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Special Report


 self-fl ush the crystalline salt and assure  separation retention time (+40%). This  dissolution is an attractive pro-
 the stability of this passive system.  work demonstrates the capability of the  cess. (ACS Sustainable Chem. Eng.,
 There is zero discharge and can stably  title strategy. (Angew. Chem. Intl. Ed.,  2024; DOI: 10.1021/acssuschemeng.  Bharat Jyoti Impex
 desalinate 70 gm per/litre NaCl solution  2024; DOI: 10.1002/anie.202416884).  4C0480).
 with water yield of 1.33 kg per sq. m.   AVAILABLE REGULARLY
 per hr. and salt collection of about  Rare-earth elements (REE)   Design and hydrodynamics    Acetophenone   Acetyl Acetone   Acrylonitrile   Adipic Acid    Methyl Iso Propyl Ketone   Methyl Propyl Ketone
 0.34 kg per sq. m. per hr. at 60°C. This  recovery from electronic waste  of a novel multidowncomer    Allyl Alcohol   Allyl Chloride   Allylamine   Alpha-Methyl Styrene    Methyl Salicylate   Methyl Stearate   Methyl Stearate / Palmitate
 is adoptable for large-scale commercial   bubble-breaking (MDBB) tray   4 Amino Phenol   Amino Ethyl Ethanol Amine    2 Methyl THF   Methyl Tin Mercaptide   Mono Cyclohexylamine
 production. (Chem. Eng. Jl., 2024, 498,  E. Sanchez Moran et al have referred    Amino Guanidine Bicarbonate   Anisole   Antimony Trioxide 99.8%    Mono Ethyl Amine 70%   Mono Isopropylamine 70% / 99%
 15 Oct., 155095; DOI: 10.1016/j.cej.  to REEs as possessing unique magnetic,  W. Wang et al have come out with a    Azelaic Acid   Barium Carbonate   Barium Nitrate 99%    Monoglyme   N Butyraldehyde   N Ethyl Pyrrolidone
         1,2,3-Benzotriazole   1,2,3 Benzotriazole 99.5%
                                                           N Pentane 95%   N Vinyl Pyrrolidone
 2024.155095).  luminescent, and catalytic properties and  novel MDBB which is based on the    Benzoyl Chloride [99.5%] China   Biphenyl    N,N Dimethyl Cyclohexylamine   N,N-Dicyclohexyl Carbodiimide
 are thus seen as key resources for di-  “droplet bubble-breaking” method to    Boron Trifluoride Etherate   1,3-Butane Diol    N,O-Bis (Tri Methyl Silyl) Acetamide
 Mechanochemical “Cage-On-  verse applications, such as in electronic  enhance  the  mass  transfer  process.    1,4 Butane Diol [DAIREN]   2 Butyne 1,4 Diol    NACOL 10-99% (N Decanol) SASOL Germany
 MOF” strategy for enhancing   devices, industrial components, mili-   Caproic Acid   Cerium Oxide   Cesium Carbonate    NACOL 6 99% (N Hexanol)   NACOL 8 99% (N Octanol)
                                                           N-Amyl Alcohol (N-Pentyl Alcohol)   N-Butyl Amine
         Cetyl Chloride   CIS-2-Butene-1,4-Diol   Crotonic Acid
 gas adsorption and separation   tary defence equipment, etc. Electronic    Cyanuric Chloride   Cyclohexanol   Cyclopentanone    N-Decanol   N-Heptane 99%   N-Hexane 99%
 through aperture matching  (e-) waste constitutes a rich source of    Cyclopropylamine   D - Tartaric Acid   D-Camphor Sulphonic Acid    N-Hexyl Alcohol (99% & 98%)   Nitro Ethane
 REEs. These authors have carried out    Di Cyclohexylamine   Di Ethyl Ketone   Di Ethyl Malonate    Nitro Methane   N-Methyl 2 Pyrolidone   N-Methyl Piperazine
 Y. Liang et al have worked on getting  a technoeconomic analysis (TEA) and    Di Ethyl Sulphate   Di Iso Butyl Ketone [DIBK]    N-Pentane 99%   1-Octanol (C8)   1-Octene
         Di Methyl Acetamide [Henan Junhua]   Di Methyl Malonate
                                                           Ortho Chloro Benzaldehyde   Para Benzoquinone
 more out of adsorptive separations  reduce environmental impact of land    Di Phenyl Carbonate   Di Sodium Phosphate Anhydrous    Para Chlorobenzaldehyde   Para Cresol
 and post-modifi cation of porous mate-  fi lling. Thus the recovery of didymium    2,4 Di Tertiary Butyl Phenol   Dibasic Ester    Para Hydroxybenzaldehyde   Paraformaldehyde 96%
 rials with molecular modulators is of  oxide (DO) recovery from hard drive    DIBOC (Di Tert. Butyl Dicarbonate)    Pelargonic Acid   Perchloric Acid
 importance. These authors have the  shreds through acid-free dissolution    Dibromomethane (Methylene Di Bromide)   Dicyclopentadiene    Petroleum Ethers 40-60 / 60-80 / 80-100 / 100-120 etc.
                                                           Phenyl Ethyl Alcohol   Phenyl Ethyl Amine [ R+ ; DL ]
         Di-Ethyl Carbamyl Chloride   Diethyl Hydroxylamine
 mechanochemical “Cage-On-MOF”  recycling is covered. An analysis  Hydrodynamic parameters were studied    Diethyl Oxalate   Diglyme   Diisobutylene   Diisopropylamine    Phosphorous Pentoxide   Pivaloyl Chloride
 strategy, utilising porous coordination  shows that 342.42 tonnes of hard drive  with respect to gas-liquid fl ow pattern,    Diisopropyl ethylamine   Diisopropyl Succinate    Potassium Bi Carbonate   Potassium Persulphate
 cages (PCCs). Only the combinations  shreds per year allows recovery of  gas holding, dry pressure drop, clear    2,2-Dimethoxy Propane   Dimethyl Oxalate   Di-N-Propyl Amine    Potassium Tertiary Butoxide   Potassium Thioacetate
 of PCCs and MOFs with closely  DO at 2.53 tonnes  whose estimated  liquid height, residual pressure drop,    DL Alfa Phenyl Ethyl Amine   D-Ribose   DMSO (Hubei Xingfa)    Propionaldehyde   Propionic anhydride
 matched aperture sizes exhibited en-  price is $130/kg. The minimum sell-  and wet pressure drop. CO  absorption    Ethyl Benzene   Ethyl Cyclo Hexane   2 Ethyl Hexyl Bromide    Pyrogallol   2-Pyrrolidone   Quinoline   Resorcinol (China)
                                                           Salicylic Acid Technical / Pure   Secondary Butanol (China)
         2-Ethylhexyl Thioglycolate   Ethyl Nicotinate
 2
 hanced gas adsorption and separation  ing price, with improvements, can  experiment were done for comparing    Ethylene Glycol Diacetate (EGDA)   Fluorobenzene   Formamide    Sodium Dichloroisocyanurate (56%) Granule
 performance. MOF-808@PCC-4 exhi-  reach $173/kg. A comparison of the  traditional sieve trays, multidowncomer    Formic Acid 99%   Fumaric Acid   Furfuraldehyde   Furfuryl Alcohol    Sodium Diethyldithiocarbamate   Sodium Ethoxide
 bited a significantly increased C H   hydrometallurgical and electrometal-  trays and MDBB and MDBB showed    Furfurylamine   Gamma Amino Butyric Acid (4 Amino Butyric Acid)    Sodium Ethoxide solution in Ethanol / Methanol
 2
 2
 uptake (+64%) and a longer CO /C H   lurgical process indicates that acid-free  improved performance. (Ind. Eng.    Gamma Butyrolactone   Glutaraldehyde 50%   Glycine    Sodium Methoxide   Sodium Sulphite (Aditya Birla -Thailand)
 2  2  2   Glycolic Acid 70%   Glyoxal 40%   Glyoxylic Acid 50%    Sodium Sulphite 98%   Sodium Sulphite Tech 90%
 Chem. Res., 2024; DOI: 10.10214/acs.   Guanidine Carbonate   Guanidine HCl   Guanidine Thiocyanate    Sodium Tertiary Butoxide   Sorbitol Powder   Stearyl Bromide
 iecr.4C03090).   Guanine   Heptane [mix]   1,6-Hexane Diol   Hippuric Acid    Stearyl Palmitate   Strontium Carbonate   Succinic Acid
         12 Hydroxy Stearic Acid   Imidazole   Isobutylamine    Succinic Anhydride   Sulfolane Anhydrous
 Regeneration of LiFePO  from    Iso Octa Decyl Alcohol   Isovaleraldehyde   Itaconic Acid    Tert. Butyl Amine   Tertiary Amyl Alcohol
         L + Tartaric Acid   Lactic Acid   Lanthanum Carbonate
                                                           Tertiary Butyl Acetate   Tetraglyme (Tetra Ethylene Glycol)
 spent materials  4   Lauric / Myristic / Palmitic / Oleic / DCFA / Caprylic Acid    Tetra Hydro Furfuryl Alcohol   THF (Dairen, Nan Ya)
         Lithium Aluminium Hydride   Lithium Amide       Thioacetamide   Thiocyanates: Ammonium / Sodium / Potassium
 S. Song  et al have emphasized the    Lithium Carbonate   Lithium Carbonate [Equivalent to I.P.]    Thioglycolic Acid 80%   TMOF / TEOF / TMO Acetate
 importance of recycling and regene-   Lithium Hydroxide   Lithium Hydroxide Anhydrous    Tolyl Triazole   Tolyltriazole Granular   Tri Ethyl Citrate
 ration of LiFePO for sustainable    Lithium Hydroxide Monohydrate LIOH : 57.7% Min    Tri Fluoro Acetic Acid   Tri Fluoro Acetic Anhydride
                                                           2,2,2 Tri Fluoro Ethanol   2,2,2-Tri Fluoro Ethylene
         Lithium Metal 99% / 99.9%   L-Proline   M. P. Diol
 4
 development and even environmental    Malonic Acid   Malononitrile   Maltol   Meta Cresol 99.5%    Tri Isodecyl Stearate   Triacetin (Glycerine Triacetate)
 protection. The infl uence of Al impurity    Meta Hydroxy Benzoic Acid   Meta Para Cresol [Meta 60%]    1,2,4-Triazole & its Sodium Salt
 is discussed  with respect  to  electro-   Methyl Amyl Ketone   Methallyl Chloride   1 Methoxy Propanol    Trichloroisocyanuric Acid 5-8 Mesh,100-120 Mesh
 chemical performance of regenerated    1-Methoxy Propyl Acetate   Methyl Cellosolve   Methyl Cyclohexane   Triethyl Ortho Acetate   Triethylsilane
         Methyl Glycol   1-Methyl Imidazole   2-Methyl Imidazole
                                                           Triisobutyl Phosphate   Tri-N-Butyl Phosphate
 LiFePO . Leaching was done with    Methyl Iso Butyl Carbinol [MIBC]   Methyl Isoamyl Ketone    Triphosgene   Triss Buffer   2,6-Xylidine
 4
 150 gm/litre of H SO ; Al  removal
 4
 2
 and control was achieved by simply      Bharat Jyoti Impex
 adjusting the pH value. The recovered   “Jasu”, Ground Floor, 30, Dadabhai Road, (Near CNM School), Vile Parle (West), Mumbai 400 056.
 product exhibits excellent performance.   Phone: +91 91528 33394 & +91 91524 33394  Whats App:. +91 99300 51288
 (ChemSusChem., 2024; DOI: 10.1002/  Email: info@bharatjyotiimpex.com  Website: www.bharatjyotiimpex.com
 cssc.202401432).  More than 2000 CheMiCals in sMall PaCking
 164  Chemical Weekly  May 13, 2025  Chemical Weekly  May 13, 2025                                     165

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