Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

Org. Process Res. Dev. 2022, 26, 347. DOI: 10.1021/acs.oprd.1c00414

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

Route A

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

During the aqueous quench, a certain degree of back-hydrolysis to 2 occurred, which contaminated the initial crude product. The problem was solved by performing the chlorination with diphenylphosphoryl chloride (1.5 equiv) in DMF (5.5 vol).

For the Hofmann rearrangement of 11, the conditions reported in the literature, that is, use of aq NaOH, pyridine, and Br2 was avoided.

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

A DSC analysis of the heptane-wet diazonium salt 12-BF4 showed a highly exothermic degradation (487 J/g) at already 33 °C.

Only traces of the desired product 1 were formed by directly heating the slurry of diazonium salt.

A further idea—and inspired by a recent publication on the increased thermal stability of triazenes compared to diazonium salts—the transformation of 12-BF4 into its corresponding triazene derivative 13 resulted in a moderate 58% yield and low purity (69% a/a).

Route B

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

The use of stannane 15 is not desirable on scale and a novel approach to access fluoroketone 5 needed to be explored.

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

Ultimately, we decided against the further development of this route due to its multistep nature which would have translated into a long production time and reactor occupancy, unfavorable atom economy, and the relatively high costs of Selectfluor on scale.

Route C

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

Therefore, a third approach was developed, in which the desired heterocycle was formed via condensation of p-anisidine with 2-fluoromalonic acid, two inexpensive and commercially available starting materials.

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

Since the Raney nickel-catalyzed hydrogenolysis was very slow and the multiple additions of Raney nickel posed a severe safety hazard, it was decided to develop an improved hydrodechlorination system. Pd/C was reported to be effective in this reaction, but intermediate 8 had to be pretreated by stirring with 10% Pd/C (5% w/w) in MeOH to remove an unidentified catalyst poison.

Therefore, it was decided to explore transfer hydrogenations since these conditions are often less sensitive to catalyst poisons.

Multi-Kg Production of 3-Fluoro-6-methoxyquinoline

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