Process Intensification and Integration for Sustainable Design. Группа авторов

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Process Intensification and Integration for Sustainable Design - Группа авторов

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2019).

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      20 20 Noureldin, M.M.B., Elbashir, N.O., and El‐Halwagi, M.M. (2014). Optimization and selection of reforming approaches for syngas generation from natural/shale gas. Industrial and Engineering Chemistry Research 53: 1841–1855. https://doi.org/10.1021/ie402382w.

      21 21 Martínez, D.Y., Jiménez‐Gutiérrez, A., Linke, P. et al. (2014). Water and energy issues in gas‐to‐liquid processes: assessment and integration of different gas‐reforming alternatives. ACS Sustainable Chemistry & Engineering 2: 216–225. https://doi.org/10.1021/sc4002643.

      22 22 Gabriel, K.J., Linke, P., Jiménez‐Gutiérrez, A. et al. (2014). Targeting of the water‐energy nexus in gas‐to‐liquid processes: a comparison of syngas technologies. Industrial and Engineering Chemical Research 53: 7087–7102. https://doi.org/10.1021/ie4042998.

      23 23 Julián‐Durán, L.M., Ortiz‐Espinoza, A.P., El‐Halwagi, M.M., and Jiménez‐Gutiérrez, A. (2014). Techno‐economic assessment and environmental impact of shale gas alternatives to methanol. ACS Sustainable Chemistry & Engineering. 2: 2338–2344. https://doi.org/10.1021/sc500330g.

      24 24 Ortiz‐Espinoza, A.P., Jiménez‐Gutiérrez, A., and El‐Halwagi, M.M. (2017). Including inherent safety in the design of chemical processes. Industrial and Engineering Chemistry Research 56: 14507–14517. https://doi.org/10.1021/acs.iecr.7b02164.

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      26 26 Ortiz‐Espinoza, A.P., Noureldin, M.M.B., Jiménez‐Gutiérrez, A., and El‐Halwagi, M.M. (2017). Design, simulation and techno‐economic analysis of two processes for the conversion of shale gas to ethylene. Computers and Chemical Engineering 107: 237–246. https://doi.org/10.1016/j.compchemeng.2017.05.023.

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      30 30 Stünkel, S., Illmer, D., Drescher, A. et al. (2012). On the design, development and operation of an energy efficient CO2 removal for the oxidative coupling of methane in a miniplant scale. Applied Thermal Engineering 43: 141–147. https://doi.org/10.1016/j.applthermaleng.2011.10.035.

      31 31 Pérez‐Uresti, S.I., Adrián‐Mendiola, J.M., El‐Halwagi, M.M., and Jiménez‐Gutiérrez, A. (2017). Techno‐economic assessment of benzene production from shale gas. Processes 5: 1–10. https://doi.org/10.3390/pr5030033.

      32 32 Agarwal, A., Sengupta, D., and El‐Halwagi, M. (2018). Sustainable process design approach for on‐purpose propylene production and intensification. ACS Sustainable Chemistry & Engineering 6: 2407–2421. https://doi.org/10.1021/acssuschemeng.7b03854.

      33 33 Jasper, S. and El‐Halwagi, M.M. (2015). A techno‐economic comparison between two methanol‐to‐propylene processes. Processes 3: 684–698. https://doi.org/10.3390/pr3030684.

      34 34 Babi, D.K., Holtbruegge, J., Lutze, P. et al. (2015). Sustainable process synthesis‐intensification. Computers and Chemical Engineering 81: 218–244. https://doi.org/10.1016/j.compchemeng.2015.04.030.

      35 35 Bertran, M.O., Frauzem, R., Sańchez‐Arcilla, A.S. et al. (2017). A generic methodology for processing route synthesis and design based on superstructure optimization. Computers and Chemical Engineering 106: 892–910. https://doi.org/10.1016/j.compchemeng.2017.01.030.

      36 36 Lutze, P., Babi, D.K., Woodley, J.M., and Gani, R. (2013). Phenomena based methodology for process synthesis incorporating process intensification. Industrial and Engineering Chemistry Research 52: 7127–7144. https://doi.org/10.1021/ie302513y.

      37 37 Castillo‐Landero, A., Jiménez‐Gutiérrez, A., and Gani, R. (2018). Intensification methodology to minimize the number of pieces of equipment and its application to a process to produce dioxolane products. Industrial and Engineering Chemistry Research 57 (30): 9810–9820. https://doi.org/10.1021/acs.iecr.7b05229.

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      40 40 Castillo‐Landero, A., Ortiz‐Espinoza, A.P., and Jiménez‐Gutiérrez, A. (2019). A process intensification methodology including economic, sustainability and safety considerations. Industrial and Engineering Chemistry Research 58 (15): 6080–6092. https://doi.org/10.1021/acs.iecr.8b04146.

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