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Special Report                                                                                                                                                                   Special Report


                                                                          has actually  helped in the crystallisa-   steps was 72%, improving the total route  of  operability provided by  continuous  this approach has  the following
                                                                          tion of pure product directly from the     yield to 53% from 27% in batch mode.  method development that would  have  advantages over batch process: (i) the
                                                                          reaction mixture. (Dennehy et al. Org.     This work clearly highlights the benefi ts  been otherwise unattainable  in batch  turbo Grignard reagent formation and
                                                                          Process Res. Dev. 2020, 24, 10, 1978 –     of combining batch and fl ow processes  mode.                        subsequent reactions are more effi cient,
                                                                          1987).                                     for safety, effi ciency, and sustainability                          improving overall synthesis effi ciency
                                                                                                                     in pharmaceutical synthesis. Advantages  Tramadol                   compared to conventional methods
                                                                             Advantages over batch process           over batch process include: (i) improved   Tramadol is an analgesic drug used  with  lower  yields  (<  35%);  (ii)  only
                                                                          include: (i) A greener approach by using   the total route yield to 53% from 27%;  for management of moderate to severe  small amounts of reactive or hazardous
                                                                          reduced solvent volume and a greener       and (ii) a total residence time for the four  pain. It was synthesized with improved  intermediates  (like Grignard reagents)
                                                                          solvent; (ii) method enables inline purifi -  steps is 90 min.                yield (96%) in a continuous fl ow reac-  are  present  at  any  time;  and  (iii)
                                                                          cation and separation, resulting in the                                      tor, in comparison to traditional batch  importantly, reduced reaction times for
                                                                          crystallisation of pure product directly   Grignard reactions                process. A multi-operation, continuous-  Grignard formation was reported.
                                                                          from  the  reaction  mixture;  and  (iii)     Synthesis  of  Grignard reagent and  fl ow platform for the synthesis of tra-
                                                                          complete removal of 2.1 equivalents of     its subsequent reaction  are pivotal to  madol, ranging from gram to decagram  Nitration and Diazotization
                                                                          the succinimide by-product.                not only pharma industry but also the  quantities, is  described by  Monos  et   These are among the most commonly
                                                                                                                     agrochemical industry. Few reports on  al. (Synlett 2020; 31(19): 1888-1893).  done reactions in pharma intermediate
                                                                             Cinnarizine, cyclizine, buclizine,      synthesis of some important drugs are  A comparison of process metrics  synthesis. Incidentally, in most of the
                                                                          and meclizine  belong to a family  of      described below-                  including E-Factor,  production rate,  cases these are done in batch mode at
                                                                          antihistamines that resemble each other                                      and space-time yield are used to con-  conditions  of  low temperature,  slow
                                                                          in terms of a 1-diphenylmethylpiperazine   Fluconazole                       textualize the developed platform with  addition of one of the reagents, use of
                                                                          moiety. A four-step continuous process        Fluconazole is a triazole compound,  respect to established engineering and  large quantities of solvents as well as
       subsequent continuous removal and  intermediate isolation. (De Vitis et al.,  to  generate  the  fi nal  antihistamines   widely used anti-fungal, also found use-  synthetic methods for making tramadol.  reagents, etc. In the recent time, it has
       mitigation  of HCl that  evolves needs  ChemistryOpen. 2017, 6(5):668-673.)  from bulk alcohols has been reported by   ful in HIV-infected and cancer patients.                   been demonstrated for a large number
       special attention.                                                 Borukhova et al. (ChemSusChem 2016,        The drug was  commercialized  way    Advantages of  this approach over  of substrates that these  reactions are
                                           Advantages over batch process  9, 67-74). HCl is used to synthesize the   back in 1988 with a tradename, Difl ucan.  the batch process include: (i) all purifi -  better when done in fl ow.
          A rapid and convenient preparation  include: (i) biocatalysed heterogeneous  intermediate chlorides in a short reac-  Korwar  et al. (Eur. J. Org. Chem.,  cation operations are  incorporated
       of Captopril using CFS  by Chemo-  regio-and stereoselective  oxidation  tion time and excellent yields with a   2017,  6495-6498)  have reported the  in-line  for  the  Mannich  reaction;  and   In a recent  study, Brocklehurst,  et
       enzymatic Method  was  demonstrated  reaction; and (ii) overall yield of 50%  total residence time 90 min for all the   formation of fl uconazole using continu-  (ii) high  production rate of tramadol  al. (Org. Process Res. Dev. 2011, 15, 6,
       by chlorination  step to transform the  after crystallisation.     four steps. Overall isolated  yields for   ous fl ow chemistry primarily involving  (13.7 g/h).                 1447-1453) have reported continuous
       chiral intermediate, (R)-3-hydroxy-                                cinnarizine, cyclizine, and  a  buclizine   the formation of an intermediate via a                             fl ow nitration of 8-bromo-1H-quinolin-
       2-methylpropanoic  acid,  into  the  fi nal   Use of CFS to undertake  a  multi-  derivative are 82, 94, and 87 %, respec-  Grignard reaction, followed by further  Melitracen     2-one with near-complete  conversion
       product. Conducted under continuous  step chlorination cascade  has been  tively).  Advantages over batch pro-  transformations to obtain fl uconazole.  Melitracen  is a drug used for the  within a 3-minute residence time at
       fl ow,  this  step  improves  safety  and  reported with effective inline work-  cess include: (i) a four-step continuous                        treatment  of anxiety and depression.  90°C followed by scale-up that yielded
       effi ciency by allowing precise control of  up and end-of-line crystallisation  in  process; and (ii) overall good yields.  In this  protocol,  the  aryl  halide  Pederson et al. (Org. Process Res. Dev.  201 g of product. Another continuous
       reactive chlorinating agents and in-line  batch,  leading  to  isolation  of  α-thio-                         reacts with iPrMgCl·LiCl to form the  2018, 22, 2, 228–235) reported a con-  nitration protocol was  established for
       separation of by-products.  The seam-  β-chloroacrylamide  Z-3  in  pure  form   Prieschl et al. (Org Process Res Dev   aryl magnesium reagent (a Grignard  tinuous  fl ow  process  for  synthesis  of  2-amino-4-bromo-benzoic acid methyl
       less integration of chlorination  with  from a complex reaction mixture, ex-  2023, 27 (4), 601-609) have reported a   reagent)  in  a  continuous  fl ow  reac-  Melitracen. In fl ow process both hydro-  ester as the batch nitration  results in
       subsequent steps makes it almost tele-  ploiting the advantage of effi cient heat  new route for synthesizing the canna-  tor, which subsequently, reacts with 1,  lysis and dehydration were performed  noticeable quantity of by-product. Further
       scopic, thereby eliminating the need for  transfer in fl ow. Using a greener solvent  binoid receptor type 2 agonist. The fi nal   3-dichloroacetone  in the continuous  in single step.  nitration  of  1-benzosuberone  in  fl ow
                                                                          synthesis strategy has four steps that     fl ow system to form the key intermedi-                              helped avoid dangerous decomposition
                                                                          combine  batch  and  fl ow.  After  batch   ate  (fl uconazole  precursor)  with  high   The phase separation step was also  of the accumulated mono-nitro deriva-
                                                                          N-pivaloylation,  high-temperature         selectivity  and high yield.  The inter-  eliminated and only THF was used as  tive in the presence of excess nitrating
                                                                          cyclisation  was  performed  in  fl ow,     mediate is then reacted with 1,2,4-tria-  a solvent in comparison  to the  batch  agent and improved the reaction’s
                                                                          yielding 82% over two steps. In a novel    zole in the presence of a base to form  process, which requires toluene-THF  selectivity.
                                                                          approach, chlorination  using oxalyl       fl uconazole. The last step is optimised  solvent mixture.  The both Grignard
                                                                          chloride has been demonstrated with        in batch conditions  due to longer  reaction (Step 1), hydrolysis and dehy-  The entire approach offered the
                                                                          a continuous cation exchange workup        reaction times. Advantages over batch  dration  (Step 2) were performed at  following advantages over batch protocol:
                                                                          to prevent side products followed by       process include: (i) safety concerns  ambient temperature, whereas the batch  (i)  scaling up nitrations  to  produce
                                                                          reaction of the aryl chloride with S-(3)-  involved with organometallic reagents,  process reaction happens at 50 C.  a  few  hundreds  of  grams;  and  (ii)  a
                                                                                                                                                                                o
                                                                          hydroxypyrrolidine, yielding 88% over      addressed  through  a  continuous  fl ow                             safer alternative to running dangerous
                                                                          two steps. The overall yield for the four   approach;  and  (ii)  enhanced  window   When compared to the batch process,  exothermic reactions in short  time,


       186                                                                 Chemical Weekly  December 17, 2024        Chemical Weekly  December 17, 2024                                                              187


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