Process Systems Engineering à la Canada

A special issue of Processes (ISSN 2227-9717). This special issue belongs to the section "Process Control and Monitoring".

Deadline for manuscript submissions: closed (31 August 2019) | Viewed by 25554

Special Issue Editors


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Guest Editor
Department of Chemical Engineering & Applied Chemistry, University of Toronto, Toronto, ON M5S 3E5, Canada
Interests: process identification, control and design, systems biology

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Guest Editor
Department of Chemical Engineering, École Polytechnique Montréal, Montréal, QC H3C 3A7, Canada
Interests: chemical and biochemical reactors, control systems, petrochemistry, biotechnology, biopharmacology

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Guest Editor
Department of Chemical Engineering, Universidad de la República, J. Herrera y Reissig 565, Montevideo, Uruguay
Interests: analysis, design and optimization of processes; modeling and simulation of chemical processes; data analysis and parameter estimation; biomass conversion to fuels and chemicals (biorefineries); energy systems

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Guest Editor
Department of Chemical Engineering, Ryerson University, Toronto, ON M4B 1B3, Canada
Interests: optimal control and optimization; process modeling and simulation

Special Issue Information

Dear Colleagues, 

The Canadian chemical engineering community (CSChE) has a long history of excellence in process systems engineering research and practice involving applied statistics and process design, control, and optimization. Members of this community recognized as early leaders include Park Reilly (Waterloo), David Bacon (Queen’s), John MacGregor (McMaster), and Grant Fisher (Alberta), all of whom served as both supervisors and mentors of hundreds of students who have themselves gone on to make contributions to these fields in both academia and industry, in Canada and around the world.  

Each year, this community gathers at the Canadian Chemical Engineering Conference to hear presentations based on work being done in the process systems engineering field on topics of relevance and importance to the chemical engineering community. This Special Issue is being coordinated with the 68th such conference that is being held in conjunction with the XXIX Interamerican Congress of Chemical Engineering in Toronto, Canada on October 28–31, 2018.  

This Special Issue focuses on, but is not limited to, papers that align with the “Systems and Control” thematic sessions of this conference:

  • Data analytics;
  • Data science;
  • Design of sustainable processes;
  • Optimal control.

We look forward to receiving your contributions.

Prof. William R. Cluett

 
Prof. Michel Perrier
Prof. Ana Inés Torres
Prof. Simant Upreti
Guest Editors

Manuscript Submission Information

Manuscripts should be submitted online at www.mdpi.com by registering and logging in to this website. Once you are registered, click here to go to the submission form. Manuscripts can be submitted until the deadline. All submissions that pass pre-check are peer-reviewed. Accepted papers will be published continuously in the journal (as soon as accepted) and will be listed together on the special issue website. Research articles, review articles as well as short communications are invited. For planned papers, a title and short abstract (about 100 words) can be sent to the Editorial Office for announcement on this website.

Submitted manuscripts should not have been published previously, nor be under consideration for publication elsewhere (except conference proceedings papers). All manuscripts are thoroughly refereed through a single-blind peer-review process. A guide for authors and other relevant information for submission of manuscripts is available on the Instructions for Authors page. Processes is an international peer-reviewed open access monthly journal published by MDPI.

Please visit the Instructions for Authors page before submitting a manuscript. The Article Processing Charge (APC) for publication in this open access journal is 2400 CHF (Swiss Francs). Submitted papers should be well formatted and use good English. Authors may use MDPI's English editing service prior to publication or during author revisions.

Published Papers (8 papers)

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14 pages, 291 KiB  
Article
Extremum Seeking Control for Discrete-Time with Quantized and Saturated Actuators
by Martin Guay and Daniel J. Burns
Processes 2019, 7(11), 831; https://0-doi-org.brum.beds.ac.uk/10.3390/pr7110831 - 08 Nov 2019
Cited by 4 | Viewed by 2019
Abstract
This paper proposes an extremum-seeking controller (ESC) design for a class of discrete-time nonlinear control systems subject to input constraints or quantized inputs. The proposed method implements a proportional-integral ESC design along with a discrete-time anti-windup mechanism. The anti-windup enforces input saturation while [...] Read more.
This paper proposes an extremum-seeking controller (ESC) design for a class of discrete-time nonlinear control systems subject to input constraints or quantized inputs. The proposed method implements a proportional-integral ESC design along with a discrete-time anti-windup mechanism. The anti-windup enforces input saturation while preserving the input dither signal. The technique incorporates a mechanism for adjusting the amplitude of the extremum seeking control dither signal. This mechanism ensures that any violation of constraints due to the dither signal is removed while maintaining the probing signal active. An amplitude update routine is also proposed. The amplitude update is coupled with a saturation bias estimation algorithm that correctly accounts for the inherent bias associated with systems operated at or near saturation conditions. The amplitude update is designed to remove the dither signal when the system approaches the optimum. It also ensures that a lower bound of the amplitude is enforced to guarantee that excitation conditions are maintained. Full article
(This article belongs to the Special Issue Process Systems Engineering à la Canada)
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19 pages, 553 KiB  
Article
An Optimal Feedback Control Strategy for Nonlinear, Distributed-Parameter Processes
by Debaprasad Dutta and Simant Ranjan Upreti
Processes 2019, 7(10), 758; https://0-doi-org.brum.beds.ac.uk/10.3390/pr7100758 - 17 Oct 2019
Cited by 3 | Viewed by 2984
Abstract
In this work, an optimal state feedback control strategy is proposed for non-linear, distributed-parameter processes. For different values of a given parameter susceptible to upsets, the strategy involves off-line computation of a repository of optimal open-loop states and gains needed for the feedback [...] Read more.
In this work, an optimal state feedback control strategy is proposed for non-linear, distributed-parameter processes. For different values of a given parameter susceptible to upsets, the strategy involves off-line computation of a repository of optimal open-loop states and gains needed for the feedback adjustment of control. A gain is determined by minimizing the perturbation of the objective functional about the new optimal state and control corresponding to a process upset. When an upset is encountered in a running process, the repository is utilized to obtain the control adjustment required to steer the process to the new optimal state. The strategy is successfully applied to a highly non-linear, gas-based heavy oil recovery process controlled by the gas temperature with the state depending non-linearly on time and two spatial directions inside a moving boundary, and subject to pressure upsets. The results demonstrate that when the process has a pressure upset, the proposed strategy is able to determine control adjustments with negligible time delays and to navigate the process to the new optimal state. Full article
(This article belongs to the Special Issue Process Systems Engineering à la Canada)
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17 pages, 1892 KiB  
Article
An Integration Method Using Kernel Principal Component Analysis and Cascade Support Vector Data Description for Pipeline Leak Detection with Multiple Operating Modes
by Mengfei Zhou, Qiang Zhang, Yunwen Liu, Xiaofang Sun, Yijun Cai and Haitian Pan
Processes 2019, 7(10), 648; https://0-doi-org.brum.beds.ac.uk/10.3390/pr7100648 - 22 Sep 2019
Cited by 24 | Viewed by 2930
Abstract
Pipelines are one of the most efficient and economical methods of transporting fluids, such as oil, natural gas, and water. However, pipelines are often subject to leakage due to pipe corrosion, pipe aging, pipe weld defects, or damage by a third-party, resulting in [...] Read more.
Pipelines are one of the most efficient and economical methods of transporting fluids, such as oil, natural gas, and water. However, pipelines are often subject to leakage due to pipe corrosion, pipe aging, pipe weld defects, or damage by a third-party, resulting in huge economic losses and environmental degradation. Therefore, effective pipeline leak detection methods are important research issues to ensure pipeline integrity management and accident prevention. The conventional methods for pipeline leak detection generally need to extract the features of leak signal to establish a leak detection model. However, it is difficult to obtain actual leakage signal data samples in most applications. In addition, the operating modes of pipeline fluid transportation process often have frequent changes, such as regulating valves and pump operation. Aiming at these issues, this paper proposes a hybrid intelligent method that integrates kernel principal component analysis (KPCA) and cascade support vector data description (Cas-SVDD) for pipeline leak detection with multiple operating modes, using data samples that are leak-free during pipeline operation. Firstly, the local mean decomposition method is used to denoise and reconstruct the measured signal to obtain the feature variables. Then, the feature dimension is reduced and the nonlinear principal component is extracted by the KPCA algorithm. Secondly, the K-means clustering algorithm is used to identify multiple operating modes and then obtain multiple support vector data description models to obtain the decision boundaries of the corresponding hyperspheres. Finally, pipeline leak is detected based on the Cas-SVDD method. The experimental results show that the proposed method can effectively detect small leaks and improve leak detection accuracy. Full article
(This article belongs to the Special Issue Process Systems Engineering à la Canada)
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14 pages, 4718 KiB  
Article
BISSO: Biomass Interface for Superstructure Simulation and Optimization
by Franco Mangone, Jimena Ferreira and Ana I. Torres
Processes 2019, 7(10), 645; https://0-doi-org.brum.beds.ac.uk/10.3390/pr7100645 - 21 Sep 2019
Viewed by 2583
Abstract
This paper presents a web-based tool for the optimization of biomass-to-chemicals processing pathways. The tool provides a user-friendly grpahical user interface (GUI) for building a process superstructure, offers the possibility of uploading data from Aspen Plus simulations and generates an optimization code to [...] Read more.
This paper presents a web-based tool for the optimization of biomass-to-chemicals processing pathways. The tool provides a user-friendly grpahical user interface (GUI) for building a process superstructure, offers the possibility of uploading data from Aspen Plus simulations and generates an optimization code to find the pathway that minimizes the annualized costs or maximizes the net present value. A processing pathway from residues to lactic acid is used to discuss and illustrate the main features of the tool. Full article
(This article belongs to the Special Issue Process Systems Engineering à la Canada)
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42 pages, 4831 KiB  
Article
A Comparison of Clustering and Prediction Methods for Identifying Key Chemical–Biological Features Affecting Bioreactor Performance
by Yiting Tsai, Susan A. Baldwin, Lim C. Siang and Bhushan Gopaluni
Processes 2019, 7(9), 614; https://0-doi-org.brum.beds.ac.uk/10.3390/pr7090614 - 10 Sep 2019
Cited by 2 | Viewed by 3551
Abstract
Chemical–biological systems, such as bioreactors, contain stochastic and non-linear interactions which are difficult to characterize. The highly complex interactions between microbial species and communities may not be sufficiently captured using first-principles, stationary, or low-dimensional models. This paper compares and contrasts multiple data analysis [...] Read more.
Chemical–biological systems, such as bioreactors, contain stochastic and non-linear interactions which are difficult to characterize. The highly complex interactions between microbial species and communities may not be sufficiently captured using first-principles, stationary, or low-dimensional models. This paper compares and contrasts multiple data analysis strategies, which include three predictive models (random forests, support vector machines, and neural networks), three clustering models (hierarchical, Gaussian mixtures, and Dirichlet mixtures), and two feature selection approaches (mean decrease in accuracy and its conditional variant). These methods not only predict the bioreactor outcome with sufficient accuracy, but the important features correlated with said outcome are also identified. The novelty of this work lies in the extensive exploration and critique of a wide arsenal of methods instead of single methods, as observed in many papers of similar nature. The results show that random forest models predict the test set outcomes with the highest accuracy. The identified contributory features include process features which agree with domain knowledge, as well as several different biomarker operational taxonomic units (OTUs). The results reinforce the notion that both chemical and biological features significantly affect bioreactor performance. However, they also indicate that the quality of the biological features can be improved by considering non-clustering methods, which may better represent the true behaviour within the OTU communities. Full article
(This article belongs to the Special Issue Process Systems Engineering à la Canada)
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24 pages, 3267 KiB  
Article
Discrete-Time Kalman Filter Design for Linear Infinite-Dimensional Systems
by Junyao Xie and Stevan Dubljevic
Processes 2019, 7(7), 451; https://0-doi-org.brum.beds.ac.uk/10.3390/pr7070451 - 15 Jul 2019
Cited by 6 | Viewed by 3273
Abstract
As the optimal linear filter and estimator, the Kalman filter has been extensively utilized for state estimation and prediction in the realm of lumped parameter systems. However, the dynamics of complex industrial systems often vary in both spatial and temporal domains, which take [...] Read more.
As the optimal linear filter and estimator, the Kalman filter has been extensively utilized for state estimation and prediction in the realm of lumped parameter systems. However, the dynamics of complex industrial systems often vary in both spatial and temporal domains, which take the forms of partial differential equations (PDEs) and/or delay equations. State estimation for these systems is quite challenging due to the mathematical complexity. This work addresses discrete-time Kalman filter design and realization for linear distributed parameter systems. In particular, the structural- and energy-preserving Crank–Nicolson framework is applied for model time discretization without spatial approximation or model order reduction. In order to ensure the time instance consistency in Kalman filter design, a new discrete model configuration is derived. To verify the feasibility of the proposed design, two widely-used PDEs models are considered, i.e., a pipeline hydraulic model and a 1D boundary damped wave equation. Full article
(This article belongs to the Special Issue Process Systems Engineering à la Canada)
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18 pages, 1343 KiB  
Article
Parallel Conical Area Community Detection Using Evolutionary Multi-Objective Optimization
by Weiqin Ying, Hassan Jalil, Bingshen Wu, Yu Wu, Zhenyu Ying, Yucheng Luo and ZhenYu Wang
Processes 2019, 7(2), 111; https://0-doi-org.brum.beds.ac.uk/10.3390/pr7020111 - 20 Feb 2019
Cited by 5 | Viewed by 3198
Abstract
Detecting community structures helps to reveal the functional units of complex networks. In this paper, the community detection problem is regarded as a modularity-based multi-objective optimization problem (MOP), and a parallel conical area community detection algorithm (PCACD) is designed to solve this MOP [...] Read more.
Detecting community structures helps to reveal the functional units of complex networks. In this paper, the community detection problem is regarded as a modularity-based multi-objective optimization problem (MOP), and a parallel conical area community detection algorithm (PCACD) is designed to solve this MOP effectively and efficiently. In consideration of the global properties of the selection and update mechanisms, PCACD employs a global island model and targeted elitist migration policy in a conical area evolutionary algorithm (CAEA) to discover community structures at different resolutions in parallel. Although each island is assigned only a portion of all sub-problems in the island model, it preserves a complete population to accomplish the global selection and update. Meanwhile the migration policy directly migrates each elitist individual to an appropriate island in charge of the sub-problem associated with this individual to share essential evolutionary achievements. In addition, a modularity-based greedy local search strategy is also applied to accelerate the convergence rate. Comparative experimental results on six real-world networks reveal that PCACD is capable of discovering potential high-quality community structures at diverse resolutions with satisfactory running efficiencies. Full article
(This article belongs to the Special Issue Process Systems Engineering à la Canada)
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7 pages, 174 KiB  
Commentary
Data Science in the Chemical Engineering Curriculum
by Thomas A. Duever
Processes 2019, 7(11), 830; https://0-doi-org.brum.beds.ac.uk/10.3390/pr7110830 - 08 Nov 2019
Cited by 8 | Viewed by 4114
Abstract
With the increasing availability of large amounts of data, methods that fall under the term data science are becoming important assets for chemical engineers to use. Methods, broadly speaking, are needed to carry out three tasks, namely data management, statistical and machine learning [...] Read more.
With the increasing availability of large amounts of data, methods that fall under the term data science are becoming important assets for chemical engineers to use. Methods, broadly speaking, are needed to carry out three tasks, namely data management, statistical and machine learning and data visualization. While claims have been made that data science is essentially statistics, consideration of the three tasks previously mentioned make it clear that it is really broader than just statistics alone and furthermore, statistical methods from a data-poor era are likely insufficient. While there have been many successful applications of data science methodologies, there are still many challenges that must be addressed. For example, just because a dataset is large, does not necessarily mean it is meaningful or information rich. From an organizational point of view, a lack of domain knowledge and a lack of a trained workforce among other issues are cited as barriers for the successful implementation of data science within an organization. Many of the methodologies employed in data science are familiar to chemical engineers; however, it is generally the case that not all the methods required to carry out data science projects are covered in an undergraduate chemical engineering program. One option to address this is to adjust the curriculum by modifying existing courses and introducing electives. Other examples include the introduction of a data science minor or a postgraduate certificate or a Master’s program in data science. Full article
(This article belongs to the Special Issue Process Systems Engineering à la Canada)
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