Mitigating Safety Concerns and Profit/Production Losses for Chemical Process Control Systems under Cyberattacks via Design/Control Methods

被引:11
作者
Durand, Helen [1 ,2 ]
Wegener, Matthew [1 ]
机构
[1] Wayne State Univ, Dept Chem Engn & Mat Sci, 5050 Anthony Wayne Dr, Detroit, MI 48202 USA
[2] 5050 Anthony Wayne Dr, Detroit, MI 48202 USA
基金
美国国家科学基金会;
关键词
process control; process design; cybersecurity; process operational safety; nonlinear dynamic systems; MODEL PREDICTIVE CONTROL;
D O I
10.3390/math8040499
中图分类号
O1 [数学];
学科分类号
0701 ; 070101 ;
摘要
One of the challenges for chemical processes today, from a safety and profit standpoint, is the potential that cyberattacks could be performed on components of process control systems. Safety issues could be catastrophic; however, because the nonlinear systems definition of a cyberattack has similarities to a nonlinear systems definition of faults, many processes have already been instrumented to handle various problematic input conditions. Also challenging is the question of how to design a system that is resilient to attacks attempting to impact the production volumes or profits of a company. In this work, we explore a process/equipment design framework for handling safety issues in the presence of cyberattacks (in the spirit of traditional HAZOP thinking), and present a method for bounding the profit/production loss which might be experienced by a plant under a cyberattack through the use of a sufficiently conservative operating strategy combined with the assumption that an attack detection method with characterizable time to detection is available.
引用
收藏
页数:38
相关论文
共 48 条
[1]   On identification of well-conditioned nonlinear systems: Application to economic model predictive control of nonlinear processes [J].
Alanqar, Anas ;
Durand, Helen ;
Christofides, Panagiotis D. .
AICHE JOURNAL, 2015, 61 (10) :3353-3373
[2]   Economic Model Predictive Control of Nonlinear Process Systems Using Empirical Models [J].
Alanqar, Anas ;
Ellis, Matthew ;
Christofides, Panagiotis D. .
AICHE JOURNAL, 2015, 61 (03) :816-830
[3]   Process operational safety using model predictive control based on a process Safeness Index [J].
Albalawi, Fahad ;
Durand, Helen ;
Christofides, Panagiotis D. .
COMPUTERS & CHEMICAL ENGINEERING, 2017, 104 :76-88
[4]   A Feedback Control Framework for Safe and Economically-Optimal Operation of Nonlinear Processes [J].
Albalawi, Fahad ;
Alanqar, Anas ;
Durand, Helen ;
Christofides, Panagiotis D. .
AICHE JOURNAL, 2016, 62 (07) :2391-2409
[5]  
[Anonymous], 2014, IEEE ETFA
[6]  
[Anonymous], THESIS
[7]  
[Anonymous], IND P OFFSH TECHN C
[8]  
[Anonymous], P ACM AS C COMP COMM
[9]  
[Anonymous], CHALLENGES SECURING
[10]  
[Anonymous], 2009, COMBINATORIAL SCI CO