Reliability of complex chemical engineering processes

被引:19
作者
Abubakar, Usman [1 ]
Sriramula, Srinivas [1 ]
Renton, Neill C. [2 ]
机构
[1] Univ Aberdeen, Lloyds Register Fdn Ctr Safety & Reliabil Engn, Aberdeen AB24 3UE, Scotland
[2] Univ Aberdeen, Sch Engn, Aberdeen AB24 3UE, Scotland
关键词
Chemical process reliability; Design optimisation; Uncertainty modelling; Stochastic analysis; Process performance simulation; OPTIMIZATION; UNCERTAINTY; STRATEGIES; SIMULATION; DESIGN;
D O I
10.1016/j.compchemeng.2014.12.013
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This paper presents a stochastic performance modelling approach that can be used to optimise design and operational reliability of complex chemical engineering processes. The framework can be applied to processes comprising multiple units, including the cases where closed form process performance functions are unavailable or difficult to derive from first principles, which is often the case in practice. An interface that facilitates automated two-way communication between Matlab (R) and process simulation environment is used to generate large process responses. The resulting constrained optimisation problem is solved using both Monte Carlo Simulation (MCS) and First Order Reliability Method (FORM); providing a wide range of stochastic process performance measures. Adding such capabilities to traditional deterministic process simulators provides a more informed basis for selecting optimum design factors; giving a simple way of enhancing overall process reliability and cost-efficiency. Two case study systems are considered to highlight the applicability and benefits of the approach. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1 / 14
页数:14
相关论文
共 38 条
[31]   Optimization of chemical processes with dependent uncertain parameters [J].
Ostrovsky, G. M. ;
Ziyatdinov, N. N. ;
Lapteva, T. V. ;
Zaitsev, I. V. .
CHEMICAL ENGINEERING SCIENCE, 2012, 83 :119-127
[32]  
Smith R, 2005, CHEM PROCESS DESIGN
[33]   Inconsistencies in dew points from different algorithm types possible causes and solutions [J].
Starling, KE ;
Luongo, JF ;
Hubbard, RA ;
Lilly, LL .
FLUID PHASE EQUILIBRIA, 2001, 183 :209-216
[34]   A strategy for multi-objective optimization under uncertainty in chemical process design [J].
Sun Li ;
Lou, Helen H. .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2008, 16 (01) :39-42
[35]  
Thoft-Christensen P., 1982, STRUCTURAL RELIABILI
[36]  
Vasquez VR, 2004, CHEM ENG COMMUNICATI, V191
[37]  
Vasquez VR, 2010, COMPUT CHEM ENG, V34, P298
[38]   DETECTING AND DISPLAYING SIZE BIMODALITY - KURTOSIS, SKEWNESS AND BIMODALIZABLE DISTRIBUTIONS [J].
WYSZOMIRSKI, T .
JOURNAL OF THEORETICAL BIOLOGY, 1992, 158 (01) :109-128