Activity Based Model Development for Esterification Reaction of‐Propionic Acid and n‐Propyl Alcohol With Solid Acidic Catalyst.
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| Title: | Activity Based Model Development for Esterification Reaction of‐Propionic Acid and n‐Propyl Alcohol With Solid Acidic Catalyst. |
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| Authors: | Velivala, Tirumalaiah1 (AUTHOR), Rayannagari, Rukmini2 (AUTHOR), Mekala, Mallaiah3 (AUTHOR) mmyadav2001@gmail.com, Chimmiri, Venkateswarlu4 (AUTHOR) |
| Source: | International Journal of Chemical Kinetics. Aug2026, Vol. 58 Issue 8, p519-529. 11p. |
| Subjects: | Esterification, Rate equation model, Propanols, Chemical kinetics, Acid catalysts, Reactive distillation, Propionic acid |
| Abstract: | The esterification reaction of n‐propyl alcohol with n‐propionic acid using Indion 140 solid catalyst is carried out in an isothermal batch reactor to produce n‐propyl propionate and water. The reaction temperature is maintained in the range of 333–353 K and the catalyst loading varies from 0.01 to 0.03 g/cc. The mole ratio of n‐propionic acid and n‐propyl alcohol varies from 1:1 to 1:6. The influence of various parameters such as temperature, catalyst loading, initial reactant molar ratio, catalyst size, and agitation speed on the reaction rate are investigated. From the experimental results, it is observed that the reaction is kinetic controlled rather than mass transfer controlled. A second‐order pseudo‐homogeneous kinetic rate equation is used to fit the experimental data. The activation energies and forward reaction rate constants are obtained from the Arrhenius plot. The comparison of the simulation results with the experimental data indicates the second‐order pseudo‐homogeneous non‐ideal kinetic model better describes the behavior of the esterification reaction. The rate equation thus developed in this work can be used in modeling and design of catalytic distillation involving esterification of propionic acid with propanol. [ABSTRACT FROM AUTHOR] |
| Copyright of International Journal of Chemical Kinetics is the property of Wiley-Blackwell and its content may not be copied or emailed to multiple sites without the copyright holder's express written permission. Additionally, content may not be used with any artificial intelligence tools or machine learning technologies. However, users may print, download, or email articles for individual use. This abstract may be abridged. No warranty is given about the accuracy of the copy. Users should refer to the original published version of the material for the full abstract. (Copyright applies to all Abstracts.) | |
| Database: | Engineering Source |
| FullText | Text: Availability: 0 |
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| Header | DbId: egs DbLabel: Engineering Source An: 194916346 AccessLevel: 6 PubType: Academic Journal PubTypeId: academicJournal PreciseRelevancyScore: 0 |
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| Items | – Name: Title Label: Title Group: Ti Data: Activity Based Model Development for Esterification Reaction of‐Propionic Acid and n‐Propyl Alcohol With Solid Acidic Catalyst. – Name: Author Label: Authors Group: Au Data: <searchLink fieldCode="AR" term="%22Velivala%2C+Tirumalaiah%22">Velivala, Tirumalaiah</searchLink><relatesTo>1</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Rayannagari%2C+Rukmini%22">Rayannagari, Rukmini</searchLink><relatesTo>2</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Mekala%2C+Mallaiah%22">Mekala, Mallaiah</searchLink><relatesTo>3</relatesTo> (AUTHOR)<i> mmyadav2001@gmail.com</i><br /><searchLink fieldCode="AR" term="%22Chimmiri%2C+Venkateswarlu%22">Chimmiri, Venkateswarlu</searchLink><relatesTo>4</relatesTo> (AUTHOR) – Name: TitleSource Label: Source Group: Src Data: <searchLink fieldCode="JN" term="%22International+Journal+of+Chemical+Kinetics%22">International Journal of Chemical Kinetics</searchLink>. Aug2026, Vol. 58 Issue 8, p519-529. 11p. – Name: Subject Label: Subjects Group: Su Data: <searchLink fieldCode="DE" term="%22Esterification%22">Esterification</searchLink><br /><searchLink fieldCode="DE" term="%22Rate+equation+model%22">Rate equation model</searchLink><br /><searchLink fieldCode="DE" term="%22Propanols%22">Propanols</searchLink><br /><searchLink fieldCode="DE" term="%22Chemical+kinetics%22">Chemical kinetics</searchLink><br /><searchLink fieldCode="DE" term="%22Acid+catalysts%22">Acid catalysts</searchLink><br /><searchLink fieldCode="DE" term="%22Reactive+distillation%22">Reactive distillation</searchLink><br /><searchLink fieldCode="DE" term="%22Propionic+acid%22">Propionic acid</searchLink> – Name: Abstract Label: Abstract Group: Ab Data: The esterification reaction of n‐propyl alcohol with n‐propionic acid using Indion 140 solid catalyst is carried out in an isothermal batch reactor to produce n‐propyl propionate and water. The reaction temperature is maintained in the range of 333–353 K and the catalyst loading varies from 0.01 to 0.03 g/cc. The mole ratio of n‐propionic acid and n‐propyl alcohol varies from 1:1 to 1:6. The influence of various parameters such as temperature, catalyst loading, initial reactant molar ratio, catalyst size, and agitation speed on the reaction rate are investigated. From the experimental results, it is observed that the reaction is kinetic controlled rather than mass transfer controlled. A second‐order pseudo‐homogeneous kinetic rate equation is used to fit the experimental data. The activation energies and forward reaction rate constants are obtained from the Arrhenius plot. The comparison of the simulation results with the experimental data indicates the second‐order pseudo‐homogeneous non‐ideal kinetic model better describes the behavior of the esterification reaction. The rate equation thus developed in this work can be used in modeling and design of catalytic distillation involving esterification of propionic acid with propanol. [ABSTRACT FROM AUTHOR] – Name: AbstractSuppliedCopyright Label: Group: Ab Data: <i>Copyright of International Journal of Chemical Kinetics is the property of Wiley-Blackwell and its content may not be copied or emailed to multiple sites without the copyright holder's express written permission. Additionally, content may not be used with any artificial intelligence tools or machine learning technologies. However, users may print, download, or email articles for individual use. This abstract may be abridged. No warranty is given about the accuracy of the copy. Users should refer to the original published version of the material for the full abstract.</i> (Copyright applies to all Abstracts.) |
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| RecordInfo | BibRecord: BibEntity: Identifiers: – Type: doi Value: 10.1002/kin.70065 Languages: – Code: eng Text: English PhysicalDescription: Pagination: PageCount: 11 StartPage: 519 Subjects: – SubjectFull: Esterification Type: general – SubjectFull: Rate equation model Type: general – SubjectFull: Propanols Type: general – SubjectFull: Chemical kinetics Type: general – SubjectFull: Acid catalysts Type: general – SubjectFull: Reactive distillation Type: general – SubjectFull: Propionic acid Type: general Titles: – TitleFull: Activity Based Model Development for Esterification Reaction of‐Propionic Acid and n‐Propyl Alcohol With Solid Acidic Catalyst. Type: main BibRelationships: HasContributorRelationships: – PersonEntity: Name: NameFull: Velivala, Tirumalaiah – PersonEntity: Name: NameFull: Rayannagari, Rukmini – PersonEntity: Name: NameFull: Mekala, Mallaiah – PersonEntity: Name: NameFull: Chimmiri, Venkateswarlu IsPartOfRelationships: – BibEntity: Dates: – D: 01 M: 08 Text: Aug2026 Type: published Y: 2026 Identifiers: – Type: issn-print Value: 05388066 Numbering: – Type: volume Value: 58 – Type: issue Value: 8 Titles: – TitleFull: International Journal of Chemical Kinetics Type: main |
| ResultId | 1 |