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@PHDTHESIS{Otto:478446,
      author       = {Otto, Alexander},
      othercontributors = {Stolten, Detlef and Palkovits, Regina},
      title        = {{C}hemische, verfahrenstechnische und ökonomische
                      {B}ewertung von {K}ohlendioxid als {R}ohstoff in der
                      chemischen {I}ndustrie},
      volume       = {268},
      school       = {Zugl.: Aachen, Techn. Hochsch.},
      type         = {Dissertation},
      address      = {Jülich},
      publisher    = {Forschungszentrum Jülich, Zentralbibliothek},
      reportid     = {RWTH-2015-02637},
      isbn         = {978-3-95806-064-7},
      series       = {Schriften des Forschungszentrums Jülich : Reihe Energie
                      $\&$ Umwelt},
      pages        = {VIII, 272 S. : graph. Darst.},
      year         = {2015},
      note         = {Zugl.: Aachen, Techn. Hochsch., Diss., 2015},
      abstract     = {The utilisation of CO2 as feedstock in the chemical
                      industry represents an alternative to the geological
                      storage, which is legally limited and socially debated.
                      Generally, scientific publications about the utilisation of
                      CO2 in chemical reactions typically address the feasibility
                      of the syntheses without paying attention to the CO2
                      reduction potential or the economy in contrast to the
                      conventional process of production. The aim of this doctoral
                      thesis is to identify chemical reactions with CO2 as
                      feedstock, which have the potential to reduce CO2 emissions.
                      These reactions are evaluated concerning the industrial
                      realization, CO2 balance and economy compared to the
                      conventional processes. To achieve this, 123 reactions from
                      the literature were collected and evaluated with the help of
                      selection criteria developed specifically for this
                      application. The criteria consider both, the quantitative
                      potential to reduce CO2 and possible economical interests in
                      these reactions. Additional to the process of the evaluation
                      of the reactions, a CO2 reduction potential of 1.33 $\%$ of
                      the greenhouse gas emissions within the European Union could
                      be calculated. For the chemicals formic acid, oxalic acid,
                      formaldehyde, methanol, urea and dimethyl ether, which most
                      fully satisfy the selection criteria, a direct comparison of
                      the CO2 based process with the conventional process is
                      performed. By literature data, process designs, and
                      simulations, it has been shown that the highest reductions
                      of CO2 emissions can be achieved for methanol with 1.43
                      kgCO2/kgMeOH and dimethyl ether with 2.17 kgCO2/kgDME, but
                      only with the assumption that the necessary hydrogen for the
                      CO2 based reaction is produced by electrolysis operated with
                      renewable energy. Overall, the CO2 based production
                      processes of methanol and dimethyl ether could reduce 0.059
                      $\%$ of the greenhouse gas emissions of the European Union
                      (EU) if all conventional processes are substituted in the
                      EU. Finally, for the CO2 based processes of methanol and
                      dimethyl ether it could be shown that the manufacturing
                      costs are 3.3 or 2.9 times higher than for the corresponding
                      conventional processes. The result of this are CO2 abatement
                      costs of 540 €/tCO2 for the CO2 based production of
                      methanol and 440 €/tCO2 for dimethyl ether. These
                      abatement costs are respectively 90 and 73 times higher than
                      for the geological storage of CO2. For the case, that the
                      production costs for the necessary hydrogen decrease from
                      5.22 to 1.22 or 1.76 €/kgH2 no abatement costs are
                      necessary.},
      cin          = {413010 / 155310 / 150000},
      ddc          = {620},
      cid          = {$I:(DE-82)413010_20140620$ / $I:(DE-82)155310_20140620$ /
                      $I:(DE-82)150000_20140620$},
      typ          = {PUB:(DE-HGF)11 / PUB:(DE-HGF)3},
      urn          = {urn:nbn:de:hbz:82-rwth-2015-026378},
      doi          = {10.18154/RWTH-2015-02637},
      url          = {https://publications.rwth-aachen.de/record/478446},
}