Data-Driven Mathematical Modeling and Global Optimization Framework for Entire Petrochemical Planning Operations

In this work we develop a novel modeling and global optimization-based planning formulation, which predicts product yields and properties for all of the production units within a highly integrated refinery-petrochemical complex. Distillation is modeled using swing-cut theory, while data-based nonlinear models are developed for other processing units. The parameters of the postulated models are globally optimized based on a large data set of daily production. Property indices in blending units are linearly additive and they are calculated on a weight or volume basis. Binary variables are introduced to denote unit and operation modes selection. The planning model is a large-scale non-convex mixed integer nonlinear optimization model, which is solved to e-global optimality. Computational results for multiple case studies indicate that we achieve a significant profit increase (37–65%) using the proposed data-driven global optimization framework. Finally, a user-friendly interface is presented which enables automated updating of demand, specification, and cost parameters. © 2016 American Institute of Chemical Engineers AIChE J, 62: 3020–3040, 2016

[1]  I. Grossmann,et al.  Refinery Production Planning: Multiperiod MINLP with Nonlinear CDU Model , 2012 .

[2]  Christodoulos A. Floudas,et al.  GloMIQO: Global mixed-integer quadratic optimizer , 2012, Journal of Global Optimization.

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

[4]  Omar J. Guerra,et al.  Improvements in Petroleum Refinery Planning: 1. Formulation of Process Models , 2011 .

[5]  Theodora Kourti,et al.  Process analysis, monitoring and diagnosis, using multivariate projection methods , 1995 .

[6]  Ali Elkamel,et al.  Multisite facility network integration design and coordination: An application to the refining industry , 2008, Comput. Chem. Eng..

[7]  Marianthi G. Ierapetritou,et al.  Mixed-Integer Linear Programming Model for Gasoline Blending and Distribution Scheduling , 2003 .

[8]  X. Zhu,et al.  A Simultaneous Optimization Strategy for Overall Integration in Refinery Planning , 2001 .

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

[10]  Brenno C. Menezes,et al.  Nonlinear Production Planning of Oil-Refinery Units for the Future Fuel Market in Brazil: Process Design Scenario-Based Model , 2014 .

[11]  Shuai Li,et al.  Modeling and monitoring of nonlinear multi-mode processes , 2014 .

[12]  Jie Li,et al.  Recipe determination and scheduling of gasoline blending operations , 2009 .

[13]  S. Joe Qin,et al.  Process data analytics in the era of big data , 2014 .

[14]  Ali Elkamel,et al.  A nonlinear programming model for refinery planning and optimisation with rigorous process models and product quality specifications , 2008 .

[15]  John F. MacGregor,et al.  Product design through multivariate statistical analysis of process data , 1998 .

[16]  Jose M. Pinto,et al.  A planning model for petroleum refineries , 2000 .

[17]  F. Morel,et al.  Consider integrating refining and petrochemical operations : Clean fuels , 2004 .

[18]  Vladimir Mahalec,et al.  Inferential monitoring and optimization of crude separation units via hybrid models , 2012, Comput. Chem. Eng..

[19]  Ignacio E. Grossmann,et al.  Improved Swing-Cut Modeling for Planning and Scheduling of Oil-Refinery Distillation Units , 2013 .

[20]  Bin Zhang,et al.  Effective MILP model for oil refinery-wide production planning and better energy utilization , 2007 .

[21]  Jose M. Pinto,et al.  A PLANNING MODEL FOR REFINERY DIESEL PRODUCTION , 1998 .

[22]  Christodoulos A. Floudas,et al.  A Framework for Globally Optimizing Mixed-Integer Signomial Programs , 2013, Journal of Optimization Theory and Applications.

[23]  R. W. Brooks,et al.  Choosing cutpoints to optimize product yields : Refining developments: Special report , 1999 .

[24]  Marianthi G. Ierapetritou,et al.  Petroleum Refining Operations: Key Issues, Advances, and Opportunities , 2011 .

[25]  Jose M. Pinto,et al.  PLANNING AND SCHEDULING MODELS FOR REFINERY OPERATIONS , 2000 .

[26]  Christodoulos A. Floudas,et al.  Dynamically generated cutting planes for mixed-integer quadratically constrained quadratic programs and their incorporation into GloMIQO 2 , 2015, Optim. Methods Softw..

[27]  A. S. Khokhlov,et al.  Rolling detailed short-term planning of oil refineries and petrochemical complexes and optimization model updating , 2015, Autom. Remote. Control..

[28]  Ignacio E. Grossmann,et al.  Integration of Nonlinear Crude Distillation Unit Models in Refinery Planning Optimization , 2011 .

[29]  Sigrid Lise Nonås,et al.  Refinery Planning and Scheduling: An Overview , 2010 .

[30]  Miguel J. Bagajewicz,et al.  Integrated Model for Refinery Planning, Oil Procuring, and Product Distribution , 2009 .

[31]  R. L. Geddes A general index of fractional distillation power for hydrocarbon mixtures , 1958 .

[32]  Sylvain Mouret,et al.  A new Lagrangian decomposition approach applied to the integration of refinery planning and crude-oil scheduling , 2011, Comput. Chem. Eng..

[33]  Wenkai Li,et al.  Integrating CDU, FCC and product blending models into refinery planning , 2005, Comput. Chem. Eng..

[34]  I. Karimi,et al.  Scheduling Gasoline Blending Operations from Recipe Determination to Shipping Using Unit Slots , 2011 .

[35]  J. Macgregor,et al.  Experiences with industrial applications of projection methods for multivariate statistical process control , 1996 .

[36]  Nan Zhang,et al.  Analytical optimisation of industrial systems and applications to refineries, petrochemicals , 2004 .

[37]  A. Elkamel,et al.  Multisite Refinery and Petrochemical Network Design: Optimal Integration and Coordination , 2009 .

[38]  I. Karimi,et al.  Improving the robustness and efficiency of crude scheduling algorithms , 2007 .

[39]  Omar J. Guerra,et al.  Improvements in Petroleum Refinery Planning: 2. Case Studies , 2011 .

[40]  T. E. Swaty Consider over-the-fence product stream swapping to raise profitability , 2002 .