Page 181 - CW E-Magazine (28-11-2023)
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Special Report                                                                   Special Report


 For the title NH synthesis the contribu-  Advantage is taken of the low-potential  of redox reactions.  TEMPO-media-  per hour and  all  this  in solvent-free
 3
 tion of hot-electron has been assessed.  oxidation of HCHO on a Pd membrane  ted oxidation of isopropanol to acetone   mode and thus eliminating the need for
 Here the activation energy is only 5g  anode to produce hydrogen that can per-  seems to be promising system for ELHP   a separation step. (Angew. Chem. Intl.
 vs 126 kj per mole for thermocatalysis.  meate through the membrane electrode.  of different TEMPO. 4-methoxy-TEMPO   Ed.; DOI: 10.1002/anie.202304219).
 The catalyst was stable for 1,000 hours.  It  is  demonstrated  that  electrocatalytic  appears to be the most promising
 This study provides a guide for the  dual hydrogenation of unsaturated  candidate. (ACS Sustainable Chem. Eng.,   Isobutanol (IB) to isobutene
 design of high performance photother-  dicarboxylic acid can be carried out when  2023;  DOI:  10.1021/acssusche-  (B)
 mal catalysts. (Angew. Chem. Intl. Ed.,  another Pd membrane electrode is also  meng.2c07419).  J-L. Dubois  et al have discussed the
 2023; DOI: 10.1002/anie.202304452).  adopted as the cathode. Thus reduction   title  conversion,  with respect  to pro-
 is done on both the anode and cathode   Dehydrogenation of perhydro-
 Electrocatalytic processes  in two separated chambers, leading to   N-propylcarbazole (PPC)  cesses and catalysts, as this has gained
 theoretical maximum FE of 200%. (Nature   The transport of much wanted H    important  for not  only  getting  iso-
       butene,  but conversion to derivatives,
 Electrocatalytic dual hydroge-  Catalysis, 2023, 6, 224-233).  through Liquid Organic Hydrogen Car- 2  like dimers, methacrylic acid, MTBE,
 nation of organic substrates   riers (LOHCs) is gaining traction for
 with a Faradaic Effi ciency (FE)   Highly selective TEMPO-cata-  large scale operations (There are indica-  multi-million  tonnes  per annum scale  catalytic reactor and it seems to be a
 approaching 200%  lysed bulk  electrooxidation   tions that it is partially commercialised).  (> 10-mtpa) The present process is at  feasible technology. There are exten-
                                         high reaction temperature and pressure  sive  opportunities  for  its  intensifi -
 [This column has covered many papers   of isopropanol to acetone for   and has problems of  safety hazards  cation. These authors have worked on
 on electrochemical processes, including  application in electrochemical   L.  Liu  et al have  worked with  Pd/
 valorisation of  CO  to CH /C H  etc.,  heat pumping  Al O -SiO catalyst  for an enhanced   and high energy consumption. Carbon  coupling between the type of catalyst,
 3
 3
 2
                                         nitride (g-C N ) with a unique sandwich  process conditions, type of membrane,
 4
 2
 2
 4
                                                  3
 in view of renewable energy avail-  effect  and have studied the effect  of   structure is a photocatalyst and H. Zhu  and reactor operation (isothermal and
                                                    4
 ability in a distributed way.]  A. Mishra  et al have referred to the   Al/Si ratio.  With Al/Si molar ratio of   et al have used this at room temperature,  non-isothermal). Ru- and Co-based
 development  of  more  energy  effi cient   2:1, Pd/AlSiO catalyst allowed 100%   atmospheric pressure, and solvent-free  catalysts and a Pd-Au membrane were
 G. Han  et al have referred to some  heat pump technologies for widespread   dehydrogenation of PPC in 360 minu-  conditions. A continuous fl ow strategy  considered. A more holistic approach
 intrinsic limitations associated with sub-  practical implications. Electrochemical   tes and had good stability. (Molecular   was adopted to reduce the effect of back  is a necessity to get the desired results.
 strate solubility and diffi cult separation  Looping Heat Pump (ELHP) techno-  Catalysis, 2023, 543, 1 June, 113-114;   mixing. The catalyst has high effi ciency,  (Reaction Chem.  Eng., 2023; DOI:
 of the products from the electrolyte.  logy has emerged as an attractive alter-  DOI:10.1016/j.mcat.2023, 113 114).  easy availability, is environmentally  10.1039/D2RE.00408A).
 The use of Pd membrane electrodes can  native to conventional vapor compres-  Selective  oxidation  of  Allyl-  friendly and stable and recyclable. (Ind.
 overcome the above problems by physi-  sion systems (VCS), which theoretically   benzene (AB) to Cinnamalde-  ETBE, and the  so-called renewable   End. Chem. Res., 2023; DOI: 10.1021/  Challenges in  unconventional
 cally separating the formation of reac-  promises  signifi cant  improvements  in   hyde (C)  aviation fuel, as IB can be obtained via   acs.iecr.3c00600).  catalysis
 tive hydrogen atoms from the hydroge-  both performance and energy consump-  [Allylic oxidations  are  practiced in   fermentation.  Thermodynamic  equili-
 nation of unsaturated organic substrates.  tion. This requires selective facilitation   bria of various reactants and products are   A. Bogaerts et al have discussed this sub-
 industry, e.g., propylene to acrolein.]  Modelling-aided coupling  of
       provided. Alumina catalysts are inhibited   catalysts, conditions, memb-  ject beyond the conventional “thermal”
 H. Fujisuka et al have come out with   by steam,  so reaction  under pressure   ranes,  and  reactors  for  effi -  catalysis. The availability of renewable
 the title process as an alternative to the   requires longer contact times and cata-  cient H  production from NH    energy is opening up new ways: Plasma
 established process based on benzalde-  lyst volume. The effect of partial pres-  2  3  catalysis;  catalysis  for  fl ow  chemistry
 hyde and acetaldehyde. BiMoO -loaded   sure of water was studied, since IB is   [This column has covered papers on   and  process  intensifi cation;  application
 x
 CoFeMoO catalysts were used and a   recovered from the fermentation broth.   NH  as H  carrier and a source for   of electromagnetic (EM) fi elds to modu-
                                                 2
                                           3
 x
 kinetic  analysis was done. (Ind. Eng.   [It  may be  noted that  5-kg of  C3-C5   energy, and indeed turbines have been   late catalytic activity; nanoscale gene-
 Chem. Res., 2023; DOI: 10.1021/acs.  alcohols are produced for every tonne   developed to burn NH . There is scope   ration at the catalyst interface of a strong
                                                           3
 iecr.3c00536).  of ethanol] (Catalysis Today, 2023,   to make H  from NH  when H  is needed   local EM by plasmonic effect. Plasma
                                                 2
                                                                2
                                                         3
       418, 1 June, 114126; DOI:10.1016/j.  as a reactant.]               catalyst  has  shown  synergistic  effects
 Solvent-free heterogeneous cata-  cattod.2023, 114126).
 lytic hydrogenation of poly-            N. Realpe et al have worked on mak-
 esters to  diols:  Polylactic  acid   Visible  light-driven  sand-  ing high-purity, pressurised H  from
                                                                  2
 (PLA) to 1,2-Propanediol (PD)  wich-like  g-C N -catalysed   NH decomposition in a membrane
                                           3
                         3
                           4
       oxidation to produce cumene
 R. Mi et al have reported the title con-  hydroperoxide (CHPO)
 version of  considerable commercial
 importance, using Zn-modifi ed Cu cata-  The producttion of phenol via air oxi-
 lyst.  The selectivity  was  99.5% and   dation of  cumene and  acid catalysed
 reactivity was 0.65gm per gm catalyst   cleavage of  CHPO  is  practiced on
 180  Chemical Weekly  November 28, 2023  Chemical Weekly  November 28, 2023                           181
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