Abstract

In an ethylene plant, steam system provides shaft power to compressors and pumps and heats the process streams. Modeling and optimization of a steam system is a powerful tool to bring benefits and save energy for ethylene plants. However, the uncertainty of device efficiencies and the fluctuation of the process demands cause great difficulties to traditional mathematical programming methods, which could result in suboptimal or infeasible solution. The growing data-driven optimization approaches offer new techniques to eliminate uncertainty in the process system engineering community. A data-driven robust optimization (DDRO) methodology is proposed to deal with uncertainty in the optimization of steam system in an ethylene plant. A hybrid model of extraction–exhausting steam turbine is developed, and its coefficients are considered as uncertain parameters. A deterministic mixed integer linear programming model of the steam system is formulated based on the model of the components to minimize the operating cost of the ethylene plant. The uncertain parameter set of the proposed model is derived from the historical data, and the Dirichlet process mixture model is employed to capture the features for the construction of the uncertainty set. In combination with the derived uncertainty set, a data-driven conic quadratic mixed-integer programming model is reformulated for the optimization of the steam system under uncertainty. An actual case study is utilized to validate the performance of the proposed DDRO method.

Highlights

  • BackgroundEthylene production supplies most of the basic raw materials for the petrochemical industry

  • The operational optimization of steam systems for ethylene plants contributes to the reduction of the operating cost

  • We propose a data-driven method for robust optimization of a steam system under device efficiency uncertainty

Read more

Summary

Background

Ethylene production supplies most of the basic raw materials for the petrochemical industry. Research [4] proposed an MINLP approach for planning optimization of the utility system in a cogeneration plant by complex steam turbine decomposition Uncertainties, such as steam turbine efficiency and process demands, in an actual ethylene plant could result in an infeasible solution from existing models and optimization methodology. This condition may lead to the pressure fluctuation of the steam header and the low-efficiency operation of the steam turbine. Research [19] proposed a data-driven adaptive robust optimization method for operational optimization of an industrial steam system under uncertainty. Studies [21,22,23] proposed different data-driven adaptive robust optimization schemas by utilizing the data-driven uncertainty set and applied them for process scheduling and planning problems

Significance
Innovations
Organization
Steam System Description and Problem Statement
Models of Building Blocks in the Steam System
Steam Turbine Model
Letdown Valve Model
Steam System Model for the Ethylene Plant
Shaft Power Demand
Process Demand
Variable Range
Collection
Data-Driven Uncertainty Set Construction
Robust CQMIP Model of the Steam System
Initial
Comparison ofof extraction ratesofofEESTS
Findings
Conclusions
Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.