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Software Sensor for Activity-Time Monitoring and Fault Detection in Production Lines. SENSORS 2018; 18:s18072346. [PMID: 30029510 PMCID: PMC6069246 DOI: 10.3390/s18072346] [Citation(s) in RCA: 21] [Impact Index Per Article: 3.5] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 05/31/2018] [Revised: 07/13/2018] [Accepted: 07/16/2018] [Indexed: 11/17/2022]
Abstract
Industry 4.0-based human-in-the-loop cyber-physical production systems are transforming the industrial workforce to accommodate the ever-increasing variability of production. Real-time operator support and performance monitoring require accurate information on the activities of operators. The problem with tracing hundreds of activity times is critical due to the enormous variability and complexity of products. To handle this problem a software-sensor-based activity-time and performance measurement system is proposed. To ensure a real-time connection between operator performance and varying product complexity, fixture sensors and an indoor positioning system (IPS) were designed and this multi sensor data merged with product-relevant information. The proposed model-based performance monitoring system tracks the recursively estimated parameters of the activity-time estimation model. As the estimation problem can be ill-conditioned and poor raw sensor data can result in unrealistic parameter estimates, constraints were introduced into the parameter-estimation algorithm to increase the robustness of the software sensor. The applicability of the proposed methodology is demonstrated on a well-documented benchmark problem of a wire harness manufacturing process. The fully reproducible and realistic simulation study confirms that the indoor positioning system-based integration of primary sensor signals and product-relevant information can be efficiently utilized in terms of the constrained recursive estimation of the operator activity.
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Panjwani S, Nikolaou M. Experiment design for control-relevant identification of partially known stable multivariable systems. AIChE J 2016. [DOI: 10.1002/aic.15212] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/08/2022]
Affiliation(s)
- Shyam Panjwani
- Chemical & Biomolecular Engineering Dept.; University of Houston; Houston TX 77204-4004
| | - Michael Nikolaou
- Chemical & Biomolecular Engineering Dept.; University of Houston; Houston TX 77204-4004
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Alenany A, Shang H. Recursive subspace identification with prior information using the constrained least squares approach. Comput Chem Eng 2013. [DOI: 10.1016/j.compchemeng.2013.03.016] [Citation(s) in RCA: 9] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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Bassingthwaighte JB, Chizeck HJ, Atlas LE. Strategies and Tactics in Multiscale Modeling of Cell-to-Organ Systems. PROCEEDINGS OF THE IEEE. INSTITUTE OF ELECTRICAL AND ELECTRONICS ENGINEERS 2006; 94:819-830. [PMID: 20463841 PMCID: PMC2867355 DOI: 10.1109/jproc.2006.871775] [Citation(s) in RCA: 13] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/05/2023]
Abstract
Modeling is essential to integrating knowledge of human physiology. Comprehensive self-consistent descriptions expressed in quantitative mathematical form define working hypotheses in testable and reproducible form, and though such models are always "wrong" in the sense of being incomplete or partly incorrect, they provide a means of understanding a system and improving that understanding. Physiological systems, and models of them, encompass different levels of complexity. The lowest levels concern gene signaling and the regulation of transcription and translation, then biophysical and biochemical events at the protein level, and extend through the levels of cells, tissues and organs all the way to descriptions of integrated systems behavior. The highest levels of organization represent the dynamically varying interactions of billions of cells. Models of such systems are necessarily simplified to minimize computation and to emphasize the key factors defining system behavior; different model forms are thus often used to represent a system in different ways. Each simplification of lower level complicated function reduces the range of accurate operability at the higher level model, reducing robustness, the ability to respond correctly to dynamic changes in conditions. When conditions change so that the complexity reduction has resulted in the solution departing from the range of validity, detecting the deviation is critical, and requires special methods to enforce adapting the model formulation to alternative reduced-form modules or decomposing the reduced-form aggregates to the more detailed lower level modules to maintain appropriate behavior. The processes of error recognition, and of mapping between different levels of model complexity and shifting the levels of complexity of models in response to changing conditions, are essential for adaptive modeling and computer simulation of large-scale systems in reasonable time.
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Bassingthwaighte JB, Chizeck HJ, Atlas LE, Qian H. Multiscale modeling of cardiac cellular energetics. Ann N Y Acad Sci 2005; 1047:395-424. [PMID: 16093514 PMCID: PMC2864600 DOI: 10.1196/annals.1341.035] [Citation(s) in RCA: 20] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Abstract] [MESH Headings] [Grants] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/12/2022]
Abstract
Multiscale modeling is essential to integrating knowledge of human physiology starting from genomics, molecular biology, and the environment through the levels of cells, tissues, and organs all the way to integrated systems behavior. The lowest levels concern biophysical and biochemical events. The higher levels of organization in tissues, organs, and organism are complex, representing the dynamically varying behavior of billions of cells interacting together. Models integrating cellular events into tissue and organ behavior are forced to resort to simplifications to minimize computational complexity, thus reducing the model's ability to respond correctly to dynamic changes in external conditions. Adjustments at protein and gene regulatory levels shortchange the simplified higher-level representations. Our cell primitive is composed of a set of subcellular modules, each defining an intracellular function (action potential, tricarboxylic acid cycle, oxidative phosphorylation, glycolysis, calcium cycling, contraction, etc.), composing what we call the "eternal cell," which assumes that there is neither proteolysis nor protein synthesis. Within the modules are elements describing each particular component (i.e., enzymatic reactions of assorted types, transporters, ionic channels, binding sites, etc.). Cell subregions are stirred tanks, linked by diffusional or transporter-mediated exchange. The modeling uses ordinary differential equations rather than stochastic or partial differential equations. This basic model is regarded as a primitive upon which to build models encompassing gene regulation, signaling, and long-term adaptations in structure and function. During simulation, simpler forms of the model are used, when possible, to reduce computation. However, when this results in error, the more complex and detailed modules and elements need to be employed to improve model realism. The processes of error recognition and of mapping between different levels of model form complexity are challenging but are essential for successful modeling of large-scale systems in reasonable time. Currently there is to this end no established methodology from computational sciences.
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Madár J, Abonyi J, Roubos H, Szeifert F. Incorporating Prior Knowledge in a Cubic Spline ApproximationApplication to the Identification of Reaction Kinetic Models. Ind Eng Chem Res 2003. [DOI: 10.1021/ie0205445] [Citation(s) in RCA: 23] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- János Madár
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201 Veszprem, Hungary, and Control Systems Engineering, Delft University of Technology, P.O. Box 5031, 2600 GA Delft, The Netherlands
| | - János Abonyi
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201 Veszprem, Hungary, and Control Systems Engineering, Delft University of Technology, P.O. Box 5031, 2600 GA Delft, The Netherlands
| | - Hans Roubos
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201 Veszprem, Hungary, and Control Systems Engineering, Delft University of Technology, P.O. Box 5031, 2600 GA Delft, The Netherlands
| | - Ferenc Szeifert
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201 Veszprem, Hungary, and Control Systems Engineering, Delft University of Technology, P.O. Box 5031, 2600 GA Delft, The Netherlands
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Chia TL. Model predictive control helps to regulate slow processes--robust barrel temperature control. ISA TRANSACTIONS 2002; 41:501-509. [PMID: 12398280 DOI: 10.1016/s0019-0578(07)60105-0] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/24/2023]
Abstract
Slow temperature control is a challenging control problem. The problem becomes even more challenging when multiple zones are involved, such as in barrel temperature control for extruders. Often, strict closed-loop performance requirements (such as fast startup with no overshoot and maintaining tight temperature control during production) are given for such applications. When characteristics of the system are examined, it becomes clear that a commonly used proportional plus integral plus derivative (PID) controller cannot meet such performance specifications for this kind of system. The system either will overshoot or not maintain the temperature within the specified range during the production run. In order to achieve the required performance, a control strategy that utilizes techniques such as model predictive control, autotuning, and multiple parameter PID is formulated. This control strategy proves to be very effective in achieving the desired specifications, and is very robust.
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Affiliation(s)
- Tien L Chia
- ControlSoft, Inc., Highland Heights, Ohio 44143, USA
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Abonyi J, Babuska R, Szeifert F. Fuzzy modeling with multivariate membership functions: gray-box identification and control design. ACTA ACUST UNITED AC 2001; 31:755-67. [DOI: 10.1109/3477.956037] [Citation(s) in RCA: 39] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
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Corrêa N, Corrêa R, Freire J. Adaptive control of paste drying in spouted bed using the GPC algorithm. BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING 2000. [DOI: 10.1590/s0104-66322000000400028] [Citation(s) in RCA: 9] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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Abonyi J, Babuška R, M. Ayala Botto,, Szeifert F, Nagy L. Identification and Control of Nonlinear Systems Using Fuzzy Hammerstein Models. Ind Eng Chem Res 2000. [DOI: 10.1021/ie990629e] [Citation(s) in RCA: 55] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- J. Abonyi
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201, Hungary, Department of Information Technology and Systems and Control Engineering Laboratory, Delft University of Technology, P.O. Box 5031 2600 GA Delft, The Netherlands, and Instituto Superior and Department of Mechanical Engineering, Technical University of Lisbon, GCAR Avenida Rovisco Pais, 1049-001 Lisboa, Portugal
| | - R. Babuška
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201, Hungary, Department of Information Technology and Systems and Control Engineering Laboratory, Delft University of Technology, P.O. Box 5031 2600 GA Delft, The Netherlands, and Instituto Superior and Department of Mechanical Engineering, Technical University of Lisbon, GCAR Avenida Rovisco Pais, 1049-001 Lisboa, Portugal
| | - M. Ayala Botto,
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201, Hungary, Department of Information Technology and Systems and Control Engineering Laboratory, Delft University of Technology, P.O. Box 5031 2600 GA Delft, The Netherlands, and Instituto Superior and Department of Mechanical Engineering, Technical University of Lisbon, GCAR Avenida Rovisco Pais, 1049-001 Lisboa, Portugal
| | - F. Szeifert
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201, Hungary, Department of Information Technology and Systems and Control Engineering Laboratory, Delft University of Technology, P.O. Box 5031 2600 GA Delft, The Netherlands, and Instituto Superior and Department of Mechanical Engineering, Technical University of Lisbon, GCAR Avenida Rovisco Pais, 1049-001 Lisboa, Portugal
| | - L. Nagy
- Department of Process Engineering, University of Veszprem, P.O. Box 158, H-8201, Hungary, Department of Information Technology and Systems and Control Engineering Laboratory, Delft University of Technology, P.O. Box 5031 2600 GA Delft, The Netherlands, and Instituto Superior and Department of Mechanical Engineering, Technical University of Lisbon, GCAR Avenida Rovisco Pais, 1049-001 Lisboa, Portugal
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