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Special Report                                                                   Special Report


 Cumene (C) mediated aerobic   techniques, such as CRISPR-based gene  batch process gives 50% yield but the  and a novel bioethanol and green NH
                                                                                                         3
 oxidation of polyethylene (PE)  editing. In the case of co-culture single  continuous process gives 84% yield and  approach; experiments were done in a
       reactor sugar gives EtOH + iPrOH –  that too in a much shorter reaction time.  pilot scale reactor operating parallel to
 Y. Che et al have referred to the endow-  BuOH and HAC + HBlc. (Chem. Eng.  This for analgesic, terpentadol. (Org.  the main reactor in a Brazilian industrial
 ment of new properties such as wetta-  Magazine, 1 Sep., 2024).  Prois. Res. Dev., 2025; DOI: 10.1021/  unit. The use of bioethanol and green
 bility and adhesion to polar material   acs.oprd.4c00447).               NH  can reduce environment impacts
                                                                             3
 via installation of polar group in PE.   Multistep continuous hetero-    by up to 5%. The proposed innovation
 Here Cu is used as a radical mediator   geneous synthesis of C.I. Reactive  Techno-economic optimisation  off ers a viable approach. (ACS Sustain-
 and O  as an oxidant to get oxidized PE   Red 195 and safety evaluation  of the renewable power to NH    able Chem. Eng., 2025; DOI: 10.1021/
                                                                       3
 2
       of the continuous diazotization  system  based  on  a  flexible    acssuschemeng.4c09745).
       process                           process
 was adopted. (Chem. Eng. Sci., 2025;  title. Concurrent FE of >97% to Cl    Synergizing process conditions,
                                                                          water sensitivity, and kinetic
 2
 DOI: 10.1016/j.ces.2025.121286; 306,  and 75% to CO at 200 mA/cm was   L. Li et al have integrated the diazotiza-  X. Zhang et al have referred to frequent
 2
                                         dynamic operation due to the fl uctuating  mechanisms to optimize sodium
 1 March, 121286).  realized. KCl is superior to NaCl and   tion and coupling reactions in solid-
 CsCl in terms of cathode FE to CO   liquid heterogeneous systems to realize  of renewable energy. Renewal energy  salicylate (SS) yield in sodium
 Mononitration of N-(4-methoxy-  and cell potential. (Chem. Eng. Pro-  large-scale, multi-step, continuous fl ow  to H  network is referred for integration  phenol carboxylation
                                            2
 phenyl))acetamide  (MPA)  in  cessing Process Intensifi cation, 2025,  with a functionalization degree of up   system of water-soluble azo dyes, which  with NH . Different alternatives are  [Salicylic acid continues to be made
                                                3
 continuous fl ow  211, May, 110209; DOI: 10.1016/j.  to 3.8 mole%. This material has a good   is quite challenging. These authors have  considered. A unit in Inner Mongolia is  by Kolbe-Schmidt process via the title
 cep.2025.110209).  adhesion to aluminium plates and has   considered. (Ind. Eng. Chem. Res., 2025;  process.]
 Z. Yu et al have studied the kinetics of   DOI: 10.1021/acs.iecr.4c 04329).
 the mononitration of MPA in a micro-  Magnetic  Nano  hydrometal-  increased tensile strength and improved   H. Zhang et al have used dried sodium
 reactor and the kinetic model was proved   elastic modulus compared to the pristine   Evaluation of the technical and   phenolate particles in a batch high-pres-
 by verifi cation experiments. Nitration   lurgy (MNHM) for metal ion  PE. Mechanism is explained. (Green   environmental  viability  of  a   sure reactor. A reaction temperature of
 separation and recovery
 isomers realized high selectivity. The   Chem., 2025; DOI: 10.1039/D5GC   bioethanol, propene, and green   160°C and a reaction pressure of 0.55
 title products and aspects of regioselec-  00034C).  NH   process  for  acetonitrile   Mpa were considered in a reaction time
 tivity were studied. It was possible to   H.E. Toma has come out with the con-  (ACN)  production  through   of about 40 min. and a stirring speed of
                                            3
 cept of MNHM, which is a nano tech- Efficient  hydrolysis  of  poly-
 work with operating conditions to get   a  comprehensive  life  cycle    50 rpm. The water content of the mate-
 selectivity for both 2-NMA and 3-NMA   nological version of hydrometallurgy.  ethylene terephthalate (PET)   reported safe operation and giving high   rial had important eff ects on the yield.
 above 99.5%. However, in practice,   Complexing supermagnetic nanoparti-  and product extraction using   throughput of 120 liters per hour and a   assessment (LCA)  A kinetic model is provided, and this
 98.4% selectivity of 2-NMA and 96%   cles can improve metal extraction. Mole-  an aqueous two-phase system   yield of up to 736 kg per day. The purity   study provides a basis for the design of
 selectivity of 3-NMA were obtained.   cules get complexed with supermagnetic   (ATPS)  of synthesized dye was 20% higher than   I.S. Freitas et al have referred to ACN   a continuous and effi  cient process. (Org.
 (Chem. Eng. Processing Process   nanoparticles containing complexing   the commercial C.I. Reactive Red 195.   as an important chemical used as solvent   Proc. Res. Dev., 2025; DOI: 10.1021/
 Intensifi cation, 2025, 208, 110136; DOI:   group. These particles then get captured   S. Liu et al have used PEG 6000/KOH/  DFT calculations were done; also the   and in pharmaceutical and fi ne chemicals   acs.oprd.4c00383).
 10.1016/j.cep.2024.110136).  by a magnet allowing a rapid and clean   H O to degrade PET at 90°C with con-  industries. These authors have analysed
 2
 separation of the sequestered metal ions.   version of 99.70% after 10 min and   ab initio Molecular Dynamics (AIMD).   the environmental footprint of ACN   Urea complete conversion to
 Paired electrochemical synthesis  This strategy has potential application in   terephthalate yield of 95.86%. Reaction   2-Naphtylamine-1,5-disulfonic acid dia-  production employing a Life Cycle   compound fertilizer in industrial-
 of Cl  from alkali chloride and   the recovery of strategic elements like   solution was used more than 5 times.   zonium salt was tested; DFT calculations   Assessment (LCA). The comparison   scale tandem reactors
 2
 CO from CO 2  Cu, Co, Ag, Hg, Au and even the lantha-  (Ind. Eng. Chem. Res., 2025; DOI:   were done. (Org. Proc. Res. Dev., 2025;   was between the fossil-based process
       DOI: 10.1021/acs.oprd.5c00055).
 nide ion. (Chem. Eng. Res. Des., 2025,
 J. Vehrenberg et al have come out with  216, April, 251-269; DOI: 10.1061/j.  10.1021/acs.iecr.4c 04596).  J. Hu et al have referred to a compound
                                                                          fertilizer with NH H PO  and KH PO
                                                                                                      2
                                                                                                         4
                                                                                              4
                                                                                           2
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 a potentially useful strategy as on the  cherd.2025.03.003).  Biofuels production via co-fer-  Continuous  flow  telescopic   which off ers signifi cant advantages in
 mentation of sugar and CO 2  synthesis of 3-methoxy propio-              enhancing both crop yield and quality.
       phenone (MPP) by Grignard
                                                                          These authors have combined electro-
 M.P. Bailey has a note on this subject   reaction (GR)                   chemical and subsequent chemical
 where in stage 1 sugar goes to H + CO 2                                  processes. A typical case refers to the
 2
 and in stage 2 H  is consumed to give   P. Wankhede and A.A. Kulkarni have   use of 200 gm urea, 1580 gm of solid
 2
 ethanol + acetic acid; stage 1 gives ace-  reported the title reaction starting with   compound fertilizers, as above, and 232
 tone + butanol + ethanol + HAC + HBlc   3-bromoanisole and making MgBr and   liters of pure H  are produced, without
                                                                                       2
 and together then go for separation. The   condensation with propionitrile. This is   any separation process. The process
 above refers to two-stage reactor adopt-  followed by quenching, neutralization,   is described. (Angew. Chem. Intl. Ed.,
 ing advanced microbial engineering   and phase separation. The optimised   2025; DOI: 10.1002/anie.2024.23092).
 156  Chemical Weekly  June 10, 2025  Chemical Weekly  June 10, 2025                                   157
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