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Special Report                                                                   Special Report


 A novel non-aqueous   Facile design of continuous   series of hydroxylated compounds (e.g.,   from adsorptive separation. MX/PX, for  required to solve this problem resulting   the carrier for removing H-acid (1-amino-
 absorbent of amino   counter-current, dual fl ow,   alcohol and phenolic compounds). The   MX, was originally done via alkylation/  in economic benefits. Biology-based   8-naphthol-3,6-disulphonic acid)
 functionalized ionic liquid   and capture SMB adsorptive   poly(METAC:1-butanol) polymer exhi-  dealkylation with isobutylene but in the  processes are under implementation,   Compared to non-imprinted polymer
 (AFIL) for effi cient CO    processes  bited the highest adsorption capacity of   recent past adsorptive separation has  e.g., in Sydney, Australia, 3000-tonnes   (N/P), H-SIP exhibited superior salt
 capture  2  46 ±5mg per gm and 46 ±4per gm Co and   been commercialized for MX.]  of waste could give 0.5-tonnes of gold   resistance in the presence of Na SO , 20
                                                                                                      4
                                                                                                   2
 [This column has covered many papers   Protein-based therapeutics have gained a  Ni, respectively, which compete with   X. Cui et al have come out with an interes-  and 800-tonnes of Cu. The start-up is   to 80 mg/L. High selectivity of H-acid/
                                                                          T-acid or H-acid/2-NSA is reported.
                                         concentrating on printed circuit boards
 on CO  absorption/desorption includ-  lot of importance, and their purifi cation  conventional materials. Deionized water   ting and potentially useful way of sepa-  (PCBs). 1-tonne of PCBs contains at   Elution was done with aq. NaOH. (Can.
 allowed highest desorption effi ciency,
 2
 ing new amines, catalysing desorption,   involves SMBC.   which makes the process “greener” and   rating MX, which exploits the differences  least 200-kg Cu, 0.4-kg silver, and 0.09-kg   J. Chem. Eng., 2024; DOI: 10.1002/
 etc. and the subject continues to attract   G. Carta, who have made many valuable   highly cost effective. (New Jl. of Chemis-  in molecular length and alkyl distribution  gold. Biological processes are under   cjce.25432).
 attention.]  contributions in this area, has opined that   try, 2024; DOI: 10.1039/D4nJ02316A).  among xylenes. These authors have pro-  consideration even for Nd from magnets.
 W. Zhao et al have reported the use of   multi-column system as well as systems   vided a length-matched MOF, formulated   Leveraging liquid-liquid
 [TETAH][3-Br-PhO]-PEG200 in dif-  where the load fl ow rate varies over time,  Liquid-Liquid Extraction   as Al(OH)[O C-C H O-CO ], featuring an  The Royal Mint in UK is using cut-  extraction (LLE) for
                2
                           2
                      2
                    4
 ferent proportions for absorbing CO .   can be employed to improve producti-  (LLE) for in-situ carboxylic   effective pore size corresponding to MX  ting-edge chemistry to extract gold from   contaminant removal
 2
 The absorption mechanism has been   vity and reduce consumption of systems   acid recovery via continuous   molecular length combined with multiple  PCBs in minutes. Metals make up close to
 elucidated using  C NMR and FTIR   under mass transfer control condition   membrane-based emulsion   negative O hydrogen bond donors distri-  half of an average smartphones weight   D.J. Glatz and B. Cross have referred to
 13
 spectroscopy. The results indicate that   using a mechanistic mode. This work   separation  bution for preferential separation of the  (minus the battery). Gold and Pd content   the use of LLE for removing a variety
 25°C and mass ratio of 3:7 leads to   provides the means to rapidly design   intermediate-size MX, from the tertiary  are low, but it is still valuable.  of contaminants in wastewater, some
 absorption capacity to 2.37 mol per kg.   periodic counter-current, dual flow  Y. Chen et al have referred to some   o-, m-, p- X mixture. MX uptake was re-  of which are refractory/untreatable. In
 Desorption was done at 120°C. (Chem.   capture system. (J. Chem. Technol. Bio-  in situ LLE of fermentation products   cord high and selectivity for MX/PX was  Flash joule heating involves applying   recent years, the US EPA has identi-
 Eng. Res. Des., 2024, 209, Sep.,102-110;   technol., 2024; DOI: 10.1002/jctb.7716).  posing emulsion formation problems.   5.3. Both vapour- and liquid phase fi xed  an intense sub-second pulse of electric   fi ed compounds that are classifi ed as
 DOI: 10.1016/j.cherd.2024.07.057).  Ionic polymer absorbents   Membrane contactors are useful but   bed tests confi rmed the above separation.  current to chopped-up waste, resulting in
 Effi cient purifi cation of   inspired by deep eutectic   require a large membrane area. These   (Angew. Chem. Intl. Ed., 2024; DOI:  heating up to more than 2700°C, which
 authors have reported that a hydrophobic
 butanone and ethyl acetate   solvents to recover Co and Ni  polytetrafl uoroethylene (PTFE) mem-  10.1002/anie.204008817).  vaporises metals which are condensed
                                         or dissolved into low-concentration HCl
 from wastewater by extractive   [This column has covered some papers   brane-based emulsion separator (MBES)   Recovery of valuable   for separation. (Chem. Eng. News, 2024,
 distillation  on the recovery of Co, Ni, etc. from used   enables continuous LLE for the recovery   materials from electronic   29  July, 26-31).
                                           th
 batteries to fi ll the gap in the availability   of an exemplary fermentation product,
 Z. Ma et al have reported optimisation   of the critical Co.]  butyric acid, with improved throughput.   waste
 of the title separation-based on cost,   The permeate fl ux of 290 litre per sq. m   Selective adsorption of
 thermodynamic and environmental  H. Bastos et al have come out with a   per hr with single-stage MBES system   P. Patel has covered this subject as the  aromatic sulfonic acid
 analysis. The wastewater containing  new strategy of using ionic polymers   was calculated to be 1450 gm per sq.   world is drowning in electronic waste   (ASA) from wastewater   emerging contaminants, which include
 both butanone and ethyl acetate form a  for the recovery of Co and Ni from   m. per hr, which is much higher than   and it seems that the fl ood of e-waste   using a surface imprinted   steroids, hormones, endocrine-disrupt-
 ternary azeotrope and extractive distil-  recovery solutions. Such ionic polymers   the 9 gm per sq. m. per hr realised in a   generated in 2022 contained $91-bn   ing compounds, pharma and personal
 lation was adopted. Four solvents were  were made, e.g., by simple and fast   membrane contactor, resulting in very   worth of valuable metals and 40% of   polymer (SIP); H-acid as a   care products. Two types of LLE are
 analysed. (Chem. Eng. Res. Des., 2024,  photopolymerisation process combin-  good economics. (Green Chem., 2024;   those metals end up in a land fi ll or were  representative contaminant  considered: Solvation extraction (SE)
 208, August, 782-794; DOI: 10.1016/j.  ing [2-(methacryloxy)ethyl][trimethyl   DOI: 10.1039/D4GC02772H).  burned in incinerators or disposed of in   and solvation with reaction extraction.
 cherd.2024.07.048).  ammonium chloride] (METAC) with a   uncontrolled ways. Only 4% of some  The separation of ASAs from waste-  Here SE uses a solvent with a lower
 Highly effi cient separation of   metals were recovered. [The average  water is problematic and more so as it is  boiling point than water. The raffi nate
 intermediate-size m-xylene   person in the US threw away 21-kg of  refractory and not biodegradable. J. Yao  phase leaving the extraction column
 (MX) from xylenes via   electronics in 2022.] Innovative ways are  et al have reported PEI/Cl-PS-DVB as  will contain the amount of solvent that is
 a length-matched Metal                                                   soluble in water and a stripping column
                                                                          recovers this solvent. (Chem. Eng. Prog.
 Organic Framework (MOF)                                                  (of AIChE), June 2024).
 with optional oxygen sites
 distribution                                                             Advances in crystallisation
 [Separation of xylene isomers – o-, m-,                                  and precipitation technologies
 p- – is of great industrial importance as                                for biotherapeutics
 pure OX can be separated by distillation
 but MX and PX separation poses prob-                                     M.D.C.P. Royo et al have discussed the
 lem. Initially, and lately again, crystal-                               title subject and have referred to the
 lization was used to get pure PX, apart                                  characteristics of biotherapeutics which


 170  Chemical Weekly  March 25, 2025  Chemical Weekly  March 25, 2025                                 171


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