Optimal demand response scheduling of an industrial air separation unit using data-driven dynamic models

被引:81
作者
Tsay, Calvin [1 ]
Kumar, Ankur [2 ]
Flores-Cerrillo, Jesus [2 ]
Baldea, Michael [1 ]
机构
[1] Univ Texas Austin, McKetta Dept Chem Engn, Austin, TX 78712 USA
[2] Praxair Inc, bSmart Operat Praxair Digital, Tonawanda, NY 14150 USA
基金
美国国家科学基金会;
关键词
Integrated scheduling and control; Scale-bridging models; Demand-side management; Electricity markets; Air separation units; POWER-INTENSIVE PROCESSES; DISCRETE-TIME; OPTIMIZATION FRAMEWORK; PREDICTIVE CONTROL; SIDE MANAGEMENT; REDUCTION; OPERATION; MARKET; INTEGRATION; STRATEGY;
D O I
10.1016/j.compchemeng.2019.03.022
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
Managing electricity demand has become a key consideration in power grid operations. Industrial demand response (DR) is an important component of demand-side management, and electricity-intensive chemical processes can both support power grid operations and derive economic benefits from electricity price fluctuations. For air separation units (ASUs), DR participation calls for frequent production rate changes, over time scales that overlap with the dominant dynamics of the plant. Production scheduling calculations must therefore explicitly consider process dynamics. We introduce a data-driven approach for learning the DR scheduling-relevant dynamics of an industrial ASU from its operational history, and present a dynamic optimization-based DR scheduling framework. We show that a class of low-order Hammerstein-Wiener models can accurately represent the dynamics of the industrial ASU and its model predictive control system. We evaluate the economic benefits of the proposed scheduling framework, and analyze their sensitivity to electricity price uncertainty. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:22 / 34
页数:13
相关论文
共 53 条
[1]  
[Anonymous], 2010, PROCESS DYNAMICS CON
[2]  
[Anonymous], 2012, Dynamics and Nonlinear Control of Integrated Process Systems
[3]   Coordinator MPC for maximizing plant throughput [J].
Aske, Elvira Marie B. ;
Strand, Stig ;
Skogestad, Sigurd .
COMPUTERS & CHEMICAL ENGINEERING, 2008, 32 (1-2) :195-204
[4]   Integrated production scheduling and model predictive control of continuous processes [J].
Baldea, Michael ;
Du, Juan ;
Park, Jungup ;
Harjunkoski, Iiro .
AICHE JOURNAL, 2015, 61 (12) :4179-4190
[5]   Integrated production scheduling and process control: A systematic review [J].
Baldea, Michael ;
Harjunkoski, Iiro .
COMPUTERS & CHEMICAL ENGINEERING, 2014, 71 :377-390
[6]   Novel MILP Scheduling Model for Power-Intensive Processes under Time-Sensitive Electricity Prices [J].
Basan, Natalia P. ;
Grossmann, Ignacio E. ;
Gopalakrishnan, Ajit ;
Lotero, Irene ;
Mendez, Carlos A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (05) :1581-1592
[7]   Integrated scheduling and control in discrete-time with dynamic parameters and constraints [J].
Beal, Logan D. R. ;
Petersen, Damon ;
Grimsman, David ;
Warnick, Sean ;
Hedengren, John D. .
COMPUTERS & CHEMICAL ENGINEERING, 2018, 115 :361-376
[8]   Economic Benefit from Progressive Integration of Scheduling and Control for Continuous Chemical Processes [J].
Beal, Logan D. R. ;
Petersen, Damon ;
Pila, Guilherme ;
Davis, Brady ;
Warnick, Sean ;
Hedengren, John D. .
PROCESSES, 2017, 5 (04)
[9]   Simultaneous Process Scheduling and Control: A Multiparametric Programming-Based Approach [J].
Burnak, Bans ;
Katz, Justin ;
Diangelakis, Nikolaos A. ;
Pistikopoulos, Efstratios N. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (11) :3963-3976
[10]   Optimal Dynamic Operation of a High-Purity Air Separation Plant under Varying Market Conditions [J].
Cao, Yanan ;
Swartz, Christopher L. E. ;
Flores-Cerrillo, Jesus .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2016, 55 (37) :9956-9970