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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NGL natural gas liquid N np number of non‐particulate processing steps N OL number of operators per shift P number of processing steps where particulate solids are handled P average pressure PRI process route index psig pounds per square inch of gauge pressure ROI return on investment SCF standard cubic feet TAC total annualized cost TEG triethylene glycol TCI total capital investment ΔTCI change in total capital investment for a given additional case UFLmix upper flammability limit of a mixture VCi total variable cost for each process unit WCI working capital investment yr years ρ average fluid density

      1 1 Al‐Douri, A., Sengupta, D., and El‐Halwagi, M.M. (2017). Shale gas monetization – a review of downstream processing to chemicals and fuels. Journal of Natural Gas Science and Engineering 45: 436–455. https://doi.org/10.1016/j.jngse.2017.05.016.

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      9 9 Duran, L.M.J., 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.

      10 10 Ortiz‐Espinoza, A.P., Jiménez‐Gutiérrez, A., Noureldin, M., 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.

      11 11 Pérez‐Uresti, S.I., Adrián‐Mendiola, J.M., El‐Halwagi, M.M., and Jiménez‐Gutiérrez, A. (2017). A techno‐economic assessment of benzene production from shale gas. Processes 5: 33–42. https://doi.org/10.3390/pr5030033.

      12 12 Zhang, C. and El‐Halwagi, M.M. (2017). Estimate the capital cost of shale‐gas monetization projects. Chemical Engineering Progress 113: 28–32.

      13 13 Kidam, K., Sahak, H.A., Hassim, M.H. et al. (2016). Inherently safer design review and their timing during chemical process development and design. Journal of Loss Prevention in the Process Industries 42 https://doi.org/10.1016/j.jlp.2015.09.016.

      14 14 Roy, N., Eljak, F., Jiménez‐Gutiérrez, A. et al. (2016). A review of safety indices for process design. Current Opinion in Chemical Engineering 14: 42–48. https://doi.org/10.1016/j.coche.2016.07.001.

      15 15 Guillen‐Cuevas, K., Ortiz‐Espinoza, A.P., Ozinan, E. et al. (2018). Incorporation of safety and sustainability in conceptual design via a return on investment metric. ACS Sustainable Chemistry & Engineering 6: 1411–1416. https://doi.org/10.1021/acssuschemeng.7b03802.

      16 16 Hurme, M. and Rahman, M. (2005). Implementing inherent safety throughout process lifecycle. Journal of Loss Prevention in the Process Industries 18: 238–244. https://doi.org/10.1016/j.jlp.2005.06.013.

      17 17 Rahman, M., Heikkila, A.M., and Hurme, M. (2005). Comparison of inherent safety indices in process concept evaluation. Journal of Loss Prevention in the Process Industries 18: 327–334. https://doi.org/10.1016/j.jlp.2005.06.015.

      18 18 Leong, C.T. and Shariff, A.M. (2009). Process route index (PRI) to assess level of explosiveness for inherent safety quantification. Journal of Loss Prevention in the Process Industries 22: 216–221. https://doi.org/10.1016/j.jlp.2008.12.008.

      19 19 Johnson, J. (2016). U.S. Chemical Safety Board investigates Mississippi natural gas plant accident. Chemical & Engineering News.

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