2019
DOI: 10.1021/acs.oprd.9b00366
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Investigation of a Flow Step Clogging Incident: A Precautionary Note on the Use of THF in Commercial-Scale Continuous Process

Abstract: Despite the many benefits that flow chemistry brings in the context of commercial manufacturing, a major issue for such continuous processing can be the clogging of flow equipment. In the case of verubecestat (MK-8931), the development of a flow chemistry process for the Mannich step greatly increased the reaction yield and the purity of the isolated product. However, in one of the plant-scale solvent runs in advance of process validation, an unforeseen and isolated clogging incident occurred. Herein, we repor… Show more

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Cited by 8 publications
(9 citation statements)
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“…With hexane as the common solvent (and i -PrOH used as a protic quench to keep the reaction mixture homogeneous), the system immediately clogged whatever the angle of micromixer, probably because of LiBr precipitation. Preparing a solution of n -BuLi in THF proved to be very challenging, as THF solutions of n -BuLi are prone to rapid degradation at room temperature. , …”
Section: Resultsmentioning
confidence: 99%
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“…With hexane as the common solvent (and i -PrOH used as a protic quench to keep the reaction mixture homogeneous), the system immediately clogged whatever the angle of micromixer, probably because of LiBr precipitation. Preparing a solution of n -BuLi in THF proved to be very challenging, as THF solutions of n -BuLi are prone to rapid degradation at room temperature. , …”
Section: Resultsmentioning
confidence: 99%
“…Preparing a solution of n-BuLi in THF proved to be very challenging, as THF solutions of n-BuLi are prone to rapid degradation at room temperature. 15,16 The equilibrium hypothesis, on the other hand, was ruled out by dedicated experiments: a microflow setup was implemented with fixed flow rate (Q 1+n-BuLi = 9 mL/min) and micromixer (θ = 90°, ID = 500 μm), and only the length of the reactor tube was modified (with fixed ID = 500 μm) (Scheme 3). With L = 3 cm (t R = 40 ms), 6 cm (t R = 80 ms), or 9 cm (t R = 120 ms), full conversion into 2 was observed with almost no evolution of the E/Z ratio over time.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
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“…An example was recently reported by researchers at Merck during a scale‐up campaign towards Verubecestat (Scheme 12). [ 23 ] When developing the synthesis of a key intermediate it was found that flow processing provided a 20 % increase in yield for a Mannich reaction between a chiral Ellman sulfinyl ketimine ( 37 ) and a methyl sulfonamide anion ( 38 ) due to the suppression of unproductive proton transfer as observed in batch mode. Flow processing was thereby employed in both the deprotonation step (using n ‐HexLi, 2.3 m , THF, –20 °C) and the subsequent Mannich reaction.…”
Section: Identifying the Pitfalls In Flow Chemistrymentioning
confidence: 99%
“…In most continuous reactor types, small-dimension tubing or fittings are locations where plugging or fouling will occur unless care is taken to filter feed solutions and ensure that every component of the system is fully in solution during all phases of the process. Even if the chemistry seems clean and homogeneity is established, solid materials can gradually coat the walls of flow reactors over time, such as polymeric species in solvents or metal plating from homogeneous catalysts . Fouling events often take many reactor turnovers to become manifest.…”
Section: Suggested Guidance For Authors Of CM Submissions To Opranddmentioning
confidence: 99%