[1] Aguilar, S. Perry, J. Kim, R.Smith, “Design and Optimization of Flexible Utility Systems Subject to Variable Conditions part 1: Modeling Framework,” Chemical Engineering Research and Design, vol. 85, pp. 1136-1148, 2007.
[2] M.R. Jafari Nasr,J.A.H. Khodaei, “CO2 Reduction through Optimization of Steam Network in Petroleum Refineries: Evaluation of New Scenario,” presented at 30th International Conference of Industrial Energy Engineering (IETC), Texas, USA, 2008.
[3] M.R. Jafari Nasr,J.A.H. Khodaei, “An Optimization Approach to Refinery Steam Management with Consideration Of CO2 Emission,” Journal of Petroleum Science and Technology, 4(1), pp. 73-84, 2014.
[4] Z. Li, L. Zhao, W. Du, F. Qian, “Modeling and Optimization of the Steam Turbine Network of an Ethylene Plant,” Chinese Journal of Chemical Engineering, 21(5), pp. 520-528, 2013.
[5] S.G. Beangstrom, T. Majozi, “Steam system network synthesis with hot liquid reuse: II. Incorporating shaft work and optimum steam levels,” Computers & Chemical Engineering, 85(SupplementC), pp. 202-209, 2016.
[6] J. Cumpston, J. Pye, “Exergoeconomic optimisation of steam networks connecting solar-thermal dish arrays. Solar Energy,” 119(Supplement C), pp. 383-398, 2015.
[7] H. Wang, H. Wang, T. Zhu, W. Deng, “A novel model for steam transportation considering drainage loss in pipeline networks,” Applied Energy, 188(Supplement C), pp. 178-189, 2017.
[8] STAR Software, Version 2, Center for Process Integration, School of Chemical Engineering & Analytical Science, University of Manchester, UK, 2009.
[9] R. Smith, “Chemical Process Design and Integration,” NewYork: John Wiley and Sons, 2005.
[10] A. Bejan, G. Tatsaronis, M.J. Moran. “Thermal Design and Optimization”, NewYork: John Wiley and Sons, 1996.