Multiscale modeling and control of Kappa number and porosity in a batch‐type pulp digester
This work proposes a multiscale modeling and model‐based feedback control framework for the delignification process in a batch‐type pulp digester. Specifically, we focus on a hardwood chip in the digester and develop a multiscale model capturing both the evolution of microscopic properties such as t...
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Veröffentlicht in: | AIChE journal 2019-06, Vol.65 (6), p.n/a |
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description | This work proposes a multiscale modeling and model‐based feedback control framework for the delignification process in a batch‐type pulp digester. Specifically, we focus on a hardwood chip in the digester and develop a multiscale model capturing both the evolution of microscopic properties such as the pore size and shape distributions in the solid phase and the dynamic changes in the temperature and component concentrations in the liquor phase. While the macroscopic model adopts the continuum hypothesis based on the Purdue model, a novel microscopic model is developed using a kinetic Monte Carlo algorithm, accounting for the dissolution of lignin, cellulose, and hemicellulose contacting the liquor phase. A reduced‐order model was built to design a Luenberger observer for state estimation, which is then used to develop a model‐based control system. The simulation results demonstrated that the proposed methodology was able to regulate both the Kappa number and porosity to desired values. |
doi_str_mv | 10.1002/aic.16589 |
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Specifically, we focus on a hardwood chip in the digester and develop a multiscale model capturing both the evolution of microscopic properties such as the pore size and shape distributions in the solid phase and the dynamic changes in the temperature and component concentrations in the liquor phase. While the macroscopic model adopts the continuum hypothesis based on the Purdue model, a novel microscopic model is developed using a kinetic Monte Carlo algorithm, accounting for the dissolution of lignin, cellulose, and hemicellulose contacting the liquor phase. A reduced‐order model was built to design a Luenberger observer for state estimation, which is then used to develop a model‐based control system. The simulation results demonstrated that the proposed methodology was able to regulate both the Kappa number and porosity to desired values.</description><identifier>ISSN: 0001-1541</identifier><identifier>EISSN: 1547-5905</identifier><identifier>DOI: 10.1002/aic.16589</identifier><language>eng</language><publisher>Hoboken, USA: John Wiley & Sons, Inc</publisher><subject>Algorithms ; Cellulose ; Computer simulation ; Digesters ; Feedback control ; Hemicellulose ; kinetic Monte Carlo simulation ; Lignin ; Macroscopic models ; model predictive control ; Modelling ; multiscale modeling ; Phase transitions ; Pore size ; Porosity ; Pulp ; pulp digester ; Purdue model ; Solid phases ; State estimation</subject><ispartof>AIChE journal, 2019-06, Vol.65 (6), p.n/a</ispartof><rights>Published 2019. 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The simulation results demonstrated that the proposed methodology was able to regulate both the Kappa number and porosity to desired values.</description><subject>Algorithms</subject><subject>Cellulose</subject><subject>Computer simulation</subject><subject>Digesters</subject><subject>Feedback control</subject><subject>Hemicellulose</subject><subject>kinetic Monte Carlo simulation</subject><subject>Lignin</subject><subject>Macroscopic models</subject><subject>model predictive control</subject><subject>Modelling</subject><subject>multiscale modeling</subject><subject>Phase transitions</subject><subject>Pore size</subject><subject>Porosity</subject><subject>Pulp</subject><subject>pulp digester</subject><subject>Purdue model</subject><subject>Solid phases</subject><subject>State estimation</subject><issn>0001-1541</issn><issn>1547-5905</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNp1kMtOwzAQRS0EEqWw4A8ssWKR1o84sZdVxaOiiA3skCzHj5IqjY2TCGXHJ_CNfAmmZctqNHPPzB1dAC4xmmGEyFzVeoYLxsURmGCWlxkTiB2DCUIIZ2mAT8FZ121TR0pOJuD1cWj6utOqsXDnjW3qdgNVa6D2bR99A72DDyoEBdthV9m414KPvqv7EdYtVLBSvX77_vzqx2BhGJoATb2xXW_jOThxqunsxV-dgpfbm-flfbZ-ulstF-tMU5qLTFDGS8UMwdowbB0zWueCG-vKKhdIEGcLInClMdJGUY5EQV1VIcepdrkVdAquDndD9O9DspZbP8Q2WUpCCC04Zxgn6vpA6fR9F62TIdY7FUeJkfwNT6bw5D68xM4P7Efd2PF_UC5Wy8PGD4BOchM</recordid><startdate>201906</startdate><enddate>201906</enddate><creator>Choi, Hyun‐Kyu</creator><creator>Kwon, Joseph Sang‐Il</creator><general>John Wiley & Sons, Inc</general><general>American Institute of Chemical Engineers</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7U5</scope><scope>8FD</scope><scope>C1K</scope><scope>L7M</scope><scope>SOI</scope><orcidid>https://orcid.org/0000-0002-7903-5681</orcidid></search><sort><creationdate>201906</creationdate><title>Multiscale modeling and control of Kappa number and porosity in a batch‐type pulp digester</title><author>Choi, Hyun‐Kyu ; Kwon, Joseph Sang‐Il</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3349-93587a5d21cd51ef5dcc498def7b49092fe6291bc10cda380963fbb0f83cf4e93</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>Algorithms</topic><topic>Cellulose</topic><topic>Computer simulation</topic><topic>Digesters</topic><topic>Feedback control</topic><topic>Hemicellulose</topic><topic>kinetic Monte Carlo simulation</topic><topic>Lignin</topic><topic>Macroscopic models</topic><topic>model predictive control</topic><topic>Modelling</topic><topic>multiscale modeling</topic><topic>Phase transitions</topic><topic>Pore size</topic><topic>Porosity</topic><topic>Pulp</topic><topic>pulp digester</topic><topic>Purdue model</topic><topic>Solid phases</topic><topic>State estimation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Choi, Hyun‐Kyu</creatorcontrib><creatorcontrib>Kwon, Joseph Sang‐Il</creatorcontrib><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><jtitle>AIChE journal</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Choi, Hyun‐Kyu</au><au>Kwon, Joseph Sang‐Il</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Multiscale modeling and control of Kappa number and porosity in a batch‐type pulp digester</atitle><jtitle>AIChE journal</jtitle><date>2019-06</date><risdate>2019</risdate><volume>65</volume><issue>6</issue><epage>n/a</epage><issn>0001-1541</issn><eissn>1547-5905</eissn><abstract>This work proposes a multiscale modeling and model‐based feedback control framework for the delignification process in a batch‐type pulp digester. Specifically, we focus on a hardwood chip in the digester and develop a multiscale model capturing both the evolution of microscopic properties such as the pore size and shape distributions in the solid phase and the dynamic changes in the temperature and component concentrations in the liquor phase. While the macroscopic model adopts the continuum hypothesis based on the Purdue model, a novel microscopic model is developed using a kinetic Monte Carlo algorithm, accounting for the dissolution of lignin, cellulose, and hemicellulose contacting the liquor phase. A reduced‐order model was built to design a Luenberger observer for state estimation, which is then used to develop a model‐based control system. The simulation results demonstrated that the proposed methodology was able to regulate both the Kappa number and porosity to desired values.</abstract><cop>Hoboken, USA</cop><pub>John Wiley & Sons, Inc</pub><doi>10.1002/aic.16589</doi><tpages>12</tpages><orcidid>https://orcid.org/0000-0002-7903-5681</orcidid></addata></record> |
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subjects | Algorithms Cellulose Computer simulation Digesters Feedback control Hemicellulose kinetic Monte Carlo simulation Lignin Macroscopic models model predictive control Modelling multiscale modeling Phase transitions Pore size Porosity Pulp pulp digester Purdue model Solid phases State estimation |
title | Multiscale modeling and control of Kappa number and porosity in a batch‐type pulp digester |
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