Integrated Gasoline Blending and Order Delivery Operations: Part I. Short-Term Scheduling and Global Optimization for Single and Multi-Period Operations

被引:16
作者
Li, Jie [1 ,2 ,3 ,4 ]
Xiao, Xin [3 ]
Floudas, Christodoulos A. [1 ,2 ]
机构
[1] Texas A&M Univ, Artie McFerrin Dept Chem Engn, College Stn, TX 77843 USA
[2] Texas A&M Univ, Texas A&M Energy Inst, College Stn, TX 77843 USA
[3] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
[4] Univ Manchester, Sch Chem Engn & Analyt Sci, Manchester M13 9PL, Lancs, England
基金
美国国家科学基金会; 中国国家自然科学基金;
关键词
scheduling; refinery operations; gasoline; blending; mixed-integer nonlinear programming; MINLP; global optimization; multi-period; CONSTRAINED QUADRATIC PROGRAMS; CONTINUOUS-TIME FORMULATION; INDUSTRIAL BATCH PLANT; RECIPE DETERMINATION; MODELS; OMEGA;
D O I
10.1002/aic.15168
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Gasoline is one of the most valuable products in an oil refinery and can account for as much as 60-70% of total profit. Optimal integrated scheduling of gasoline blending and order delivery operations can significantly increase profit by avoiding ship demurrage, improving customer satisfaction, minimizing quality give-aways, reducing costly transitions and slop generation, exploiting low-quality cuts, and reducing inventory costs. In this article, we first introduce a new unit-specific event-based continuous-time formulation for the integrated treatment of recipes, blending, and scheduling of gasoline blending and order delivery operations. Many operational features are included such as nonidentical parallel blenders, constant blending rate, minimum blend length and amount, blender transition times, multipurpose product tanks, changeovers, and piecewise constant profiles for blend component qualities and feed rates. To address the non-convexities arising from forcing constant blending rates during a run, we propose a hybrid global optimization approach incorporating a schedule adjustment procedure, iteratively via a mixed-integer programming and nonlinear programming scheme, and a rigorous deterministic global optimization approach. The computational results demonstrate that our proposed formulation does improve the mixed-integer linear programming relaxation of Li and Karimi, Ind. Eng. Chem. Res., 2011, 50, 9156-9174. All examples are solved to be 1%-global optimality with modest computational effort. (C) 2016 American Institute of Chemical Engineers
引用
收藏
页码:2043 / 2070
页数:28
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