Kinetic studies of esterification of rosin and pentaerythritol

Esterification of rosin with pentaerythritol produces rosin pentaerythritol ester (RPE) which is widely used in paint, coating, and pressure-sensitive and hot-melt adhesive industries. Although RPE has excellent valuable applications and has been industrially produced, studies on the reaction kineti...

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Main Authors: Hardhianti, Meiga Putri Wahyu, Rochmadi, Rochmadi, Azis, Muhammad Mufti
Format: Article PeerReviewed
Language:English
Published: MDPI 2022
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Online Access:https://repository.ugm.ac.id/282235/1/Hardhianti%20et%20al%20-2022%20-Kinetic%20Studies%20of%20Esterification%20of%20Rosin%20and%20Pentaerythritol.pdf
https://repository.ugm.ac.id/282235/
https://www.mdpi.com/2227-9717/10/1/39
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spelling id-ugm-repo.2822352023-11-27T00:50:23Z https://repository.ugm.ac.id/282235/ Kinetic studies of esterification of rosin and pentaerythritol Hardhianti, Meiga Putri Wahyu Rochmadi, Rochmadi Azis, Muhammad Mufti Chemical Engineering not elsewhere classified Chemical Engineering Engineering Esterification of rosin with pentaerythritol produces rosin pentaerythritol ester (RPE) which is widely used in paint, coating, and pressure-sensitive and hot-melt adhesive industries. Although RPE has excellent valuable applications and has been industrially produced, studies on the reaction kinetics have not been widely reported in the present literature. This work proposed a kinetic study of RPE synthesis by including a series of consecutive reactions forming mono-, di-, tri-, and tetra-ester with decarboxylation of rosin as a side reaction in the kinetics model. For esterification, the reaction rates were determined by the second-order kinetic model. The first-order kinetic order was proposed for decarboxylation. Kinetic experiments were performed at a temperature range of 260◦C to 290◦C. The initial molar ratio of pentaerythritol to rosin (in the mole of OH/COOH) used was between 0.8 and 1.2. A small amount of samples were withdrawn in certain time interval. The sample was analyzed to evaluate their acid and saponification number. Afterward, those experimental data were used to simulate and validate the proposed kinetic model. In general, the proposed model could capture the experimental data well. The resulting activation energies ranged from 65.81 to 129.13 kJ mol−1 for esterification and 233.00 kJ mol−1 for decarboxylation. This model also offers a new insight that correlates well with tetra-ester formation and the softening point. © 2021 by the authors. Licensee MDPI, Basel, Switzerland. MDPI 2022 Article PeerReviewed application/pdf en https://repository.ugm.ac.id/282235/1/Hardhianti%20et%20al%20-2022%20-Kinetic%20Studies%20of%20Esterification%20of%20Rosin%20and%20Pentaerythritol.pdf Hardhianti, Meiga Putri Wahyu and Rochmadi, Rochmadi and Azis, Muhammad Mufti (2022) Kinetic studies of esterification of rosin and pentaerythritol. Processes, 10 (1). pp. 1-11. ISSN 2227-9719 https://www.mdpi.com/2227-9717/10/1/39
institution Universitas Gadjah Mada
building UGM Library
continent Asia
country Indonesia
Indonesia
content_provider UGM Library
collection Repository Civitas UGM
language English
topic Chemical Engineering not elsewhere classified
Chemical Engineering
Engineering
spellingShingle Chemical Engineering not elsewhere classified
Chemical Engineering
Engineering
Hardhianti, Meiga Putri Wahyu
Rochmadi, Rochmadi
Azis, Muhammad Mufti
Kinetic studies of esterification of rosin and pentaerythritol
description Esterification of rosin with pentaerythritol produces rosin pentaerythritol ester (RPE) which is widely used in paint, coating, and pressure-sensitive and hot-melt adhesive industries. Although RPE has excellent valuable applications and has been industrially produced, studies on the reaction kinetics have not been widely reported in the present literature. This work proposed a kinetic study of RPE synthesis by including a series of consecutive reactions forming mono-, di-, tri-, and tetra-ester with decarboxylation of rosin as a side reaction in the kinetics model. For esterification, the reaction rates were determined by the second-order kinetic model. The first-order kinetic order was proposed for decarboxylation. Kinetic experiments were performed at a temperature range of 260◦C to 290◦C. The initial molar ratio of pentaerythritol to rosin (in the mole of OH/COOH) used was between 0.8 and 1.2. A small amount of samples were withdrawn in certain time interval. The sample was analyzed to evaluate their acid and saponification number. Afterward, those experimental data were used to simulate and validate the proposed kinetic model. In general, the proposed model could capture the experimental data well. The resulting activation energies ranged from 65.81 to 129.13 kJ mol−1 for esterification and 233.00 kJ mol−1 for decarboxylation. This model also offers a new insight that correlates well with tetra-ester formation and the softening point. © 2021 by the authors. Licensee MDPI, Basel, Switzerland.
format Article
PeerReviewed
author Hardhianti, Meiga Putri Wahyu
Rochmadi, Rochmadi
Azis, Muhammad Mufti
author_facet Hardhianti, Meiga Putri Wahyu
Rochmadi, Rochmadi
Azis, Muhammad Mufti
author_sort Hardhianti, Meiga Putri Wahyu
title Kinetic studies of esterification of rosin and pentaerythritol
title_short Kinetic studies of esterification of rosin and pentaerythritol
title_full Kinetic studies of esterification of rosin and pentaerythritol
title_fullStr Kinetic studies of esterification of rosin and pentaerythritol
title_full_unstemmed Kinetic studies of esterification of rosin and pentaerythritol
title_sort kinetic studies of esterification of rosin and pentaerythritol
publisher MDPI
publishDate 2022
url https://repository.ugm.ac.id/282235/1/Hardhianti%20et%20al%20-2022%20-Kinetic%20Studies%20of%20Esterification%20of%20Rosin%20and%20Pentaerythritol.pdf
https://repository.ugm.ac.id/282235/
https://www.mdpi.com/2227-9717/10/1/39
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