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Moreira Neto J, Costa JM, Bonomi A, Costa AC. A Novel Kinetic Modeling of Enzymatic Hydrolysis of Sugarcane Bagasse Pretreated by Hydrothermal and Organosolv Processes. Molecules 2023; 28:5617. [PMID: 37513489 PMCID: PMC10386732 DOI: 10.3390/molecules28145617] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 06/28/2023] [Revised: 07/20/2023] [Accepted: 07/21/2023] [Indexed: 07/30/2023] Open
Abstract
Lignocellulosic biomasses have a complex and compact structure, requiring physical and/or chemical pretreatments to produce glucose before hydrolysis. Mathematical modeling of enzymatic hydrolysis highlights the interactions between cellulases and cellulose, evaluating the factors contributing to reactor scale-up and conversion rates. Furthermore, this study evaluated the influence of two pretreatments (hydrothermal and organosolv) on the kinetics of enzymatic hydrolysis of sugarcane bagasse. The kinetic parameters of the model were estimated using the Pikaia genetic algorithm with data from the experimental profiles of cellulose, cellobiose, glucose, and xylose. The model considered the phenomenon of non-productive adsorption of cellulase on lignin and inhibition of cellulase by xylose. Moreover, it included the behavior of cellulase adsorption on the substrate throughout hydrolysis and kinetic equations for obtaining xylose from xylanase-catalyzed hydrolysis of xylan. The model for both pretreatments was experimentally validated with bagasse concentration at 10% w/v. The Plackett-Burman design identified 17 kinetic parameters as significant in the behavior of process variables. In this way, the modeling and parameter estimation methodology obtained a good fit from the experimental data and a more comprehensive model.
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Affiliation(s)
- João Moreira Neto
- Department of Engineering, Federal University of Lavras, Lavras 37200-000, MG, Brazil
| | - Josiel Martins Costa
- School of Food Engineering, University of Campinas, Campinas 13083-862, SP, Brazil
| | - Antonio Bonomi
- Brazilian Biorenewables National Laboratory (LNBR), Brazilian Center for Research in Energy and Materials (CNPEM), Campinas 13083-100, SP, Brazil
| | - Aline Carvalho Costa
- Laboratory of Fermentative and Enzymatic Process Engineering, School of Chemical Engineering, University of Campinas, Campinas 13083-852, SP, Brazil
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Padierna-Vanegas D, Acosta-Pavas JC, Granados-García LM, Botero-Castro HA. Modeling Based Identifiability and Parametric Estimation of an Enzymatic Hydrolysis Process of Amylaceous Materials. ACS OMEGA 2022; 7:14544-14555. [PMID: 35557667 PMCID: PMC9088767 DOI: 10.1021/acsomega.1c06193] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 11/04/2021] [Accepted: 03/21/2022] [Indexed: 06/15/2023]
Abstract
This work presents the modeling of an enzymatic hydrolysis process of amylaceous materials considering the parameter identification problem as a basis for the construction of the model. For this, a modeling methodology is modified in order to apply the identifiability property and improve the proposed model structure. A brief theoretical explanation of the identifiability is described. This concept is based on the observability property of a nonlinear dynamic system. The used methodology is based on the phenomenological based semiphysical model (PBSM). This methodology visualizes that the structure of a dynamic model can only improve with new mass or energy balances suggested by model suppositions. Additionally, a computer algorithm is included in the methodology to validate if the model is structurally locally identifiable or know if the parameters are unidentifiable. Also, an optimization algorithm is used to obtain the numeric values of the identifiable parameters and, hence, guarantee the validity of the result. The methodology focuses on the liquefaction and saccharification stages of an enzymatic hydrolysis process. The results of the model are compared with experimental data. The comparison shows low errors of 7.96% for liquefaction and 7.35% for saccharification. These errors show a significant improvement in comparison with previous models and validate the proposed modeling methodology.
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Affiliation(s)
- Daniel Padierna-Vanegas
- Departamento
de Energía Eléctrica y Automática, Facultad de
Minas, Universidad Nacional de Colombia, Medellín 050034, Colombia
- KALMAN,
Grupo de investigación en Procesos Dinámicos, Universidad Nacional de Colombia, Medellín 050034, Colombia
| | - Juan Camilo Acosta-Pavas
- Departamento
de Procesos y Energía, Facultad de Minas, Universidad Nacional de Colombia, Medellín 050034, Colombia
- BIOFRUN,
Grupo de investigación Bioprocesos y Flujos Reactivos, Universidad Nacional de Colombia, Medellín 050034, Colombia
| | - Laura María Granados-García
- Departamento
de Energía Eléctrica y Automática, Facultad de
Minas, Universidad Nacional de Colombia, Medellín 050034, Colombia
| | - Héctor Antonio Botero-Castro
- KALMAN,
Grupo de investigación en Procesos Dinámicos, Universidad Nacional de Colombia, Medellín 050034, Colombia
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Liang E, Zhang S, Liu B, Qi B, Nie Y, Yuan Z. Mathematical Modeling for the Industrial 2-Mercaptobenzothiazole Batch Production Process. ACS OMEGA 2022; 7:6963-6977. [PMID: 35252688 PMCID: PMC8892915 DOI: 10.1021/acsomega.1c06646] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Grants] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 11/23/2021] [Accepted: 02/08/2022] [Indexed: 06/14/2023]
Abstract
As an important chemical intermediate, 2-mercaptobenzothiazole (MBT) is widely used in various processes, especially in the rubber industry. However, there is no first-principles model that describes the synthetic process of MBT. This paper focuses on the formulation of a reliable mathematical model represented by a series of differential and algebraic equations for the industrial batch MBT production process. It is difficult to estimate all of the unknown parameters in the model because of the lack of sufficient industrial/experimental data. Thus, a reduced estimable parameter set is derived by performing estimability analysis on the original estimation problem. A multiple-starting-point strategy is then applied to numerically solve the non-convex parameter estimation problem with the weighted least-squares approach. Subsequently, a cross-validation technique is employed to evaluate the generalizability of the proposed model. Finally, it is confirmed that the proposed model produces encouraging prediction performance with regard to independent test data.
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Affiliation(s)
- Enzhi Liang
- State
Key Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
| | - Song Zhang
- China
Sunsine Chemical Holdings Ltd., Shanxian City, Shandong 274300, China
| | - Bin Liu
- China
Sunsine Chemical Holdings Ltd., Shanxian City, Shandong 274300, China
| | - Bujin Qi
- China
Sunsine Chemical Holdings Ltd., Shanxian City, Shandong 274300, China
| | - Yanpei Nie
- China
Sunsine Chemical Holdings Ltd., Shanxian City, Shandong 274300, China
| | - Zhihong Yuan
- State
Key Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
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Monclaro AV, Gorgulho Silva CDO, Gomes HAR, Moreira LRDS, Filho EXF. The enzyme interactome concept in filamentous fungi linked to biomass valorization. BIORESOURCE TECHNOLOGY 2022; 344:126200. [PMID: 34710591 DOI: 10.1016/j.biortech.2021.126200] [Citation(s) in RCA: 14] [Impact Index Per Article: 7.0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 08/28/2021] [Revised: 10/19/2021] [Accepted: 10/20/2021] [Indexed: 05/15/2023]
Abstract
Biomass represents an abundant and inexpensive source of sugars and aromatic compounds that can be used as raw materials for conversion into value-added bioproducts. Filamentous fungi are sources of plant cell wall degrading enzymes in nature. Understanding the interactions between enzymes is crucial for optimizing biomass degradation processes. Herein, the concept of the interactome is presented as a holistic approach that depicts the interactions among enzymes, substrates, metabolites, and inhibitors. The interactome encompasses several stages of biomass degradation, starting with the sensing of the substrate and the subsequent synthesis of hydrolytic and oxidative enzymes (fungus-substrate interaction). Enzyme-enzyme interactions are exemplified in the complex processes of lignocellulosic biomass degradation. The enzyme-substrate-metabolite-inhibitor interaction also provides a better understanding of biomass conversion, allowing bioproduct production from recalcitrant agro-industrial residues, thus bringing greater value to residual biomass. Finally, technological applications are presented for optimizing the interactome at various levels.
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Affiliation(s)
- Antonielle Vieira Monclaro
- Center for Microbial Ecology and Technology (CMET), Department of Biotechnology, Faculty of Bioscience Engineering, Ghent University, Coupure Links 653, 9000 Ghent, Belgium; Center for Advanced Process Technology and Urban Resource Efficiency (CAPTURE), Frieda Saeysstraat, 9052 Ghent, Belgium
| | - Caio de Oliveira Gorgulho Silva
- Faculty of Chemistry, Biotechnology and Food Science, Norwegian University of Life Sciences (NMBU), P.O. Box 5003, 1432 Ås, Norway; Protein Chemistry and Enzyme Technology Section, DTU Bioengineering, Department of Biotechnology and Biomedicine, Technical University of Denmark, 2800 Kgs Lyngby, Denmark
| | - Helder Andrey Rocha Gomes
- Health Science School, University Center of the Federal District (UDF), DF, Brasília 70390045, Brazil
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Zhang Y, Zhang Y, Song M, Topakas E, Yu Q, Yuan Z, Wang Z, Guo Y. Combining Michaelis-Menten theory and enzyme deactivation reactions for the kinetic study of enzymatic hydrolysis by different pretreated sugarcane bagasse. Process Biochem 2021. [DOI: 10.1016/j.procbio.2021.03.023] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Submit a Manuscript] [Subscribe] [Scholar Register] [Indexed: 10/21/2022]
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