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@ARTICLE{Samsun:875365,
      author       = {Samsun, Remzi Can and Prawitz, Matthias and Tschauder,
                      Andreas and Meissner, Jan and Pasel, Joachim and Peters,
                      Ralf},
      title        = {{R}eforming of {D}iesel and {J}et {F}uel for {F}uel
                      {C}elles on a {S}ystems {L}evel: {S}teady-{S}tate and
                      {T}ransient {O}peration},
      journal      = {Applied energy},
      volume       = {279},
      issn         = {0306-2619},
      address      = {Amsterdam [u.a.]},
      publisher    = {Elsevier Science},
      reportid     = {FZJ-2020-01983},
      pages        = {115882},
      year         = {2020},
      abstract     = {The operation of fuel cell systems using liquid fuels
                      widens the application possibilities of this promising
                      energy conversion technology. However, systems utilizing
                      diesel and jet fuel reforming are fairly complex and suffer
                      from poor stability and limited dynamics. To address these
                      challenges, this paper investigates the steady-state and
                      transient operation of a 28 kWth fuel processor on the
                      systems level. With the help of experiments that make use of
                      the developed prototype, suitable operating parameters are
                      sought to maximize the simultaneous fuel conversion in the
                      reformer and CO conversion in the shift reactor.
                      Furthermore, a load change strategy is developed with the
                      aim of keeping the CO concentration at the fuel cell anode
                      inlet below the target concentration of $1\%$ of the wet
                      product gas at all times. The identified parameters enable
                      very high conversions $(>99.95\%)$ and CO concentrations
                      even lower than the target during steady-state operation
                      using three commercial fuels under full load. The developed
                      load change strategy was validated during 90 min tests,
                      including 16 load change cycles with loads between $40\%$
                      and $100\%.$ As well as providing excess steam during load
                      change, the selection and control of optimal O2/C and H2O/C
                      ratios and temperature levels proved to be of key
                      importance. In order to minimize the CO concentration, it is
                      recommended to operate the reformer at the identified
                      parameters for each fuel and keep the shift outlet
                      temperature between 295 and 300 °C by adjusting the water
                      feed. The proposed fuel processor concept and the
                      experimentally-validated operating strategies in this work
                      can enable the successful implementation of fuel cell
                      technology in different application areas, including
                      auxiliary power units, remote power systems and range
                      extenders.},
      cin          = {IEK-14},
      ddc          = {620},
      cid          = {I:(DE-Juel1)IEK-14-20191129},
      pnm          = {135 - Fuel Cells (POF3-135)},
      pid          = {G:(DE-HGF)POF3-135},
      typ          = {PUB:(DE-HGF)16},
      UT           = {WOS:000594115100005},
      doi          = {10.1016/j.apenergy.2020.115882},
      url          = {https://juser.fz-juelich.de/record/875365},
}