% IMPORTANT: The following is UTF-8 encoded.  This means that in the presence
% of non-ASCII characters, it will not work with BibTeX 0.99 or older.
% Instead, you should use an up-to-date BibTeX implementation like “bibtex8” or
% “biber”.

@ARTICLE{Burre:877458,
      author       = {Burre, Jannik and Bongartz, Dominik and Mitsos, Alexander},
      title        = {{P}roduction of {O}xymethylene {D}imethyl {E}thers from
                      {H}ydrogen and {C}arbon {D}ioxide—{P}art {II}: {M}odeling
                      and {A}nalysis for {OME} 3–5},
      journal      = {Industrial $\&$ engineering chemistry research},
      volume       = {58},
      number       = {14},
      issn         = {0888-5885},
      address      = {Columbus, Ohio},
      publisher    = {American Chemical Society},
      reportid     = {FZJ-2020-02211},
      pages        = {5567 - 5578},
      year         = {2019},
      abstract     = {Oxymethylene dimethyl ethers (OMEn) have high potential as
                      diesel fuels or blending components due to their promising
                      combustion properties and can be produced from hydrogen (H2)
                      and carbon dioxide (CO2) by combining existing process
                      concepts. However, such a process chain has not been
                      analyzed in detail yet, so its performance and bottlenecks
                      are unknown. In this second part of our two-part article, we
                      analyze a process chain for production of the longer chain
                      variant OME3–5 from renewable H2 and green CO2 via
                      trioxane and OME1. We simulate in Aspen Plus using detailed
                      thermodynamic models with coupled oligomerization reactions
                      and rigorous unit operation models. The overall exergy
                      efficiency of OME3–5 production from H2 and CO2 using
                      established process concepts is $53\%.$ Therein, the
                      trioxane process step has the highest losses due to its high
                      heat demand. Considering a pinch-based heat integration
                      throughout the entire process chain its total heat demand
                      can be reduced by $16\%.$ Thus, the exergy efficiency
                      increases to $54\%.$ This is still significantly lower
                      compared to the production of other alternative fuels like
                      OME1, methane, and dimethyl ether. Thus, more efficient
                      processes, e.g., by avoiding trioxane production, are
                      required},
      cin          = {IEK-10},
      ddc          = {660},
      cid          = {I:(DE-Juel1)IEK-10-20170217},
      pnm          = {899 - ohne Topic (POF3-899)},
      pid          = {G:(DE-HGF)POF3-899},
      typ          = {PUB:(DE-HGF)16},
      UT           = {WOS:000464769200023},
      doi          = {10.1021/acs.iecr.8b05577},
      url          = {https://juser.fz-juelich.de/record/877458},
}