Process Intensification and Integration for Sustainable Design

4 4 Bullin, K.A. and Krouskop, P.E. (2009). Compositional variety complicates processing plans for us shale gas. Oil & Gas Journal 107: 50–55.

5 5 Martini, A.M., Walter, L.M., and McIntosh, J.C. (2008). Identification of microbial and thermogenic gas components from Upper Devonian black shale cores, Illinois and Michigan basins. AAPG Bulletin 92: 327–339. https://doi.org/10.1306/10180706037.

6 6 Kidnay, A.J., Parrish, W.R., and McCartney, D.G. (2011). Fundamentals of Natural Gas Processing, 2e. Boca Raton: CRC Press.

7 7 Farley, T. and Hutchinson, T. (2018). Overcome engineering challenges for multi‐well gathering facilities. Gas Processing News. http://www.gasprocessingnews.com/features/201404/overcome-engineering-challenges-for-multi-well-gathering-facilities.aspx(accessed 1 August 2018).

8 8 Khan, F.I. and Amyotte, P.R. (2005). I2SI: a comprehensive quantitative tool for inherent safety and cost evaluation. Journal of Loss Prevention in the Process Industries 18: 310–326. https://doi.org/10.1016/j.jlp.2005.06.022.

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. https://cen.acs.org/articles/94/i28/US-Chemical-Safety-Board-investigates.html(accessed 1 August 2018).

20 20 BP (2018). BP Energy Outlook, 2018e. BP.

21 21 AlNouss, A., Ibrahim, M., and Al‐Sobhi, S.A. (2018). Potential energy savings and greenhouse gases (GHGs) emissions reduction strategy for natural gas liquid (NGL) recovery: process simulation and economic evaluation. Journal of Cleaner Production 194: 525–539. https://doi.org/10.1016/j.jclepro.2018.05.107.

22 22 Gas Processors Supply Association (2004). Engineering Data Book, 2.1–2.3. Tulsa, OK: Gas Processors Suppliers Association.

23 23 (2013). Purity Product Specifications. Lone Star NGL LLC. https://cms.energytransfer.com/wp-content/uploads/2018/12/LST_Purity_Specifications-Combined_03-04-2013.pdf.

24 24 (2015). Promax Foundations. Bryan Research & Engineering, Inc. http://www.bre.com/PDF/Foundations-Manual-En.pdf.

25 25 (2012). Aspen Capital Cost Estimator User's Guide, 608–610. Aspentech.

26 26 El‐Halwagi, M.M. (2012). Sustainable Design Through Process Integration: Fundamentals and Applications to Industrial Pollution Prevention Resource Conservation, and Profitability Enhancement. Oxford: Butterworth‐Heinemann.

27 27 ICIS Chemical Business (2008). Triethylene Glycol, vol. 273, 54–55. ICIS Chemical Business. https://www.icis.com/resources/news/2008/01/28/9095618/chemical-profile-triethylene-glycol.

28 28 Turton, R., Bailie, R.C., Whiting, W.B., and Shaeiwitz, J.A. (2011). Analysis, Synthesis and Design of Chemical Processes, 3e. Upper Saddle River, NJ: Pearson Education.

29 29 (2016). Typical Bills and Average Rates Report – Summer 2016. Edison Electric Institute. http://www.eei.org/resourcesandmedia/products/Pages/ProductDetails.aspx?prod=6B4E01F2-84AE-4EFA-AEB8-57B0199F2B90&type=P.

30 30 EIA. (2017) Henry Hub natural gas spot price. https://www.eia.gov/dnav/ng/hist/rngwhhdm.htm(accessed 27 October 2017).

31 31 Bureau of Labor Statistics. (2016) Occupational employment and wages, May 2016 – 51‐8092 gas plant operators. https://www.bls.gov/oes/current/oes518092.htm(accessed 2 September 2017).

32 32 Bureau of Labor Statistics. (2016) Occupational employment and wages, May 2016 – 11‐3051 industrial production managers. https://www.bls.gov/oes/current/oes113051.htm(accessed 2 September 2017).

33 33 Bloomberg L.P. 2017. Mont Belvieu LST Prices.

34 34 Polasek, J.C., Donnelly, S.T., and Bullin, J.A. (1989). Process Simulation and Optimization of Cryogenic Operations Using Multi‐stream Brazed Aluminum Exchangers, 100–106. Tulsa, OK: Gas Processors Association.

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