Material stream network modeling, retrofit and optimization for raw natural gas refining systems

Abstract The demand for natural gas is increasing in the energy market because of its lower emissions and sustainable development. This increasing demand for natural gas promotes the capacity expansion of raw natural gas refining systems (RNGRSs), resulting in parallel refining processes in a RNGRS. Optimizing the material stream network between these refining processes is very challenging because of the complex thermodynamics, unit operations and utility configurations. An optimization framework is presented for the retrofit of the material stream network between these refining processes to improve the economic performance. The retrofit framework integrates raw natural gas supply, refining processes, utility subsystems and product delivery and is formulated as a mixed-integer nonlinear programming (MINLP) optimization model to obtain an optimal material stream network to increase profit. The model presented here is applied to a Chinese industrial RNGRS and results in an optimal retrofit. A comparison before and after the retrofit demonstrates a significant increase in profit.

[1]  Xianglong Luo,et al.  A multi-period mathematical model for simultaneous optimization of materials and energy on the refining site scale , 2015 .

[2]  Onder Ozgener,et al.  Energy and exergy analysis of electricity generation from natural gas pressure reducing stations , 2015 .

[3]  Panos M. Pardalos,et al.  Optimization Models in The Natural Gas Industry , 2010 .

[4]  Nguyen Van Duc Long,et al.  A novel self-heat recuperative dividing wall column to maximize energy efficiency and column throughput in retrofitting and debottlenecking of a side stream column , 2015 .

[5]  Vijay Modi,et al.  Potential for regional use of East Africa’s natural gas , 2015 .

[6]  Jacek Kalina,et al.  Energy and exergy recovery in a natural gas compressor station – A technical and economic analysis , 2015 .

[7]  Uthaiporn Suriyapraphadilok,et al.  Industrial wastewater treatment network based on recycling and rerouting strategies for retrofit design schemes , 2016 .

[8]  Chi Wai Hui,et al.  A hydraulics-based heuristic strategy for capacity expansion retrofit of distillation systems and an industrial application on a light-ends separation plant , 2012 .

[9]  Carl R. Branan,et al.  Rules of thumb for chemical engineers , 2016 .

[10]  Mark Robinson,et al.  A short-term operational planning model for natural gas production systems† , 2008 .

[11]  Pierre Neveu,et al.  Combined constructal and exergy optimization of thermochemical reactors for high temperature heat storage , 2013 .

[12]  Roger Z. Ríos-Mercado,et al.  Optimization problems in natural gas transportation systems. A state-of-the-art review , 2015 .

[13]  Serge Domenech,et al.  Improving the performance of natural gas pipeline networks fuel consumption minimization problems , 2009 .

[14]  J. A. Bandoni,et al.  Automatic design and optimization of natural gas plants , 1997 .

[15]  José Luiz de Medeiros,et al.  Comparative analysis of separation technologies for processing carbon dioxide rich natural gas in ultra-deepwater oil fields , 2017 .

[16]  Javad Mahmoudimehr,et al.  Optimal design of a natural gas transmission network layout , 2013 .

[17]  P. I. Barton,et al.  Stochastic pooling problem for natural gas production network design and operation under uncertainty , 2011 .

[18]  Bingjian Zhang,et al.  An optimization procedure for retrofitting process energy systems in refineries , 2012 .

[19]  Mahmoud M. El-Halwagi,et al.  Optimal planning and infrastructure development for shale gas production , 2016 .

[20]  Igor Bulatov,et al.  Application of optimal design methodologies in retrofitting natural gas combined cycle power plants with CO2 capture , 2016 .

[21]  Christodoulos A. Floudas,et al.  ANTIGONE: Algorithms for coNTinuous / Integer Global Optimization of Nonlinear Equations , 2014, Journal of Global Optimization.

[22]  Konrad Hungerbühler,et al.  Retrofit design of a pharmaceutical batch process considering “green chemistry and engineering” principles , 2015 .

[23]  Ali Elkamel,et al.  Generalized mixed-integer nonlinear programming modeling of eco-industrial networks to reduce cost and emissions , 2015 .

[24]  Rigoberto Ariel Yépez A Cost Function for the Natural Gas Transmission Industry , 2008 .

[25]  Jiří Jaromír Klemeš,et al.  Forty years of Heat Integration: Pinch Analysis (PA) and Mathematical Programming (MP) , 2013 .

[26]  Jin-Kuk Kim,et al.  Simulation-Based Process Design and Integration for the Sustainable Retrofit of Chemical Processes , 2011 .

[27]  Boqiang Lin,et al.  China\'s natural gas consumption peak and factors analysis: a regional perspective , 2017 .

[28]  Athanasios I. Papadopoulos,et al.  Systematic selection of amine mixtures as post-combustion CO2 capture solvent candidates , 2016 .

[29]  Hendrik Lambrecht,et al.  Enhancing sustainable production by the combined use of material flow analysis and mathematical programming , 2015 .

[30]  Ignacio E. Grossmann,et al.  Optimal synthesis of thermally coupled distillation sequences using a novel MILP approach , 2014, Comput. Chem. Eng..

[31]  Halit Üster,et al.  Optimization for Design and Operation of Natural Gas Transmission Networks , 2014 .

[32]  Ignacio E. Grossmann,et al.  A multiperiod planning model for gas production system , 2011 .

[33]  Jiří Jaromír Klemeš,et al.  Cleaner energy for cleaner production: modelling, simulation, optimisation and waste management , 2016 .

[34]  David Kendrick,et al.  GAMS, a user's guide , 1988, SGNM.

[35]  E. J. Anthony,et al.  Carbon capture and storage update , 2014 .