals across the plasma membrane of cells. These transmembrane molecules to characteristically consist of an extracellular ligand-binding domain connected through a segment in the plasma membrane to an intracellular tyrosine kinase domain. Binding of ligand to the receptor results in stimulation of the receptor-associated tyrosine kinase activity which leads to phosphorylation of tyrosine residues on both the receptor and other intracellular molecules. These changes in tyrosine phosphorylation initiate a signalling cascade leading to a is variety of cellular responses. To date, at least nineteen distinct RTK subfamilies, defined by amino acid sequence homology, have been identified.
- FIt-I fms-like tyrosine kinase receptor
- KDR kinase insert domain-containing receptor
- Flt-4 fms-like tyrosine kinase receptor
- VEGF is a key stimulus for vasculogenesis and angiogenesis.
- This cytokine induces a is vascular sprouting phenotype by inducing endothelial cell proliferation, protease expression and migration, and subsequent organisation of cells to form a capillary tube (Keck et al, Science (Washington DC), 246: 1309-1312, 1989; Lamoreaux et al, Microvasc. Res., 55: 29- 42, 1998; Pepper et al, Enzyme Protein, 49: 138-162, 1996).
- VEGF induces significant vascular permeability (Dvorak et al, Int. Arch. Allergy Immunol., 107: 233-235,
- Angiogenesis and/or an increase in vascular permeability is present in a wide range of disease states including cancer (including leukaemia, multiple myeloma and lymphoma), diabetes, psoriasis, rheumatoid arthritis, Kaposi's sarcoma, haemangioma, acute and chronic nephropathies, atheroma, arterial restenosis, autoimmune diseases, asthma, acute inflammation,o excessive scar formation and adhesions, lymphoedema, endometriosis, dysfunctional uterine bleeding and ocular diseases with retinal vessel proliferation including age-related macular degeneration.
- cancer including leukaemia, multiple myeloma and lymphoma
- diabetes including leukaemia, multiple myeloma and lymphoma
- psoriasis rheumatoid arthritis
- Kaposi's sarcoma haemangioma
- haemangioma haemangioma
- AZD2171 is a potent inhibitor of VEGF RTK and demonstrates >800-5000 fold selectively compared to VEGFR-2 compared to the epidermal growth factor receptor tyrosine5 kinase, the ErbB2 receptor tyrosine kinase, the TEK (Tie-2) receptor tyrosine kinase and cyclin dependent kinase-2.
- AZD2171 shows excellent activity in the in vitro (a) enzyme and (b) HUVEC assays that are described in WO 00/47212 (pages 80-83).
- the AZD2171 IC 50 values for inhibition of isolated KDR (VEGFR-2), FIt-I (VEGFR-I) and Flt-4 (VEGFR-3) tyrosine kinase activities in the enzyme assay were ⁇ 2 nM, 5 + 2 nM and ⁇ 3 nM respectively.
- 0 AZD2171 inhibits VEGF-stimulated endothelial cell proliferation potently (IC 50 value of 0.4 ⁇ 0.2 nM in the HUVEC assay), but does not inhibit basal endothelial cell proliferation appreciably at a > 1250 fold greater concentration (IC 50 value is > 500 nM).
- WO 02/12227 discloses several possible routes for preparing indoleoxy bicyclic0 compounds. However, there is no specific disclosure in WO 02/12227 of a process for preparing a compound of the Formula I.
- WO 00/47212 discloses a route for the preparation of a compound of Formula I (see Example 240). This route for preparing the compound of the Formula I is satisfactory for the synthesis of relatively small amounts of the compound. However, the route involves linear rather than convergent synthesis, requiring the use of multiple purification steps and the isolation of a substantial number of intermediates. As such, the overall yield of the synthesis is not high. There is, therefore, a need for a more efficient synthesis of the compound of the Formula I suitable to make larger quantities of that compound.
- the new syntheses should minimise the number of intermediate compounds that need to be isolated and should not involve costly and time-consuming purification procedures. Additionally, the new syntheses should form consistently high quality compounds, in particular so as to form a high quality compound of the Formula I to satisfy the high purity requirements of a pharmaceutical product. The new syntheses should also use procedures and reagents that can safely be used in a manufacturing plant and that meet environmental guidelines.
- processes are also provided for the manufacture of key intermediate compounds that may be used in the manufacture of AZD2171.
- the new processes are advantageous in that they allow the compounds to be made in high quality and high yield on a larger scale.
- the processes allow a substantial reduction in the number of intermediate compounds that must be isolated and, in general, are more convergent than the previous routes. Such changes provide significant advantages of time and COSt.
- AZD2171 refers to the AZD2171 free base, unless otherwise stated.
- a key intermediate that may be used in the preparation of AZD2171 is 2-methyl-4-fluoro-5-hydroxy-indole, the compound of the Formula II:
- Example 237 of WO 00/47212 discloses three routes for the preparation of a compound of the Formula II.
- the first route involves the reaction of 2-fluoro-4-nitroanisole with
- the mixture of protected indoles is reacted in tetrahydrofuran (THF) solvent with tert- butyllithium and methyl iodide followed by trifluoroacetic acid to give a mixture of 6- fluoro-5-methoxy-2-methyl-indole and 4-fluoro-5-methoxy-methylindole.
- THF tetrahydrofuran
- 4-fluoro-5-methoxy-methylindole is reacted with boron tribromide in methylene chloride to give the compound of Formula II, 4-fluoro-5-hydroxy-2- methylindole.
- the second route involves the reaction of ethyl acetoacetate with l,2,3-trifluoro-4- nitrobenzene in THF in the presence of sodium hydride to form 3-acetylmethyl-l,2- difluoro-4-nitrobenzene.
- 3-Acetylmethyl-l,2-difluoro-4-nitrobenzene is then reacted with trimethyl orthoformate in methylene chloride in the presence of montmorillonite to form l,2-difluoro-3-(2,2-dimethoxypropyl)-4-nitrobenzene.
- l,2-Difluoro-3-(2,2- dimethoxypropyl)-4-nitrobenzene is then reacted with benzyl alcohol in dimethylacetamide (DMA) in the presence of sodium hydride to form 3-acetylmethyl-l- benzyloxy-2-fluoro-4-nitrobenzene.
- DMA dimethylacetamide
- This compound is cyclized and deprotected by reacting with 10% palladium on charcoal in ethanol/acetic acid in the presence of hydrogen to give the compound of Formula II, 4-fluoro-5-hydroxy-2 -methylindole.
- the third route involves the reaction of l,2-difluoro ⁇ 3-(2,2-dimethoxypropyl)-
- the routes disclosed in the prior art documents for the preparation of a compound of 5 the Formula II are satisfactory for the synthesis of relatively small amounts of the compound. However, they all require each of the intermediates to be isolated and, therefore, include multiple isolation and/or purification steps. This results in a satisfactory overall yield of the compound of the Formula II on the small scale used.
- the routes disclosed in the prior art documents are unsuitable for use on a manufacturing scale because they includeo multiple isolation and/or purification steps, which cannot be conducted efficiently on a manufacturing scale.
- the routes disclosed in the prior art documents are unsuitable for use in the manufacture of a high purity pharmaceutical product.
- the news synthesis should not involve costly and time-consuming isolation and/or purification procedures.
- the new synthesis should reduce the number of isolation and/or purification procedures required, thereby reducing costs and time of manufacture.
- the new synthesis should minimise the number of solvents used throughout the process, which improves environmental performance and provides the opportunity for solvent recovery.
- the new synthesis should also provide a robust and reliable method of isolating the compound of the Formula II and consistently should provide high quality compound of the Formula II, for example so as to satisfy the regulatory requirements for the introduction of starting materials into the production of pharmaceutical products.
- R 1 and R 2 are independently selected from fluorine, chlorine, bromine, iodine and optionally substituted alkylsulphonyloxy such as trifloxy or tosyloxy; which process comprises the steps of:
- R 1 and R 2 are independently selected from fluorine, chlorine, bromine and iodine. In another embodiment R 1 and R 2 are independently selected from fluorine, chlorine and bromine. In another embodiment R 1 is fluorine and R 2 is bromine. In another embodiment both R 1 and R 2 are fluorine.
- R 3 is a suitable esterifying group such as optionally substituted C ⁇ aHcyl or optionally substituted benzyl.
- suitable esterifying groups such as optionally substituted C ⁇ aHcyl or optionally substituted benzyl.
- the skilled person would be able to select suitable esterifying groups which would not interfere with the processes of this embodiment of the invention and would allow removal of the ester group during process step (c).
- R 3 is C 1-6 alkyl or benzyl. In another embodiment Q-ealkyl. In another embodiment R 3 is C ⁇ -4 alkyl. In a further embodiment R 3 is C 4 alkyl, conveniently tert-butyl.
- reaction of process (a) is conveniently carried out in the presence of a suitable solvent such as tetrahydrofuran or acetonitrile or in another embodiment a suitable non-polar solvent, such as toluene, trimethylbenzene or xylene, in the presence of a suitable base such as sodium /-butoxide or sodium tert-pentoxide.
- a suitable solvent such as tetrahydrofuran or acetonitrile
- a suitable non-polar solvent such as toluene, trimethylbenzene or xylene
- a suitable base such as sodium /-butoxide or sodium tert-pentoxide.
- the non-polar solvent is selected from toluene or trimethylbenzene.
- step (a) is carried out at a temperature in the range, for example, of from 50 to 110°C, conveniently in the range of from 60 to 80°C, more conveniently in the range of from 65 to 75 0 C.
- the compound of Formula IV may conveniently be selected from methyl 3- oxobutanoate, ethyl 3-oxobutanoate, propyl 3-oxobutanoate, butyl 3-oxobutanoate, sec-butyl
- the compound of Formula IV may be selected from methyl 3-oxobutanoate, ethyl 3-oxobutanoate and ⁇ -butyl 3-oxobutanoate.
- t-butyl 3-oxobutanoate can be used since this requires milder reaction conditions to be used in the process which has the advantage that the reactions are easier to perform and lower levels of side products are produced.
- reaction of process (b) is conveniently carried out in a suitable solvent such as water or a water miscible solvent such as tetrahydrofuran or acetonitrile in the presence of a suitable base such as sodium hydroxide, potassium hydroxide or lithium hydroxide.
- a suitable solvent such as water or a water miscible solvent such as tetrahydrofuran or acetonitrile
- a suitable base such as sodium hydroxide, potassium hydroxide or lithium hydroxide.
- step (b) is carried out at a temperature in the range, for example, of from 30 to 70°C, conveniently in the range of from 40 to 60 0 C, more conveniently in the range of from 45 to 55 0 C.
- aryl-alkyl ammonium salts include Triton B (trimethyl benzyl ammonium hydroxide) which is commercially available.
- tetra-alkyl ammonium salts include tetra-butyl ammonium chloride and tetra-butyl ammonium bromide.
- reaction of process (c) is conveniently carried out in a suitable solvent, such as dichloromethane in the presence of an acid, such as trifluoroacetic acid or toluene in the presence of an acid, such as para-toluene sulphonic acid, acetic acid, propionic acid or a mixture of acetic acid and sulphuric acid.
- a suitable solvent such as dichloromethane in the presence of an acid, such as trifluoroacetic acid or toluene in the presence of an acid, such as para-toluene sulphonic acid, acetic acid, propionic acid or a mixture of acetic acid and sulphuric acid.
- step (c) When trifluoroacetic acid in dichloromethane is used the reaction of step (c) is earned out at a temperature in the range, for example, of from 0 to 4O 0 C, conveniently in the range of from 10 to 35°C, more conveniently in the range of from 20 to 3O 0 C.
- a temperature in the range for example, of from 0 to 4O 0 C, conveniently in the range of from 10 to 35°C, more conveniently in the range of from 20 to 3O 0 C.
- toluene is used in the presence of para-toluene sulphonic acid, acetic acid, propionic acid or a mixture of acetic acid and sulphuric acid the reaction of step (c) is carried out a temperature in the range of between 8O 0 C and the boiling point of the solvent/acid mixture. In one embodiment the temperature is 9O 0 C.
- step (d) is carried out at a temperature in the range, for example, of from 0 to 5O 0 C, conveniently in the range of from 10 to 4O 0 C, more conveniently in the range offrom 20 to 30°C.
- the process of the first aspect of the present invention is advantageous in that it allows a compound of the Formula II to be made in high quality and high yield on a larger scale.
- steps (a) to (c) can optionally be conducted as a continuous process without isolation and/or purification of the intermediate compounds of the Formulae V and VI. This significantly reduces the time and cost of manufacturing the compound of the Formula II on a larger scale.
- the process for the manufacture of a compound of the Formula II may further include the step (e) of isolating and/or purifying the compound of the Formula II.
- the step (e) may comprise any suitable steps or procedures for isolating the desired product that are described in the literature and/or that are known to the skilled person. Particular steps that would be of use would provide high quality and high purity product.
- the step (e) may, for example, also comprise crystallisation using a suitable solvent system.
- a suitable solvent system is a solvent system comprising dissolving the product in dichloromethane and crystallisation by the addition of isohexane or isoheptane, which provides a compound of the Formula II in a high purity, typically in a purity of greater than 90%, conveniently greater than 98%.
- R 4 is a protecting group
- Example 7 of WO 03/064413 discloses a route for the preparation of a compound of the Formula VIII wherein R 4 is benzyl.
- the route involves the reaction of 7-benzyloxy-4- chloro-6-methoxyquinazoline free base with 4-fluoro-5-hydroxy-2-methylindole and potassium carbonate in a N-methyl pyrrolidinone as solvent to provide the compound of the Formula VIII. It is stated in Example 7 of WO 03/064413 that 7-benzyloxy-4-chloro-6- methoxyquinazoline was prepared from 7-benzyloxy-6-methoxy-3,4-dihydroquinazolin-4-one by reaction with thionyl chloride in dimethylformamide as solvent.
- the new synthesis should not involve costly and time-consuming isolation and/or purification procedures.
- the new synthesis should reduce the number of isolation and/or purification procedures required, thereby reducing costs and time of manufacture.
- the new synthesis should conveniently also allow for effective isolation of the compound of the Formula VIII in a crystalline form in high purity and yield, which crystalline form should have good filtration characteristics.
- R 4 is a protecting group from a compound of the Formula IX:
- step (g) reacting the compound of the Formula X with a compound of Formula II (2-methyl- 4-fluoro-5-hydroxy-indole) optionally in situ and optionally in the presence of the solvent used in step (f) to form the compound of the Formula VIII.
- the term 'protecting group' refers to groups which are readily removed under mild acidic conditions, neutral conditions or mild basic conditions. Suitable methods for protection are those known to those skilled in the art. Conventional protecting groups may be used in accordance with standard practice (for illustration see T. W. Green, Protective Groups in Organic Synthesis, John Wiley and Sons, 1991).
- Suitable protecting groups at R 4 include benzyl, substituted benzyl (for example C 1-4 alkoxybenzyl, di-alkoxybenzyl, alkylbenzyl and di-C 1-4 alkybenzyl), tert-bntyl, 1, 1 -dimethyl- 1-ethylmethyl, allyl, substituted allyl (such as Ci -4 alkylallyl) or methoxyethoxymethyl.
- R 4 is benzyl.
- the process of the second aspect of the invention is advantageous in that it allows a compound of the Formula VIII to be made in high purity and high yield on a larger scale.
- the derivatizing agent could comprise any suitable agent for inserting a leaving group at the 4 position of the compound of Formula IX.
- L 1 include chlorine, bromine, iodine and optionally substituted alkylsulphonyl such as triflyl and tosyl.
- derivatizing agents include a chlorinating agent (such as phosphorus oxychloride), a brominating agent (such as phosphorus oxybromide or a mixture of N-bromosuccinimide and tri-isopropyl phosphite) and an iodinating agent.
- the process step (f) could comprise:
- a suitable solvent in step (f) is selected from toluene, chlorobenzene, 1,2-dimethoxyethane, acetonitrile and anisole.
- the solvent is anisole or toluene. In another embodiment the solvent is anisole.
- a suitable solvent in step (g) is selected from toluene, chlorobenzene, 1,2- dimethoxyethane and anisole.
- the solvent is anisole or toluene.
- the solvent is anisole.
- a co-solvent or co-solvents may be required to be added to solvents in (f) and (g) for example to aid solubility of the chlorobenzyline or indole intermediates.
- anisole can optionally comprise acetonitrile and N-methyl pyrolidinone and 1,2- dimethoxyethane can comprise N-methyl pyrolidinone.
- steps (f) and (g) are conducted in toluene as the solvent. In another aspect of the invention, steps (f) and (g) are conducted in anisole as the solvent.
- step (f) need not be isolated before conducting the step (g). This allows the process to be conducted as a continuous process without isolation and/or purification of the intermediate compound of the Formula X. This significantly reduces the time and cost of manufacturing the compound of the Formula VIII on a larger scale.
- anisole as the reaction solvent is advantageous because this solvent minimise the formation of by-products.
- the choice of solvent also allows for the easy and convenient isolation of the compound of the Formula VIII. For example, when the reaction mixture is cooled to ambient temperature, the compound of the Formula VIII typically forms a solid, which solid may then be collected by any conventional method.
- step (f) The mode of addition of the reagents in step (f) (i.e. as described in steps (f-1), (f-2) and (f-3)) is advantageous because it minimises the formation of by-products/impurities in that step. Reducing the formation of by-products/impurities enables the intermediate compound of the Formula X produced in step (f) to be used in step (g) without isolation and/or purification. Reducing the formation of by-products/impurities in step (f) also allows for the correct stoichiometry of the reagents in step (g) of the process and, therefore, a more efficient reaction in that step. This is turn provides a high yield and high purity of the compound of the Formula IX in step (g).
- a suitable chlorinating agent for use in step (f) is phosphorus oxychloride.
- a molar excess of chlorinating agent is used relative to the compound of the Formula IX.
- a molar excess in the range of from 1 to 2.0, conveniently in the range of from 1.2 to 1.4, may be used.
- a suitable base for use in step (f) is a base selected from triethylamine and N 5 N- diisopropylethylamine.
- the base is diisopropyethylamine.
- Adding a source of chloride to the reaction mixture may reduce the formation of by-products.
- step (f-1) the reaction is carried out at a temperature in the range of from 60 to
- step (f-2) the addition of reagents is carried out at ambient temperature.
- ambient temperature we mean a temperature in the range of from -10 to 3O 0 C, especially a temperature in the range of from 10 to 20 0 C, more especially a temperature of about 15 0 C.
- the reaction mixture is then heated to a temperature in the range of from 70 to
- step (f-3) the reaction is carried out at a temperature in the range of from 70 to
- step (f) the term “of about” is used in the expressions "of about 60 minutes", “of about 15 minutes”, “of about 90 minutes and “of about 1 hour” to indicate that the time periods quoted should not be construed as being absolute values because, as will be appreciated by those skilled in the art, the time periods may vary slightly. For example, the time periods quoted may vary by ⁇ 50 %, particularly by ⁇ 15 %, particularly by ⁇ 10% from the values quoted in step (f).
- the process for manufacturing a compound of the Formula X further includes the step of isolating the compound of the Formula X.
- the step may comprise any suitable steps or procedures for isolating the desired product that are described in the literature and/or that are known to the skilled person.
- step (g) is carried out at a temperature in the range of from 60 to 85°C, conveniently in the range of from 65 to 80 0 C, more conveniently in the range of from 70 to
- step (g) of the process the compound of the
- Formula VIII is isolated and/or purified, for example before storage, handling and/or further reaction. Therefore, in one aspect of the invention, the process for manufacturing a compound of the Formula VIII further includes the step (h) of isolating the compound of the
- the step (h) may comprise any suitable steps or procedures for isolating the desired product that are described in the literature and/or that are known to the skilled person.
- reaction mixture may be cooled to ambient temperature, at which temperature the compound of the Formula VIII typically forms a solid, and the solid so formed may be collected by any conventional method, for example by filtration.
- Both the compounds of the Formula IX and the nitrobenzene derivative of Formula III starting material are commercially available or can be prepared using conventional methods.
- the compound of Formula IX may be prepared as described in Example 5, preparation of starting materials.
- Example 7 of WO 03/064413 discloses a route for the preparation of a compound of the Formula XL The route involves the reaction of 7-ben2yloxy-4-(2-methyl-4-fluoroindol-5- yloxy) -6-methoxyquinazoline (a compound of Formula VIII) with ammonium formate in dimethylformamide containing 10% palladium on carbon to give a compound of Formula XL This route disclosed in the prior art for the preparation of a compound of the Formula XL
- the new synthesis should not involve costly and time-consuming purification procedures.
- the new synthesis should reduce the number of isolation and/or purification procedures required, thereby reducing costs and time of manufacture.
- the new synthesis should minimise the number of solvents used throughout the process, which improves environmental performance and provides the opportunity for solvent recovery.
- the new synthesis should also enable effective crystallisation of the compound of the Formula XI in a crystalline form with good filtration characteristics and in high purity and yield.
- R 4 is a protecting group which process comprises the steps of: (f) reaction of a compound of Formula IX with a derivatizing agent to form a compound of
- step (g) reacting the compound of the Formula X with a compound of Formula II (2-methyl-4- fluoro-5-hydroxy-indole), optionally in , «Y «,optionally in the presence of the solvent used in step (f) to form a compound of the Formula VIII;
- the process of the third aspect of the invention is advantageous in that it allows the compound of the Formula XI to be made in high purity and high yield on a larger scale.
- step (i) is carried out at a temperature in the range of from 20 to 60 0 C, more conveniently in the range of from 35 to 45°C.
- the reduction of the compound of Formula VIII is performed by catalytic hydrogenation, for example using hydrogen gas and an appropriate catalyst such as palladium on carbon.
- the reduction of the compound of Formula VIII is performed by catalytic transfer hydrogenation, using for example a non-gaseous hydrogen donor such as cyclohexene or ammonium formate and an appropriate catalyst such as palladium on carbon.
- a non-gaseous hydrogen donor such as cyclohexene or ammonium formate
- an appropriate catalyst such as palladium on carbon.
- Suitable solvents for step (i) include N-methylpyrrolidinone (NMP), dimethylformamide or dimethylacetamide.
- NMP N-methylpyrrolidinone
- dimethylformamide dimethylacetamide.
- Formula XI is isolated and/or purified. Any suitable steps or procedures for isolating and/or purifying the desired product that are described in the literature and/or that are known to the skilled person may be used. Particular steps that would be of use would provide high quality and high purity product.
- the compound of Formula XI may be isolated from NMP by addition of an antisolvent such as water, methanol, ethanol, isopropanol, butanol or acetonitrile.
- the compound of Formula XI is used in situ in the next step in the process.
- R 4 is a protecting group which process comprises the steps of: (f) reaction of a compound of Formula IX with a derivatizing agent to form a compound of
- the derivatizing agent could comprise any suitable agent for inserting a leaving group at the 4 position of the compound of Formula IX.
- L 1 include chlorine, bromine, iodine and optionally substituted alkylsulphonyl such as triflyl and tosyl.
- derivatizing agents include a chlorinating agent (such as phosphorus oxychloride), a
- step (g-1) The reaction of step (g-1) is carried out by addition of a solution of a salt of a compound ofQ the Formula VII to a solution of a compound of the Formula X in the solvent used in step (f- 1).
- the salt of a compound of the Formula VII may be prepared by use of lithium hydroxide, potassium hydroxide, sodium hydroxide, lithium carbonate, potassium carbonate, sodium carbonate or cesium carbonate. Optimally sodium hydroxide is used.
- the salt is formed at a temperature of -2O 0 C to +20 0 C, more conveniently in the range -10 0 C to O 0 C.
- the solutions of the salt of a compound of the Formula VII is added to a solution of a compound of the Formula X in the solvent used in step (f-1) at a temperature of 60 0 C to 100 0 C, conveniently in the range 70-90 0 C.
- step (i-1) is carried out at a temperature in the range of from 20 toQ 60°C, more conveniently in the range of from 35 to 45 0 C.
- the reduction of the compound of Formula XIV is performed by catalytic hydrogenation, for example using hydrogen gas and an appropriate catalyst such as palladium on carbon.
- the reduction of the compound of Formula XIV is5 performed by catalytic transfer hydrogenation, using for example a non-gaseous hydrogen donor such as cyclohexene or ammonium formate and an appropriate catalyst such as palladium on carbon.
- a non-gaseous hydrogen donor such as cyclohexene or ammonium formate
- an appropriate catalyst such as palladium on carbon.
- Suitable solvents for step (i) include N-methylpyrrolidinone (NMP), dimethylformamide or dimethylacetamide. 0
- NMP N-methylpyrrolidinone
- dimethylformamide dimethylacetamide
- Formula XI is isolated and/or purified. Any suitable steps or procedures for isolating and/or purifying the desired product that are described in the literature and/or that are known to the skilled person may be used. Particular steps that would be of use would provide high quality and high purity product.
- the compound of Formula XI may be isolated from NMP by addition of an antisolvent such as water, methanol, ethanol, isopropanol, butanol or acetonitrile.
- step (i-1) the compound of Formula XI is used in situ in the next step in the process.
- the further embodiment of the third aspect of the invention is applicable to the preparation of a number of ring systems substituted by 4-fluoro-2-methylindol-5-yloxy.
- a process for the manufacture of a compound of Formula XI- 1 is provided.
- A is a suitable ring system from a compound of the Formula X-I, wherein L 1 is a leaving group;
- Suitable rings systems for ring A are rings capable of being activated to allow displacement of the activating group by a phenolate ion, i.e. the structure of Formula VII.
- Such ring systems include:
- ring A is selected from quinazoline, quinoline, cinnoline and pyrrolotriazine. In another embodiment ring A is quinazoline. In another embodiment ring A is pyrrolotriazine. In another embodiment ring A is quinazoline and L 1 is at the 4-position of the quinazoline ring. In another embodiment ring A is pyrrolotriazine and L 1 is at the 4-position of the pyrrolotriazine ring.
- L 1 examples include chlorine, bromine, iodine and optionally substituted alkylsulphonyloxy or arylsulphonyloxy such as triflyloxy and p-tosyloxy.
- Reaction conditions for Process (s-2) Reactions conditions for Process (g-2) are analogous to process conditions for process (g-1).
- Reaction conditions for Process (i-2) Reactions conditions for Process (i-2) are analogous to process conditions for process (i-1).
- ring system A could be substituted by one or more groups. Such groups may be unaffected by the processes in this embodiment of the invention or may require protecting during the processes of this embodiment. The skilled man would be familiar with strategies to protect such group such as the use of protecting groups, the use of gentler reaction conditions which still facilitate the processes of the embodiment and/or the use of alternative catalysts. Conventional protecting groups may be used in accordance with standard practice (for illustration see T. W. Green, Protective Groups in Organic Synthesis, John Wiley and Sons, 1991) as described above.
- step (i-2) of the process the compound of the 5 Formula XI-I is isolated and/or purified. Any suitable steps or procedures for isolating and/or purifying the desired product that are described in the literature and/or that are known to the skilled person may be used. Particular steps that would be of use would provide high quality and high purity product.
- step (i-2) the compound ofQ Formula XI-I is used in situ in the next step in the process.
- a further embodiment of the invention provides a process for the manufacture of a compound of Formula XI-I from a compound of Formula X-I comprising the process steps (g-2) and (i-2) above.
- L 1 examples include chlorine, bromine, iodine and optionally substituted alkylsulphonyl such as triflyl and tosyl.
- Reactions conditions for Process (g-3) are analogous to process conditions for process (g-1). Reaction conditions for Process (i-3)
- Reactions conditions for Process (i-3) are analogous to process conditions for process (i-1).
- reaction of process (J-3) is conveniently carried out in a suitable solvent such as water or a water miscible solvent such as tetrahydrofuran or acetonitrile in the presence of a suitable base such as sodium hydroxide, potassium hydroxide or lithium hydroxide.
- a suitable solvent such as water or a water miscible solvent such as tetrahydrofuran or acetonitrile
- a suitable base such as sodium hydroxide, potassium hydroxide or lithium hydroxide.
- step (J-3) is carried out at a temperature in the range, for example, of from 30 to 70 0 C, conveniently in the range of from 40 to 60 0 C, more conveniently in the range of from 45 to 55 0 C.
- aryl-alkyl ammonium salts include Triton B (trimethyl benzyl ammonium hydroxide) which is commercially available.
- tetra-alkyl ammonium salts include tetra-butyl ammonium chloride and tetra-butyl ammonium bromide.
- step (j-3) of the process the compound of the Formula XI-I is isolated and/or purified. Any suitable steps or procedures for isolating and/or purifying the desired product that are described in the literature and/or that are known to the skilled person may be used. Particular steps that would be of use would provide high quality and high purity product.
- step (j-3) the compound of Formula XI-I is used in situ in the next step in the process.
- a further embodiment of the invention provides a process for the manufacture of a compound of Formula XI-I from a compound of Formula X-I comprising the process steps (g-3), (i-3) and (j-3) above.
- R 4 is a protecting group which process comprises the steps of: (f) reaction of a compound of Formula IX with a derivatizing agent to form a compound of
- the process step (f) could comprise: s (f) reacting the compound of the Formula IX with a suitable derivatizing agent in the presence of a suitable base and a solvent selected from toluene and anisole, wherein the reaction is carried out by:
- the process of the fourth aspect of the invention is advantageous in that it allows a0 compound of the Formula XI to be made in high purity and high yield on a larger scale.
- this aspect of the invention following the manufacture of the compound of the
- step (g) the compound is isolated and, optionally, purified in step (h) of the process.
- the isolated compound of the Formula VIII is then used in step (j) for manufacturing a compound of the Formula XI, either immediately or following storage for an5 appropriate period of time.
- the isolation of the compound of the Formula VIII in step (h) is advantageous because it enables a broader choice of methods for removing the R group from the compound of the Formula VIII in step (j), for example compared to when this step is conducted in situ.
- step (j) may comprise any suitable steps or procedures for removing R 4 that are described in the literature and/or that are known to the skilled person. Particular steps that would be of use would provide high quality and high purity product.
- step (j) when R is a benzyl group this may be removed by catalytic hydrogenation, such as hydrogen gas and a suitable catalyst such as palladium on carbon.
- catalytic hydrogenation is advantageous because it provides a highly efficient and mild method of removing the benzyl group and because it allows for the efficient removal of by-products from the waste stream.
- the reaction of step Q) may be carried out at any temperature and in any solvent suitable for the particular method of removal of the benzyl group being used. For example with N-methylpyrrolidinone as solvent at a temperature between 20 to 6O 0 C.
- step (j) of the process the compound of the Formula XI is isolated and/or purified. Any suitable steps or procedures for isolating and/or purifying the desired product that are described in the literature and/or that are known to the skilled person may be used. Particular steps that would be of use would provide high quality and high purity product.
- R 4 is a protecting group. which process comprises the steps of converting the compound of the Formula IX to a compound of the Formula XI:
- the compound of the Formula XII is provided as the hydrochloride salt. In another embodiment the compound of Formula XII is provided as the oxalate salt. According to a further embodiment of the invention there is provided an oxalate salt of a compound of Formula XII.
- Example of L 2 include chlorine, bromine, iodine, mesyloxy and tosyloxy. In another embodiment example of L 2 include chlorine, bromine and iodine.
- step (k) the compound of Formula XI is reacted with a compound of Formula XII. In another embodiment in step (k) the compound of Formula XI is reacted with a compound of Formula XIII.
- the compound of the Formula I obtained in the form of the free base may be converted into a salt form and the compound of the Formula I obtained in the form of a salt may be converted into the free base or into the form of an alternative salt, if necessary.
- the process of the fifth aspect of the invention is advantageous in that it allows the compound of the Formula I to be made in high purity and high yield on a larger scale. Typically the process of the fifth aspect of the present invention proceeds in greater than 80% yield.
- the process of the fifth aspect of the invention is also advantageous for at least the 5 reasons discussed above in relation to the third and fourth aspects of the invention.
- step (k) the compound of the Formula XI is isolated and/or purified before step (k) is conducted, for example using any suitable steps or procedures that are described in the literature and/or that are known to the skilled person as discussed above.
- the compound of the Formula XI is reacted in-situ with a compound of FormulaQ XII or Formula XIII.
- a suitable base for use in step (k) is selected from sodium carbonate, potassium carbonate, sodium hydroxide, potassium hydroxide, potassium fert-butoxide and cesium carbonate.
- Step (k) may be conducted in any suitable solvent and at any suitable temperature.
- step (k) When the base used in step (k) is selected from sodium carbonate and potassium carbonate, suitable solvents include, for example, N-methylpyrrolidinone and N,N-dimethylformarnide.
- step (k) typically may be conducted at a temperature in the range of from 60 to 105°C, conveniently in the range of from 80 to 100°C, convenientlyQ in the range of from 75 to 85 0 C.
- the process of the fifth aspect of the invention is advantageous in that it allows the AZD2171 to be made in high purity and high yield on a larger scale. Typically, each of the steps of the process of the fifth aspect of the present invention proceeds in greater than 80% yield. 5 According to a sixth aspect of the present invention, there is provided a process for the manufacture of AZD2171 from a compound of the Formula IX:
- step (g) reacting the compound of the Formula X with 2-methyl-4-fluoro-5-hydroxy-indole, optionally in situ, optionally in the presence of the solvent used in step (f), to form a compound of the Formula VIII:
- AZD2171 (hexafluorophosphate), chloride or bromide; in the presence of a suitable base to provide a compound of the Formula I (AZD2171) or a salt thereof; whereafter the AZD2171 obtained in the form of the free base may be converted into a pharmaceutically acceptable salt form, if necessary.
- the process of the sixth aspect of the invention is advantageous in that it allows the AZD2171 to be made in high purity and high yield on a larger scale.
- each of the steps of the process of the seventh aspect of the present invention proceeds in greater than
- the process step (f) could comprise: (f) reacting the compound of the Formula IX with a suitable derivatizing agent in the presence of a suitable base and a solvent selected from toluene and anisole, wherein the reaction is carried out by:
- the base used in step (k) of the process of the sixth aspect of the present invention is potassium carbonate and the suitable solvent is N-methylpyrrolidinone.
- the aqueous layer was separated and washed with toluene (250 1).
- the aqueous layer was diluted with water (250 1), heated to 4O 0 C and acetic acid (191.4 kg) added, reducing the pH from 10.1 to 3.8.
- the pH was then adjusted to 1 with 20% w/w sulphuric acid ( ⁇ 315 kg).
- the mixture was cooled to O 0 C and seeded with l-(2-fluoro-3-hydroxy-6-nitrophenyl)-propan-2-one. Further water (600 kg) was added and the solid isolated by filtration.
- the filter cake was washed with water (300 1).
- the product was dried under vacuum (50 mbar) at 4O 0 C. Yield: 56.0 kg, 74% based on 1,2,3- trifluoro-4-nitrobenzene.
- the mixture was held at 25 0 C for 2 hours.
- the product was isolated by filtration, washing the filter cake with water (366 kg).
- the product was dried under reduced pressure (50 mbar) at
- the lower aqueous layer was separated and the organic layer further washed twice with hydrochloric0 acid (6% w/w, 36 ml).
- the organic layer was washed with aqueous sodium bicarbonate solution (2.3%w/w, 15 ml) and then water (30 ml). Further mesitylene (21 ml) was charged and the mixture evaporated on a rotary evaporator (25 mbar, bath 4O 0 C), giving 25 ml of solution.
- the aquous layer was further extracted with dichloromethane (24 ml) and the combined organic phase basified by the addition of aqueous sodium hydroxide (8.5% w/w, 23 ml) to pH 10.5.
- the aqueous phase was further washed with isohexane (23 ml), to give an aqueous solution of methyl 2-(2-fluoro-3-hydroxy-6-nitrophenyl)-3- oxobutanoate.
- aqueous layer was separated and discarded and the organic layer washed twice with hydrochloric acid 6% w/w, 90 ml), then with aqueous sodium bicarbonate (2.3% w/w, 37.5 ml) and finally water (75 ml).
- the mixture was cooled to 4O 0 C and 16.19% w/w aqueous sodium hydroxide solution (132 kg) added over 15 minutes, allowing the temperature to rise to 5O 0 C, followed by a line wash of water (5 kg).
- the mixture was held at 5O 0 C for 30 minutes, then heated to 8O 0 C.
- the batch was filtered through a Gaf filter, followed by a line-wash of anisole (10 kg). The lower aqueous layer was separated and the
- the 7-benzyloxy-6-methoxy-3,4-dihydroquinazolin-4-one starting material was prepared as follows: 0 A mixture of vanillic acid (200 g), acetonitrile (600 ml) and N-ethyldiisopropylamine
- Benzyl 4-(benzyloxy)-3-methoxybenzoate (78 g) was mixed with dichloromethane (580 ml), water (72 ml) and glacial acetic acid (288 ml). The mixture was cooled to 1O 0 C. Concentrated sulfuric acid (108 ml) was added in a controlled manner maintaining the temperature of the reaction mixture below 25°C. Concentrated nitric acid (17.5 ml) was then added keeping the temperature of the reaction mixture below 2O 0 C. The reaction mixture was then stirred at 20 0 C for 23 hours. The lower aqueous layer was removed and the organic layer was washed with water (290 ml).
- Benzyl 4-(benzyloxy)-5-methoxy-2-nitrobenzoate (77 g) was dissolved in acetonitrile (882 ml).
- Sodium dithionite (160.5 g) was added to the solution and the temperature adjusted to 25°C.
- Water (588 ml) was then added, maintaining the temperature at 25°C.
- the pH was maintained at 6 using 8.8 M sodium hydroxide during the reduction.
- the slurry was then heated to 65°C and the lower aqueous phase was removed. Concentrated hydrochloric acid (35% w/w, 7.25 ml) was then added. The slurry was allowed to cool to 4O 0 C and then to 20°C.
- the reactor was purged with nitrogen and recirculated through a Gaf filter before being filtered through a l ⁇ m Pall filter into a new reactor.
- a line wash of l-methyl-2-pyrrolidinone (66 kg) through the filters was applied to give a solution of 4-[(4-fluoro-2-methyl-lH-indol-5-yl)oxy]- 6-methoxyquinazolin-7-ol.
- potassium carbonate (10.3 kg) and the mixture heated to 80 0 C.
- 4-[(4-fluoro-2-methyl-lH-indol-5-yl)oxy]-6-methoxy-7-[3-(pyrrolidin-l- yl)propoxy]quinazoline can be similarly prepared by using a methyl tert-butyl ether solution of l-(3-chloropropyl)pyrrolidine prepared from l-(3-chloropropyl)pyrrolidine oxalate. l-(3-Chloropropyl)pyrrolidine oxalate (134.8 kg) was suspended in water (226 1) and methyl tert-butyl ether (83.4 kg) added.
- the stirred mixture was basified to p ⁇ >11 by addition of 49% w/w aqueous potassium hydroxide solution (138.9 kg).
- a line wash of water (22.6 1) was applied.
- the lower aqueous layer was separated and transferred to a second reactor.
- the upper organic layer was transferred to 200 1 drums.
- a line wash of methyl tert- butyl ether (16.7 kg) was applied.
- the aqueous layer was recharged to the original reactor and further extracted with methyl tert-butyl ether (83.4 kg).
- the lower aqueous layer was discarded.
- the original oraganic layer was recharged from the drums.
- a line wash of methyl tert-butyl ether (16.7 kg) was applied.
- l-(3-Chloropropyl)pyrrolidine oxalate was prepared as follows: To a solution of l-bromo-3-chloropropane (190 g) in toluene (455 ml) at 4O 0 C was added pyrrolidine (173 g), maintaining the temperature at 40-45 0 C. A line wash of toluene (40 ml) was then applied.
- the mixture was maintained at 40-45 0 C for 4 hours, then cooled to 2O 0 C and held for 6 hours.
- the mixture was washed with water (400 ml), and then further water (265 ml) added and the p ⁇ adjusted to 8.8-9.0 with extracted with 37% hydrochloric acid (9.5 ml).
- the aqueous layer was separated.
- the organic layer was added to a solution of oxalic acid dihydrate (129.31 g) in a mixture of w ⁇ propanol (1070 ml) and water 109 ml) over 1 hour at 65-70 0 C.
- the mixture was cooled to 55 0 C and held at this temperature for 30 minutes to initiate crystallisation.
- the mixture was then cooled to 1O 0 C over 1.5 hours, and held at 10 0 C for an hour before filtering.
- the solid was washed with methyl tert-butyl ether (400 ml) and finally methyl tert-butyl ether (300 ml).
- the solid was dried at 40 0 C in a vacuum oven to give l-(3- chloropropyl)pyrrolidine oxalate. Yield . 208.23g, 72.5% of theoretical
- Methanol (114 1) was cooled to 0°C and degassed as above. Maleic acid (6.96 kg) was added and the mixture stirred to give a clear solution whilst maintaining the temperature at O 0 C. This was transferred via a l ⁇ m Pall filter to the crystalliser, maintaining the temperature in the crystalliser at 55-6O 0 C. A line wash of methanol (43 1) was applied. The temperatureQ was adjusted to 55°C and micronised 4-[(4-fluoro-2-methyl-lH-indol-5-yl)oxy]-6-methoxy-7- (3-pyrrolidin-l-ylpropoxy)quinazoline maleate salt (Form A, 0.43 kg) was added.
- the batch was cooled to 20 0 C and concentrated under reduced pressure (130 mbar), allowing the batch temperature to reach 100 0 C, collecting 24 ml of distillate.
- the batch temperature was adjusted to 65°C and a solution of water (4 ml) in methanol (28 ml) added.
- the mixture was cooled to 20 0 C and the product filtered.
- the filter cake was washed with methanol (2 x
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Abstract
Description
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AU2007315982A AU2007315982B2 (en) | 2006-11-02 | 2007-11-01 | Process for preparing indol- 5 -oxy- quinazoline derivatives and intermediates |
CN2007800404376A CN101528688B (en) | 2006-11-02 | 2007-11-01 | Process for preparing indol- 5 -oxy- quinazoline derivatives and intermediates |
MX2009004708A MX2009004708A (en) | 2006-11-02 | 2007-11-01 | Chemical process. |
CA002667920A CA2667920A1 (en) | 2006-11-02 | 2007-11-01 | Process for preparing indol-5-oxy-quinazoline derivatives and intermediates |
BRPI0717751-8A2A BRPI0717751A2 (en) | 2006-11-02 | 2007-11-01 | PROCESS FOR MANUFACTURING A COMPOUND, COMPOUND, AND SALT OF A COMPOUND. |
JP2009535123A JP2010508340A (en) | 2006-11-02 | 2007-11-01 | Process for preparing indole-5-oxy-quinazoline derivatives and intermediates |
EP07824415A EP2129657A2 (en) | 2006-11-02 | 2007-11-01 | Process for preparing indol-5-oxy-quinazoline derivatives and intermediates |
IL198117A IL198117A0 (en) | 2006-11-02 | 2009-04-07 | Process for preparing indol-5-oxy-quinazoline derivatives and intermediates |
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US9688688B2 (en) | 2013-02-20 | 2017-06-27 | Kala Pharmaceuticals, Inc. | Crystalline forms of 4-((4-((4-fluoro-2-methyl-1H-indol-5-yl)oxy)-6-methoxyquinazolin-7-yl)oxy)-1-(2-oxa-7-azaspiro[3.5]nonan-7-yl)butan-1-one and uses thereof |
US9790232B2 (en) | 2013-11-01 | 2017-10-17 | Kala Pharmaceuticals, Inc. | Crystalline forms of therapeutic compounds and uses thereof |
US9827248B2 (en) | 2013-02-15 | 2017-11-28 | Kala Pharmaceuticals, Inc. | Therapeutic compounds and uses thereof |
US9833453B2 (en) | 2013-02-20 | 2017-12-05 | Kala Pharmaceuticals, Inc. | Therapeutic compounds and uses thereof |
US9890173B2 (en) | 2013-11-01 | 2018-02-13 | Kala Pharmaceuticals, Inc. | Crystalline forms of therapeutic compounds and uses thereof |
CN107840843A (en) * | 2017-10-17 | 2018-03-27 | 浙江工业大学义乌科学技术研究院有限公司 | A kind of synthetic method of AZD2171 intermediate |
US10253036B2 (en) | 2016-09-08 | 2019-04-09 | Kala Pharmaceuticals, Inc. | Crystalline forms of therapeutic compounds and uses thereof |
US10336767B2 (en) | 2016-09-08 | 2019-07-02 | Kala Pharmaceuticals, Inc. | Crystalline forms of therapeutic compounds and uses thereof |
US10766907B2 (en) | 2016-09-08 | 2020-09-08 | Kala Pharmaceuticals, Inc. | Crystalline forms of therapeutic compounds and uses thereof |
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HU228964B1 (en) | 1999-02-10 | 2013-07-29 | Astrazeneca Ab | Quinazoline derivatives as angiogenesis inhibitors, process for their preparation and medicaments containing them |
ATE549329T1 (en) * | 2002-02-01 | 2012-03-15 | Astrazeneca Ab | CHINAZOLINE COMPOUNDS |
CN102603718B (en) * | 2012-02-08 | 2014-01-29 | 武汉凯斯瑞科技有限公司 | Synthesis method of cediranib |
WO2023080193A1 (en) * | 2021-11-04 | 2023-05-11 | 日産化学株式会社 | Method for producing indole compound |
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IL198117A0 (en) | 2009-12-24 |
MY179610A (en) | 2020-11-11 |
MY150219A (en) | 2013-12-31 |
TW200833667A (en) | 2008-08-16 |
BRPI0717751A2 (en) | 2013-10-22 |
NO20091588L (en) | 2009-05-28 |
EP2540706A2 (en) | 2013-01-02 |
CL2007003158A1 (en) | 2008-05-16 |
RU2012139319A (en) | 2014-03-20 |
EP2129657A2 (en) | 2009-12-09 |
US20080221322A1 (en) | 2008-09-11 |
EP2540705A3 (en) | 2013-10-30 |
AU2007315982B2 (en) | 2012-07-12 |
AR063449A1 (en) | 2009-01-28 |
US7851623B2 (en) | 2010-12-14 |
US8754240B2 (en) | 2014-06-17 |
RU2009120567A (en) | 2010-12-10 |
US20110257395A1 (en) | 2011-10-20 |
RU2012139318A (en) | 2014-03-20 |
CN102584798A (en) | 2012-07-18 |
SG176446A1 (en) | 2011-12-29 |
SG176447A1 (en) | 2011-12-29 |
EP2540705A2 (en) | 2013-01-02 |
CA2667920A1 (en) | 2008-05-08 |
JP2010508340A (en) | 2010-03-18 |
AU2007315982A1 (en) | 2008-05-08 |
EP2540706A3 (en) | 2013-11-06 |
CN102532108A (en) | 2012-07-04 |
CN101528688B (en) | 2012-09-05 |
WO2008053221A3 (en) | 2008-12-31 |
KR20090079247A (en) | 2009-07-21 |
CN101528688A (en) | 2009-09-09 |
MX2009004708A (en) | 2009-05-15 |
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