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Special Report


       High pressure molecular           intensification in view of the need   products were bicarbonates, unstable
       sieving of high-humidity          for  CO   removal  with  lower  energy   carbamates, etc. Their system consists of
                                               2
       C H /C H  mixture by a            consumption for recovery.]       tertiary amine diethanolamine (DEEA) as
              2
        2
           4
                 6
       hydrophobic flexible MOF          Computational study on CO        the main regent with several monoamines
       [This column has covered some papers   absorption mechanism and   2  as promoters. DEEA was combined with
       on adsorption-based separations for   structure-activity relationship   piperazine (PZ) and 4-amino-1-methyl-
       C H /C H  and C H /C H  in view of   in biphasic solvent           piperidine (PP) and gave a loading of
                     3
          4
             2
                            8
                          3
        2
                        6
               6
       high capital and energy costs associated                           0.988 mole CO  per mole amine. Regene-
                                                                                      2
       with cryogenic distillation. Adsorbents   F. Tang et al have referred to primary   ration duty was low at 2.14-GJ/t. (Chem.
                                                                                            st
       have been developed to even reverse the   amino groups showing stronger proton   Eng. Jl., 2024, 493, 1  August, 152699;
       selectivity for alkane vs alkenes.]  affinity than secondary ones, when poly-  DOI:10.1016/j.cej.2024, 152699).
                                         amines follow zwitterion mechanism.  Mass transport mechanism of
       Y-W.  Zhang  et  al  have  reported  a   It is stressed that the biphasic solvents
       flexible adsorbent showing molecular   are expected to improve the efficiency   nitrate selective nanofiltration
       sieving at ambient temperature and high   of CO  capture and reduce the energy   (NF) membrane on the basis
       pressure, even under high humidity. A   consumption  in  desorption  of  CO    of the Donnan stearic pore
                                              2
       high transition pressure of 16.6 atm, is   from loaded solutions. DFT calculation   model with dielectric exclusion
                                                                       2
       found for C H  at 25°C, and even more   were adopted. Selection of diamines   (DSPH-DE)
                2
                  4
       importantly C H  is completely excluded   is referred: 1,4 butanediamine (BDA)
                   6
                 2
       below the pore-opening pressure of 10   and  N-(2-aminoethyl)ethanolamine   N. Cevallos-Cueva et al have worked
       atm. (Angew. Chem. Intl. Ed.,2024; DOI:   (AEEA) with typical phase separation   on the troublesome problem of nitrate
       10.1002/anie.202317648).          promoters – 2-(diethylamino)ethano-   removal, whose discharge into waste
                                                                          streams is not allowed. The title stra-
       Magnetic nanoparticles            lamine (DEEA), and N,N,N’,N’’-penta-   tegy has succeeded in nitrate/sulphate
       (MNPs)-induced sorbent            methyldiethylenetriamine (PMDETA)   separation. Thin film composite mem-
       regeneration for Direct Air       were selected. (Chem. Eng. Jl., 2024,   branes were made having a polyamide
       Capture (DAC)                     493, 1 August, 152653; DOI:10.1016/   selective  layer. This  required  inter-
                                         j.cej.2024.152653).
       [This column has covered many papers on                            facial polymerisation of piperazine and
       removal of CO , including that from air,   Novel tri-solvent amines   trimesoyl chloride. (Chem. Eng. Jl., 2024,
                  2
       which is attracting some attention.]                               493, 1 August, 152775; DOI:10.1016/j.
                                         absorption for flue gas CO       cej.2024.152775).
                                                                    2
       Direct capture of CO  from air involves  capture: Efficient absorption
                       2
       considerable energy consumption. K.  and regeneration with low     1,3-Dioxalane (DO)
       Li et al have reported an effective and   energy consumption       production via reactive
       scalable adsorbent sorbent regeneration                            distillation (RD) combined
       method for liquid DAC solvents based  G. Li et al have synthesised a novel   with vapour permeation (VP)
       on MNPs heating with AC magnetic  tri-solvent amine absorbent. This system
       fields. MNPs can be directly heated to  gave  high  CO   loading  with  cyclic   S. Liu et al have reported the title process
                                                     2
       provide uniform and rapid volumetric  capacity. The regeneration heat duty was  to give 99.9 wt% DO in a new energy-
       heating. Aqueous solution of K-Sar-  reduced to 2.14-GJ/tCO . The reaction  saving  and  cost-reduction  process.
                                                            2
       cosinate was used to demonstrate the
       above method. MNPs can be used for
       several recycles. (AIChE Jl, 2024; DOI:
       10.1002/aic.18500).
       Absorption of CO ;
                         2
       Desorption of loaded amine
       solution
       [This column has covered several papers
       on this subject and this area continues
       to attract a lot of attention for further
       Chemical Weekly  February 11, 2025                                                              173


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