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Special Report


       catalysis. The marked improvement in
       H  recovery arises out of metal carbide
        2
       formation induced by the mechanocata-
       lytic process, which does not catalyse
       formation of hydrocarbons. Thus, we
       have a process for net zero emissions.
       (Angew. Chem. Intl. Ed., 2024, 100;
       DOI: 10.1002/anie.202417644).
       Boosting the catalytic
       performance of core-shell
       structured Ru@Pd/SBA-15
       in 2-ethyl anthraquinone
       hydrogenation by tuning
       d-band centre                     initiator  or  zeolite  alone.  Cracking  at  of making alcohols instead of the
                                         445°C is reported. (Ind. Eng. Chem.  well-known hydroformylation reac-
       Y. Zhang et al have given the prepa-  Res.,  2024;  DOI: 10.1021/acs.iecr.  tion followed by hydrogenation.  Here
       ration  of the title catalyst for  the   4c01706).                 CH OH is added to the C=C bond in
                                                                             3
       hydrogenation under reference, which   Selective hydrogenation of   a  100%  atom  efficient  manner.  This
       is  relevant  in  H O   production. This   halogenated nitroarenes  is a tandem reaction as CH OH gives
                                                                                                 3
                       2
                     2
       catalyst gives a selectivity of 97.3%.                             CO:H  in a 1:2 ratio. Mn/pincer com-
                                                                               2
       (J. Catalysis, 2024; DOI: 10.1016/j.  G. Chen  et al have  worked on cost-   plex catalyst is able to take up this
       jcat.2024.115793; 440, Dec., 115793).  effective non-precious metal catalyst   daunting task. The ratio of the linear
                                         for  the title catalyst and single-atom   to branched alcohols was 93:7 and
       TEMPO-assisted thermal            cobalt catalyst has been used. This was   turnover numbers of more than 17,000
       and catalytic cracking of         tuned by tailoring the structure of sec-  could be realised (Thus, we have a cata-
       3-carene (3-C) and JP-10 to       ond coordination sphere via P doping.   lyst without Rh).  This process does
       produce low-molecular weight      Synchrotron  radiation-based  X-ray  ab-  not require pressure exceeding 10 bar.
                                                                          (Angew. Chem. Intl. Ed., 2024; DOI:
                                         sorption spectroscopy was used to charac-
       hydrocarbons                      terise catalyst. 20 examples are given   10.1002/anie.202418984).
       S.  Priyadarshi  et al  have reported the   with over 99% yields at 80°C under 0.5   Advances for catalysts in one-
       combo-effect of a free-radical initiator,   Pa H  pressure. (Angew. Chem. Intl. Ed.,   step oxidative esterification of
                                            2
       TEMPO  (2,2,6,6- Tetramethyl-1-piperi-   2024; DOI: 10.1002/anie.202421277).  aldehydes and alcohols with
       dinyloxy) and a zeolite HY catalyst on   Methanolysis of olefins: Low
       pyrolysis of 3-C and JP-10 (exotetra-   pressure synthesis of alcohols   alcohols to esters
       hydrodicyclopentadiene) to make hydro-   by the formal addition of   L. Ding et al have worked on making
       carbon fuels.  The combo system    methanol to olefins             esters without using carboxylic acids
       enhances the yield of low molecular weight                         and have referred to the necessity of
       hydrocarbons compared to thermal   S. Stahl et al have come out with an   the development of catalysts with high
       cracking or  cracking with  either   interesting and potentially useful way   catalytic  activity  and  a long  service
                                                                          life. The recent advances of the total
                                                                          process have been reviewed where
                                                                          one-step  oxidative  esterification  is
                                                                          realised. Heterogeneous catalysts based
                                                                          on  Au/Pd/Co,  and  Cu-based  and
                                                                          homogeneous catalysts are covered.
                                                                          Methods of the preparation of cata-
                                                                          lysts are covered. (Ind. Eng. Chem.
                                                                          Res.,  2024;  DOI:  10.1021/acs.iecr.
                                                                          4c02011).


       Chemical Weekly  January 28, 2025                                                               171


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