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@ARTICLE{Klingberg:872611,
      author       = {Klingberg, Patrik and Wilkner, Kai and Schlüter, Markus
                      and Grünauer, Judith and Shishatskiy, Sergey},
      title        = {{S}eparation of {C}arbon {D}ioxide from {R}eal {P}ower
                      {P}lant {F}lue {G}ases by {G}as {P}ermeation {U}sing a
                      {S}upported {I}onic {L}iquid {M}embrane: {A}n
                      {I}nvestigation of {M}embrane {S}tability},
      journal      = {Membranes},
      volume       = {9},
      number       = {3},
      issn         = {2077-0375},
      address      = {Basel},
      publisher    = {MDPI},
      reportid     = {FZJ-2020-00104},
      pages        = {35 -},
      year         = {2019},
      abstract     = {The separation of carbon dioxide from coal-fired power
                      plant flue gases using a CO2/N2-selective supported ionic
                      liquid membrane (SILM) was investigated and the performance
                      and stability of the membrane during operation are reported.
                      The membrane is composed of a polyacrylonitrile (PAN)
                      ultrafiltration membrane as a support and a selective layer
                      of an ionic liquid (IL), 1-ethyl-3-methylimidazolium
                      bis(trifluoromethylsulfonyl)imide (EMIM Tf2N). The
                      feasibility of large-scale SILM production was demonstrated
                      by the formation of a square-meter-scale membrane and
                      preparation of a membrane module. A flat-sheet envelope-type
                      SILM module containing 0.67 m2 of the membrane was
                      assembled. Prior to real flue gas operation, the separation
                      behaviour of the membrane was investigated with single
                      gases. The stability of the SILM during the test stand and
                      pilot plant operation using real power plant flue gases is
                      reported. The volume fraction of carbon dioxide in the flue
                      gas was raised from approx. 14 vol. $\%$ (feed) to 40 vol.
                      $\%$ (permeate). However, issues concerning the membrane
                      stability were found when SO3 aerosols in large quantities
                      were present in the flue gas},
      cin          = {IEK-1},
      ddc          = {570},
      cid          = {I:(DE-Juel1)IEK-1-20101013},
      pnm          = {113 - Methods and Concepts for Material Development
                      (POF3-113)},
      pid          = {G:(DE-HGF)POF3-113},
      typ          = {PUB:(DE-HGF)16},
      pubmed       = {pmid:30836621},
      UT           = {WOS:000464144000001},
      doi          = {10.3390/membranes9030035},
      url          = {https://juser.fz-juelich.de/record/872611},
}