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Development of a Digital Twin for the Prediction and Control of Supersaturation during Batch Cooling Crystallization
[Image: see text] Fine chemicals produced via batch crystallization with properties dependent on the crystal size distribution require precise control of supersaturation, which drives the evolution of crystal size over time. Model predictive control (MPC) of supersaturation using a mechanistic model...
Autores principales: | , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
American Chemical Society
2023
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10360059/ https://www.ncbi.nlm.nih.gov/pubmed/37484628 http://dx.doi.org/10.1021/acs.iecr.3c00371 |
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author | Leeming, Ryan Mahmud, Tariq Roberts, Kevin J. George, Neil Webb, Jennifer Simone, Elena Brown, Cameron J. |
author_facet | Leeming, Ryan Mahmud, Tariq Roberts, Kevin J. George, Neil Webb, Jennifer Simone, Elena Brown, Cameron J. |
author_sort | Leeming, Ryan |
collection | PubMed |
description | [Image: see text] Fine chemicals produced via batch crystallization with properties dependent on the crystal size distribution require precise control of supersaturation, which drives the evolution of crystal size over time. Model predictive control (MPC) of supersaturation using a mechanistic model to represent the behavior of a crystallization process requires less experimental time and resources compared with fully empirical model-based control methods. Experimental characterization of the hexamine–ethanol crystallization system was performed in order to collect the parameters required to build a one-dimensional (1D) population balance model (PBM) in gPROMS FormulatedProducts software (Siemens-PSE Ltd.). Analysis of the metastable zone width (MSZW) and a series of seeded batch cooling crystallizations informed the suitable process conditions selected for supersaturation control experiments. The gPROMS model was integrated with the control software PharmaMV (Perceptive Engineering Ltd.) to create a digital twin of the crystallizer. Simulated batch crystallizations were used to train two statistical MPC blocks, allowing for in silico supersaturation control simulations to develop an effective control strategy. In the supersaturation set-point range of 0.012–0.036, the digital twin displayed excellent performance that would require minimal controller tuning to steady out any instabilities. The MPC strategy was implemented on a physical 500 mL crystallizer, with the simulated solution concentration replaced by in situ measurements from calibrated attenuated total reflection–Fourier transform infrared (ATR-FTIR) spectroscopy. Physical supersaturation control performance was slightly more unstable than the in silico tests, which is consistent with expected disturbances to the heat transfer, which were not specifically modeled in simulations. Overall, the level of supersaturation control in a real crystallizer was found to be accurate and precise enough to consider future adaptations to the MPC strategy for more advanced control objectives, such as the crystal size. |
format | Online Article Text |
id | pubmed-10360059 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2023 |
publisher | American Chemical Society |
record_format | MEDLINE/PubMed |
spelling | pubmed-103600592023-07-22 Development of a Digital Twin for the Prediction and Control of Supersaturation during Batch Cooling Crystallization Leeming, Ryan Mahmud, Tariq Roberts, Kevin J. George, Neil Webb, Jennifer Simone, Elena Brown, Cameron J. Ind Eng Chem Res [Image: see text] Fine chemicals produced via batch crystallization with properties dependent on the crystal size distribution require precise control of supersaturation, which drives the evolution of crystal size over time. Model predictive control (MPC) of supersaturation using a mechanistic model to represent the behavior of a crystallization process requires less experimental time and resources compared with fully empirical model-based control methods. Experimental characterization of the hexamine–ethanol crystallization system was performed in order to collect the parameters required to build a one-dimensional (1D) population balance model (PBM) in gPROMS FormulatedProducts software (Siemens-PSE Ltd.). Analysis of the metastable zone width (MSZW) and a series of seeded batch cooling crystallizations informed the suitable process conditions selected for supersaturation control experiments. The gPROMS model was integrated with the control software PharmaMV (Perceptive Engineering Ltd.) to create a digital twin of the crystallizer. Simulated batch crystallizations were used to train two statistical MPC blocks, allowing for in silico supersaturation control simulations to develop an effective control strategy. In the supersaturation set-point range of 0.012–0.036, the digital twin displayed excellent performance that would require minimal controller tuning to steady out any instabilities. The MPC strategy was implemented on a physical 500 mL crystallizer, with the simulated solution concentration replaced by in situ measurements from calibrated attenuated total reflection–Fourier transform infrared (ATR-FTIR) spectroscopy. Physical supersaturation control performance was slightly more unstable than the in silico tests, which is consistent with expected disturbances to the heat transfer, which were not specifically modeled in simulations. Overall, the level of supersaturation control in a real crystallizer was found to be accurate and precise enough to consider future adaptations to the MPC strategy for more advanced control objectives, such as the crystal size. American Chemical Society 2023-07-03 /pmc/articles/PMC10360059/ /pubmed/37484628 http://dx.doi.org/10.1021/acs.iecr.3c00371 Text en © 2023 The Authors. Published by American Chemical Society https://creativecommons.org/licenses/by/4.0/Permits the broadest form of re-use including for commercial purposes, provided that author attribution and integrity are maintained (https://creativecommons.org/licenses/by/4.0/). |
spellingShingle | Leeming, Ryan Mahmud, Tariq Roberts, Kevin J. George, Neil Webb, Jennifer Simone, Elena Brown, Cameron J. Development of a Digital Twin for the Prediction and Control of Supersaturation during Batch Cooling Crystallization |
title | Development of a Digital Twin for the Prediction and
Control of Supersaturation during Batch Cooling Crystallization |
title_full | Development of a Digital Twin for the Prediction and
Control of Supersaturation during Batch Cooling Crystallization |
title_fullStr | Development of a Digital Twin for the Prediction and
Control of Supersaturation during Batch Cooling Crystallization |
title_full_unstemmed | Development of a Digital Twin for the Prediction and
Control of Supersaturation during Batch Cooling Crystallization |
title_short | Development of a Digital Twin for the Prediction and
Control of Supersaturation during Batch Cooling Crystallization |
title_sort | development of a digital twin for the prediction and
control of supersaturation during batch cooling crystallization |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10360059/ https://www.ncbi.nlm.nih.gov/pubmed/37484628 http://dx.doi.org/10.1021/acs.iecr.3c00371 |
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