Page 155 - CW E-Magazine (24-6-2025)
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Special Report


       A rapid wrap-up of what’s new in Operations,

       Processes and Products


       Renewable Raw Materials


                                                                          of enhancing butanol productivity by up
                                                                          to 50% in the second stage. The overall
                                                                          sugar consumption of the two-stage
                                                                          packed-bed reactor with in-line gas strip-
                                                                          ping was 69%. (J. Chem. Technol. Bio-
                                                                          technol., 2024; DOI: 10.1002/jctb,7799).

                                                                          Conversion of sugarcane
                                                                          lignin (L) into renewable fuel-
                                                                          range cyclo-alkanes

                                                                          O.D. Saliu et al have used sugar-based
                                                                          triflate (mannose triflate) and AlCl  and in
                                                                                                    3
                                                                          situ supply of H  from propylene glycol to
                                                                                      2



       Enzymatic hydrolysis of           Provadis Hoschschule, BASF SE, and
       residual soybean oil with         hte GmbH, to get specially propylene
       simultaneous separation using     glycol (PG). The pretreatment as well
       membranes                         as the product purification were eva-
                                         luated. The annual requirements of PG,
       B.J.S. Pacheco et al have investigated   in 2022, was 1.9 mtpa; ethylene glycol
       the  simultaneous  separation  process   (EG) in 2023 at 28 mtpa and glycerol
       using a batch reactor coupled to a cellu-   in 2021 at 1 mtpa. This work refers to
       lose acetate membrane for the enzymatic   getting glycols from the carbohydrate   valorise L into renewable fuels. L conver-
       hydrolysis of residual soyabean oil.   wastes. (Chem. Ing. Technik, 2024; DOI:   sion of 98.5% was realised with particle
       The lipase was Pichig Pastoris and was   10.1002/cite.202300226).  size of 100 µm, and at temperature of
       used at 45°C and pH 7 in batches, with                             150°C. Lowest amounts of oxygenates
       and without simultaneous separation.  Enhanced biobutanol          and phenolics are formed and the
       Encouraging results are reported with  production from rice straw   highest yield of monocyclic alkanes was
       membrane. (Chem.Eng.Technol., 2024;  with a two-stage packed-bed   56 wt% corresponding to 79% selectivity.
       DOI: 10.1002/ceat.202400097).     fermenter coupled with in-line   The cycloalkanes are ethylcyclopentane,
                                         gas stripping
       Carbohydrate wastes to
       chemicals (CTC): From             C. Silvestre et al have
       second generation sugars to       worked on continuous
       glycols                           packed bed reactors
                                         containing clostridium
       G. Cusati et al have reported the title  beijerinckii DSM 6422
       work arising out of collaboration of  attached to support.
       Air Liquide Engineering & Construc-  Nutrient supplementation
       tion, Air Liquide Innovation campus,  was an effective method   Schematic diagram of two-stage PBR configuration with in-line GS


       Chemical Weekly  June 24, 2025                                                                  155


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