Page 175 - CW E-Magazine (23-7-2024)
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Special Report                                                                   Special Report


 for the catalyst (Pd/CsPMA). Spectro-                                    Effect of H  addition on coke
                                                                                      2
 scopic techniques were used, and theore-                                 formation and product distri-
 tical calculations were done. The mecha-                                 bution in catalytic coupling of
 nism of sulphite activation is discussed.                                CH
                                                                              4
 (ACS Catal., 2024, 14, No. 6, 4352-4361;                                 [A number of papers have appeared on
 DOI:10.1021/acscatal.4c00234).                                           the valorisation of CH , particularly to
                                                                                             4
 was converted to xylenes with the evo-                                   get C H  and this column has covered
                                                                               2
 lution of H S.  This reaction was con- A novel process for the oxida-    some papers.]
                                                                                 4
 2
 ducted at 375 C. (ACS Catal., 2024, 14,  tive dehydrogenation of eth-
 o
 No.6, 3867-3877; DOI:10.1021/acs-  ane to produce ethylene and           This coupling reaction  is at 100 C.
                                                                                                       o
 catal.3c06088).  acetic acid                                             Addition of 10% H  decreases the CH
                                                                                          2
                                                                                                         4
 [The concept of oxidative conversion of   imidazolium  chloride is  the IL.  Tem-  conversion by  a factor of 2; aromatic
 Sulphite-enhanced aerobic   ethane to ethylene and acetic acid has   perature of reactor is at 180 C. (Cata-  selectivity  is  signifi cantly  reduced.
 o
 methane oxidation to CH OH  been discussed for quite some time and   lysis Today, 2024, 434, 15 May, 114696;   10% H  reduces coke  deposition.  A
 3
                                                                                 2
 [Attempts to directly convert CH  to  it seems a 30,000-tpa plant exists in   DOI: 10.1016/j.cattod.2024.114696).  part of H  generated in the process is
 4
                                                                                  2
 CH OH continue to attract attention and  Saudi Arabia.]  Water-tolerant superbase   recycled. (Ind. Eng. Chem. Res., 2024;
 3
 this column has covered some papers.]  polyoxometalate [H (Nb O )]       DOI: 10.1021/acs.iecr.4c00381).
 -
 R. Bermeja  et al, Linde Engineering,   2  6  19  6
 S. Wang et al have reported that H -re-  have come out with the title process to   for homogeneous catalysis  Upgrading of aqueous ethanol
 2
 duced phosphomolybdate (PMA) gives   give polymer-grade ethylene and gla-  S. Kikkawa et al have reported Lind-  (EtOH) to long-chain alcohols
 promising title reaction at room tempera-  cial quality acetic acid.  This strategy   qvist-type NB oxide cluster, which is a   over immobilised highly dis-
 ture. Sulphite anions act as a promoter to   has many advantages, e.g., integrating   superbase and catalyses  Knoevenagel   persed Ni-Re catalyst
 with production of vinyl acetate (VAM)
 and ethylene vinyl alcohol (EVOH)   An integrative chemical recyc-  have come out with layered organic-  [A number of papers have appeared in
 products.  Ethylene requirements by   ling approach for catalytic   inorganic catalysts by the reaction of   the past for direct conversion of EtOH
 2028 may reach  230-mtpa. This cata-  oxidation of epoxy resin and   phosphotungstic acid and a Gemini   to e.g., n-butanol.]
 lytic process has lower CO  emissions.   in situ separation of degraded   quaternary ammonium salt.  This cat-
 2
 The proprietary  catalyst operates for   products  alyst gave a selectivity of 85% in the   Q. Zhang  et al have reported the Re
 more than 2 years and can be regene-    absence of organic solvents. (Ind. Eng.   doped Ni@C catalyst, made by a facile
 rated. Multi-tubular reactor is proposed   L. Liu  et al have worked on the title   Chem. Res., 2024; DOI: 10.1021/acs.  sol-gel method.  The bimetal 70-Ni-
 with molten salt cooling. (Hydrocarbon   problem as  we  can anticipate  prob-  iecr.4c00120).  Re@C gave higher selectivity towards
 Processing, 2024, March.)  lems associated  with the used blades         long-chain  alcohols. EtOH conver-
 and crossed aldol condensation  reac-  of windmills.  The oxidative  degrada-  Macrostructural design ap-  sion was about 60% and 45% long-
 Development of ionic liquids   tions (pKa>26). This superbase is water   tion depends on Fe/V=O radicals with  proach of the monolithic   chain alcohols were formed. (Ind. Eng.
 (ILs) promoted low content   tolerant. (Angew. Chem. Intl. Ed., 2024;   strong oxidising properties.  The  de-  catalyst and its application in   Chem. Res., 2024; DOI: 10.1021/acs.
 Ru catalysts for acetylene   DOI: 10.1002/anie.202401526).  graded products with different carboxyl  nitrobenzene (NB) hydroge-  iecr.4c00488).
 hydrochlorination  Transforming ethyl chloroace-  content can be effortlessly separated   nation  Optimisation of greener and
 [Vinyl chloride based on CH CH + HCl  tate (ECA) production – lever-  into liquid and solid phase.  The high   more effi cient 1,7-octadiene
 is a classic process widely practiced in  aging Reactive Chromato-  value application of degraded products  H. Wang et al have referred to the re-  (OD) epoxidation catalysed by
 China (one plant in India and forth-  graphy with Amberlyst-15  is referred. (Angew. Chem. Intl. Ed.,  duced pressure drop and improved cata-
                                         lyst utilisation effi ciency in monolithic  polymer-supported Mo (VI)
 coming unit in Kutch). It has a problem   2024; DOI: 10.1002/anie.202405912).
 associated with mercury-based catalysts,   ECA is an important intermediate and   catalyst. The trends in additive manu-  complex
 which  is  hazardous,  and  an  alternative   C. Gupta and S.M. Mahjani have come   Design of organic-inorganic   facturing technology allows innovative
 based on gold has been developed.]  out with the title strategy where the re-  phase transfer hybrid cata-  three-dimensional structural monolithic  M.M.R. Bhuiyan  and  B.  Saha  have re-
 action and separation are combined in a   lyst and its application in the   catalysts. The idea is also to eliminate  ported the title reaction (OD comes from
 H. Wang  et al have prepared nitro-  continuous way. The problems of equili-  epoxidation of α-olefi ns  internal diffusion.  A carbon-based  selective dimerisation of butadiene) us-
 gen-containing ILs modifi ed Ru-based  brium-based conversion is avoided.   monolithic catalyst was developed for  ing a heterogeneous polybenzimidazole
 catalysts for the title reaction; Ru con-  Modelling was done and this can be a   H. Ju et al have worked on long chain  the title  reaction.  The above catalyst  supported Mo (VI) catalyst  and  tert-
 tent reduced to 0.3%. This catalyst exhi-  basis for designing a SMBR. (Ind. Eng.   α-olefi ns where the traditional homo-  worked for NB hydrogenation.  (Ind.  butyl hydroperoxide (TBHP) as an oxi-
 bited high catalytic activity and stabi-  Chem. Res., 2024; DOI: 10.1021/acs.ie-  geneous or heterogeneous catalysts  Eng. Chem. Res., 2024; DOI: 10.1021/acs.  dising source.  The catalyst  was fully
 lity. 1,3-bis (2,6-diisopropylphenyl)  cr.4c00247).  show poor performance. These authors  iecr.4c00466).  characterised,  and  optimisation  was


 174  Chemical Weekly  July 23, 2024  Chemical Weekly  July 23, 2024                                   175


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