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Special Report                                                                   Special Report


 In one case the impurity at 6% level could   pressure up to 10 bar. Two cases of 98%
 be purged in a single crystallisation by   and 99.5% C H  minimum purity were
                   4
                 2
 switching the crystal form. In two other   considered. For the 98% purity C H
                                      4
                                   2
 cases where impurity level were 14%   recovery was 94.6%; for 99.5%+ purity
 and 3.5%, solvent switches solved the   the maximum C H  recovery was 80%.
                    2
                      4
 problems. (Org. Proc. Res. Dev., 2024;   (Ind. Eng. Chem. Res., 2024; DOI:
 DOI: 10.1021/acs.oprd.3C00406).  10.1021/acs.iecr.3C02808).
 has N O whose recovery is facilitated in  infl uence the performance of subsequent  Instantaneous and continuous   Application of Taylor Vortex
 2
 the above manner. AgZK-5 has N O/CO   unit operations in an undesirable way.  preparation of Avermectin   Flow Reactor (TVFR) for
 2
 2
 selectivity of 2.2. (Angew. Chem. Intl .Ed.,  These authors have followed the mod-  (A) nanoparticles (NPs) with   precise control of nucleation   CA, which removes C H  effi ciently and  95%. Acetic acid aqueous solution
                                                            8
                                                          3
 2023; DOI: 10.1002/anie.2023.17435).  el-free Quality-by-Control (QbC) frame-  high gravity anti-solvent   in reactive crystallisation  also moderate C H  removal. The C H 8   had higher dissolution effi ciency and
                                                        6
                                                                     3
                                                      2
 work and have improved crystallisation   precipitation technology  uptake was 177.8 cc (STP) per gm and  selectivity and the separation factor was
 Mixed matrix membranes   which brought out the effectiveness of   moderate C H  of 52.9 cc (STP) per gm.  up to 5038. (Green Chem., 2024; DOI:
                                                  2
                                                    6
 (MMM) incorporating amino-  temperature cycling. This also leads to   M. Hosoya et al have reported the use   The CH  uptake was only 7.7 cc (STP)  10.1039/D3GC04800D).
                                               4
 functionalised ZIF-8-NH    improvement in time for fi ltration. QbC   Y-J. Dong et al have referred to the   of TVFR for reactive crystallisation,   per gm. The C H /CH  uptake ratio was
                                                    3
                                                          4
                                                      8
 inherent insolubility of A in water and
       which requires handling of slurry. The
 2
 in a carboxylic polyimide   still has suboptimal performance. These   its easy degradation property. The title   example chosen was that of imination –   as high as 23.1, which to date is higher.  Australia’s Spodumene (S):
 for molecularly selective gas   authors have then adopted model-based   approach has been advocated leading to   p-hydroxybenzaldehyde reaction with   Theoretical calculations were done. The  Advances in Li extraction
 separation  QbC framework for commercial product.   enhanced performance. From the CSTR   p-fl uoroaniline. This type of reaction   recyclability is excellent and lends for   technologies, decarbonisation,
 The title method was adopted. Finally,   method to the title method resulted in   realises high shear stress and mixing   easy scale-up. (Ind. Eng. Chem. Res.,   and circular economy
 Q. Zhao et al have referred to the use of   the nominal temperature profi le gave the   2024; DOI: 10.1021/acs.iecr.3C04499).
 MMMs, which combine the advantages   desired product. (Org. Proc. Res. Dev.,   particle size decreasing from 166 to 66   efficiency. This ensures precise con-  A.H. Asif  et al have referred to the
 of polymers and inorganic materials, re-  2024; DOI: 10.1021/acs.oprd.3C00373).  nm. The preparation time was reduced   trol of nucleation and no adhesion is   Selective neodymium   abundance of Li in S (LiAl/(SiO ) ) and
                                                                                                    3 2
 sulting in higher gas permeability. There   from 60 min to 1 sec. The addition of   observed. (Org. Proc. Res. Dev., 2024;   (Nd) recovery from model   Australia has world’s largest reserves.
 are problems in the above combo mem-  Industrial cases of   PVP  avoids the agglomeration. The   DOI: 10.1021/acs.oprd.3C00369).  permanent magnets using   This review has covered in a comprehen-
 branes and the authors have mentioned   concomitant precipitation of   product so obtained had prolonged   cost-effective organic acid   sive way the current status of reserves
 how the membranes face problems   solid-state miscible product –   effi cacy and displayed a better killing   Phosphorus Ore Floating   system
 and to overcome hurdles co-polyimide   effect for Plutella Xylostella. (Ind. Eng.   Tailings (POFT): Treatment
 (6FBDA) was designed with carboxylate   Impurity phases in solution   Chem. Res., 2024; DOI: 10.1021/acs.  and disposal technology  C. Pozo-Gonzalo  et al have worked
 side groups to enhance the interfacial   crystallisation  iecr.3C03802).  Valorisation of phosphate rock, parti-  on the title subject as Nd is essential
 compatibility with amino-functionalised   F.L. Nordstrom et al have presented three   cularly lower grades, is done and froth   for making powerful magnets. The re-
 MOF (ZIF-8-NH ). They have explained   industrial case studies from the pharma   Ethylene purifi cation by PSA   fl oatation is carried out. There is a prob-  covery of Nd over iron (Fe) from their
 2
 how these combo membranes do a good   companies Boehringer-Ingelheim and   with the paraffi n selective   lem associated with the disposal of the   oxides is discussed. A variety of Deep
 job. The defect-free MMMs with 50 wt%   Merck & Co. Inc. where the title problem   MOF–DUT-8  tailings and hence valorisation should be   Eutectic Solvents (DES) were conside-
 MOF show CO  and H  permeability of   is encountered. They have explained the   [This column has covered some papers   considered. POFT has been widely used   red and the combination of guanidine
 2
 2
 80.8 Barrier and 127.5 Barrier, and with   underlying mechanism as to how the   on PSA for C H /C H  and C H /C H    in agriculture and industry fi elds, parti-  and their processing facilities. Several
 3
 8
 6
 3
 6
 2
 4
 2
 a CO /CH  and H /CH  selectivity of   impurities get incorporated via the Solu-  separation where the cryogenic distil-  cularly in fertilisers, soil remediation,   metallurgical processes are involved,
 4
 2
 4
 2
 89.4 and 141.7, respectively. (J. Mem-  bility-Limited Impurity Purge (SLIP) test.   lation systems are capital as well as   building materials, roadbed materials,   ranging from salt roasting to acid leach-
 brane Sci., 2024, 693, Feb., 122326;   Different approaches were made based on   energy intensive.]  etc. The concept of circular economy is   ing. However, here we have excessive
 DOI:10.106/jmemsci.2033.122326).  the prevailing solid-state miscibility, solid  V.V. Santana et al have come out with a   important. X. Li et al have reviewed this   pressure on reserves, energy, and waste
 Crystallisation  form landscape, and solvent solubilities.  new attractive strategy to have selective   subject. (Ind. Eng. Chem. Res., 2024;   management. Recent technological
 adsorption instead of C H    DOI: 10.1021/acs.iecr.3C02747).             advancements are covered. (Ind. Eng.
 2
 6
 Digital design of an   rather than C H  which is                         Chem. Res., 2024; DOI: 10.1021/acs.
 2
 4
 agrochemical crystallisation   the normal case and this   A robust Al-based MOF for   iecr.3C04048).
 process via two-dimensional   can lead to many benefi ts   highly effi cient Natural Gas
 population balance modelling   with respect to capital and   (NG) purifi cation  hydrochloride (GUC) and hydrogen  New membranes for
 (PBM)  recurring costs. Modelling       bond donors were less benefi cial for  dehydrating organic solvents
 was done and adsorption   Many NG have considerable content of  the leaching of Nd O  with a maximum
                                                         3
                                                       2
 W-L. Wu et al have referred to the prob-  equilibrium data were col-  ethane/propane/butane (more so in the  value of 78% in comparison with the  G. Ondrey has covered the recent deve-
 lem in solution crystallisation where   lected. DUT-8 was used   associated gas) and M. Chang et al have  individual system. In the absence of  lopment by Asahi Kasei Corp. of mem-
 needle shape crystals are formed which   at three temperatures and   come out with an Al-MOF, CAU-3-ND-  GUC the maximum dissolution was  brane for dehydrating solvents without
 168  Chemical Weekly  August 27, 2024  Chemical Weekly  August 27, 2024                               169
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