Plant-wide Scheduling and Marginal Value Analysis for a Refinery
نویسندگان
چکیده
This paper presents an integrated refinery scheduling model and its applications for a refinery located in Jiujiang, Jiangxi, P.R.China. The model integrates a crude oil unloading and storage area, a refining area, a blending area and a product storage area of the refinery. The scheduling model can be applied for optimizing the operation, configuration and production schedule of the refinery. The new modeling technique and solution strategy were developed to schedule crude oil unloading and storage. This method avoids solving an MINLP problem directly and shortens significantly the solution time. In the refining area, processing units such as CDU (crude distillation unit) and FCC (fluidized-bed catalytic cracking) were included and modeled. Yield models for CDU and FCC were used to optimize the CDU cut points and the FCC conversion level. This allows the refinery model to produce much more reliable and cost-effective solutions. A new analytical method called “marginal value analysis” is proposed to provide additional economic information for all stream flows inside the refinery. Important insights are generated using the analysis to find production bottlenecks, assist in decision making and price intermediate materials, etc. A real industrial example is used to illustrate the plant-wide scheduling model and corresponding marginal value analysis.
منابع مشابه
Fuzzy possibilistic modeling and sensitivity analysis for optimal fuel gas scheduling in refinery
In refinery, fuel gas which is continuously generated during the production process is one of the most important energy sources. Optimal scheduling of fuel gas system helps the refinery to achieve energy cost reduction and cleaner production. However, imprecise natures in the system, such as prediction of production rate of fuel gas, prediction of energy demand of the equipments and cost coeffi...
متن کاملOptimization of Control System of Petroleum Refinery Isomerization Unit by Plant-Wide Control Principles
Industrial process control system due to integration of equipment, existing material and energy recycle streams and their effects are extraordinary importance. The process in terms of safety, product quality and control stability have a challenge when there was defects in a process control system. The isomerization process is gaining importance in the presence of refining context due to upgradi...
متن کاملRobust Scheduling of Crude Oil Operations under Demand and Ship Arrival Uncertainty
Scheduling of crude oil operations is an important and complex routine task in a refinery. It involves crude oil unloading, tank allocation, storage and blending of crudes, and CDU charging. Optimal crude oil scheduling can increase profits by exploiting cheaper but poor quality crudes, minimizing crude changeovers, avoiding ship demurrage, and managing crude inventory optimally. In our previou...
متن کاملStability Proof of Gain-Scheduling Controller for Skid-to-Turn Missile Using Kharitonov Theorem
Gain scheduling is one of the most popular nonlinear control design approaches which has been widely and successfully applied in fields ranging from aerospace to process control. Despite the wide application of gain scheduling controllers, there is a notable lack of analysis on the stability of these controllers. The most common application of these kinds of controllers is in the field of fligh...
متن کاملA multi-objective resource-constrained optimization of time-cost trade-off problems in scheduling project
This paper presents a multi-objective resource-constrained project scheduling problem with positive and negative cash flows. The net present value (NPV) maximization and making span minimization are this study objectives. And since this problem is considered as complex optimization in NP-Hard context, we present a mathematical model for the given problem and solve three evolutionary algorithms;...
متن کامل