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Special Report                                                                   Special Report


 Ligand-engineered Zr-  enantiomeric excess of 26% is reported.
 MOF membranes with fast   By adopting fi ve-stage counter-current
 water transport channels for   extraction and reverse extraction the ee
 alcohol-water solution  value could be improved to 91%. Mole-
       cular simulations were done. (AIChE Jl.,
 B. Mo et al have reported that MOF   2024; DOI: 10.1002/aic.18367).
 membranes with rich functionality and
 a tuneable pore system are promising for   Absorption of methyl
 molecular separation. Aperture size can   mercaptan (MM)
 be manipulated to allow fast and selec-
 tive permeation of water over alcohol   P. Liang et al have screened physical sol-
 molecules. Thus butanol/water separa-  vents using quantum chemical calcula-
 tion was performed with total fl ux of   tions coupled with experiments. DMSO,
 5,226-gm m hr  and separation factor   Sulfolane (SLL), propylene carbonate   with polymer RO membranes. RO mem-  acid works for Sn with high selectivity.
 -1
 -2
 -1
 of 1,281, and water content of 99.3% in   (PC), DMF and NMP were considered   branes having assumed hypothetical per-  Thus FA-ChCl extracted Cu and Fe at
 the permeate. (AIChE Jl., 2024; DOI:   using the COSMO-RS model. The order   meance values for ethanol 0.1 time and  100°C. Oxalic acid (1M) removed Sn
 heat and pressure, particularly for pharma  are different from commercial-scale dis-  10.1002/aic.18368).  was NMP> PC> DMSO> SLL> DMF.   water of 2 times proved to be feasible  at 80°C. (ChemSusChem, 2024; DOI:
 applications. This is based on forward-os-  tillation. Column internals and column   The treatment of sour natural gas which   to realise lower energy consumption.  10.1002/cssc.202301418).
 mosis system, which uses a hollow fi bre  sizing software are discussed. Pumps,   Experimental and   contains H S, COS, CH SH is discussed.   (J. Chem. Eng. Japan, 2024, 57, Issue1;
               2
                         3
 membrane module and a draw solution.  flowmeters, control valves, types of   computational studies on   (ACS  Omega,  2023;  DOI:  10.1021/  DOI: 10.1080/00219592.2023.2294934).
 Thus water is removed without the loss  trays and packing are different in pilot   isolation of cardanol from   acsomega.2C06173).  Thermally self-suffi cient heat
 of APIs. Highly soluble liquids like THF,  facilities. Appropriate sample points   Green Deep Eutectic Solvents   pump-assisted azeotropic
 toluene or methanol can bring down water  or overline analyses capabilities and   Cashew Nut Shell Liquid   Analysis of RO separation   (DESs) for sustainable   dividing-wall column (DWC)
 content below 1,000-ppm without apply-  instrumentation have to be provided.   (CNSL) using diethanolamine   performance of ethanol (E)   for biofuels recovery from
 ing heat or pressure. A variety of solvents  Flexibility has to be provided. Aspects  (DEA) based deep eutectic   water mixtures and design   recovery from thermally   isopropanol-butanol-ethanol
 can be handled. (Chem. Eng. Magazine,  of high-vacuum operation, heat con-  solvent at different molar   of ethanol concentration   treated PCBs: A greener   (IBE) fermentation
 2024, Feb.).  trol, refl ux control, distillate and side  ratios  processes  alternative to conventional
 stream product are discussed. Glass     methods                          T. Jankovic et al (Prof. A.A. Kiss and
 Innovations in pilot-plant   Oldershaw-style trays are commonly  V. Malaiyarasan et al have amine-based   coworkers) have reported that IBE
 distillation process design  used; “off-the-shelf” components in  Deep Eutectic mixture composed of   Ethanol production via fermentation  S. Mishra  et al have worked on the   fermentation is superior to acetone-
 the range of dia from 28 to 100 mm are  choline chloride with DEA-based hydro-  has witnessed meteoric rise and here the  waste PCBs, the core of e-waste, which   butanol-ethanol (ABE) due to better pro-
 G. Graham and R. Rocks, AVP Corp.,  referred; scale-up is facilitated by pilot  gen bond donor in different mole ratios.   concentration of E rarely crosses 12%  are rich in Cu, Sn, Zn, Fe, and Ni, to   perties. A novel thermally self-suffi cient
 have reported specific concerns in  facilities. (Chem. Eng. Magazine, 2024,  Ethyl acetate and MIBK could be used   and energy consumption constitutes an  recover these valuable metals. PCBs   and eco-effi cient downstream process
 small-scale distillation processes which  Feb. issue).  as co-solvents. Temperature was varied   important factor in making azeotropic  from mobile phones were treated with   is reported for a 74,000-tpa capacity
 from 20°C to 70°C at 1 atm. Thermal   mixture and absolute. E.K. Akamatsu  Choline Chloride based DESs. Formic   from a highly dilute broth having over
       et al have successfully analysed the  acid (FA)-ChCl had maximum solubility
 stability of the solvent was checked.   RO separation performances of E/water  of Cu, Fe, and Ni, while urea-ChCl had   97 wt% water. Gas stripping and heat
 Cardanol extraction details are given. (J.   mixtures, with E conc. from 1-37 wt%,  high Zn selectivity and solubility. Oxalic   pump-assisted vacuum evaporation was
 Chem. Technol. Biotechnol., 2024; DOI:                                   implemented for the products from the
 10.1002/jctb.7612).                                                      broth. An advanced highly integrated
                                                                          heat-pump assisted azeotropic DWC
 Enhancement of separation                                                was designed to give high purity (99%
 performance for ofl oxacin (O)                                            wt) butanol and isopropanol-ethanol
 enantiomers by a biphasic                                                fuel supplement (89 wt%). It is cost
 recognition chiral extraction                                            effective at $0.130/kg IBE and energy
 (BRCE) system                                                            consumption of 0.673 KWeh/kg IBE.
                                                                          Full recycle of biomass and most
 J. Li et al have worked on separation of                                 of the separated water is reported.
 enantiomers via BRCE. The case study                                     (Chem. Eng. Processing – Process
 of O was taken using beta-cyclodextrin                                   Intensification, 2024,197, March,
 as hydrophobic and hydrophilic selec-                                    109689; DOI:10.1016/j.cep.2024.
 tors. Enantioselectivity value of 2.4 and                                109689).


 170  Chemical Weekly  August 27, 2024  Chemical Weekly  August 27, 2024                               171


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