Cargando…

Keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks

Heteropolyacids (HPA) with Keggin structures, such as H(3)PMo(12)O(40) (H(3)PMo), have been described as efficient catalysts in trans/esterification reactions due to their tolerance to water and free fatty acids contents, with particularly well-suited characteristics of high proton mobility and stab...

Descripción completa

Detalles Bibliográficos
Autores principales: da Conceição, Leyvison Rafael V., Reis, Cristiano E. R., de Lima, Rosemar, Cortez, Daniela V., de Castro, Heizir F.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2019
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9069312/
https://www.ncbi.nlm.nih.gov/pubmed/35530583
http://dx.doi.org/10.1039/c9ra04300d
_version_ 1784700405478850560
author da Conceição, Leyvison Rafael V.
Reis, Cristiano E. R.
de Lima, Rosemar
Cortez, Daniela V.
de Castro, Heizir F.
author_facet da Conceição, Leyvison Rafael V.
Reis, Cristiano E. R.
de Lima, Rosemar
Cortez, Daniela V.
de Castro, Heizir F.
author_sort da Conceição, Leyvison Rafael V.
collection PubMed
description Heteropolyacids (HPA) with Keggin structures, such as H(3)PMo(12)O(40) (H(3)PMo), have been described as efficient catalysts in trans/esterification reactions due to their tolerance to water and free fatty acids contents, with particularly well-suited characteristics of high proton mobility and stability. The versatile array of HPA is considerably increased when such catalysts are supported onto solid matrices. In this sense, Al(2)O(3) was assessed as support for H(3)PMo to be used in trans/esterification reactions to produce biodiesel from high-acid feedstocks. The catalyst structure was characterized and applied on trans/esterification reaction of acid oils using ethanol as acyl acceptor. A face centered composite design was employed to conduct the experimental design and results analysis, taking macaw palm oil as study model. The process achieved an optimum level of 99.8% ester content and 4.1 mm(2) s(−1) viscosity under the following reaction conditions: 190 °C reaction temperature, 50 : 1 ethanol-to-oil molar ratio and 13.0% catalyst concentration. Other tested feedstocks (fungal single cell oil and residual frying oil) were also tested promoting satisfactory results, though the parameters were found to be slightly outside the limits set by the USA (ASTM D6715) standard. The H(3)PMo/Al(2)O(3) catalyst presented good regeneration and can be reused for up to four reaction cycles and requires lower ethanol-to-oil ratio, temperature, and catalyst concentration in comparison with other data from the literature.
format Online
Article
Text
id pubmed-9069312
institution National Center for Biotechnology Information
language English
publishDate 2019
publisher The Royal Society of Chemistry
record_format MEDLINE/PubMed
spelling pubmed-90693122022-05-05 Keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks da Conceição, Leyvison Rafael V. Reis, Cristiano E. R. de Lima, Rosemar Cortez, Daniela V. de Castro, Heizir F. RSC Adv Chemistry Heteropolyacids (HPA) with Keggin structures, such as H(3)PMo(12)O(40) (H(3)PMo), have been described as efficient catalysts in trans/esterification reactions due to their tolerance to water and free fatty acids contents, with particularly well-suited characteristics of high proton mobility and stability. The versatile array of HPA is considerably increased when such catalysts are supported onto solid matrices. In this sense, Al(2)O(3) was assessed as support for H(3)PMo to be used in trans/esterification reactions to produce biodiesel from high-acid feedstocks. The catalyst structure was characterized and applied on trans/esterification reaction of acid oils using ethanol as acyl acceptor. A face centered composite design was employed to conduct the experimental design and results analysis, taking macaw palm oil as study model. The process achieved an optimum level of 99.8% ester content and 4.1 mm(2) s(−1) viscosity under the following reaction conditions: 190 °C reaction temperature, 50 : 1 ethanol-to-oil molar ratio and 13.0% catalyst concentration. Other tested feedstocks (fungal single cell oil and residual frying oil) were also tested promoting satisfactory results, though the parameters were found to be slightly outside the limits set by the USA (ASTM D6715) standard. The H(3)PMo/Al(2)O(3) catalyst presented good regeneration and can be reused for up to four reaction cycles and requires lower ethanol-to-oil ratio, temperature, and catalyst concentration in comparison with other data from the literature. The Royal Society of Chemistry 2019-07-29 /pmc/articles/PMC9069312/ /pubmed/35530583 http://dx.doi.org/10.1039/c9ra04300d Text en This journal is © The Royal Society of Chemistry https://creativecommons.org/licenses/by-nc/3.0/
spellingShingle Chemistry
da Conceição, Leyvison Rafael V.
Reis, Cristiano E. R.
de Lima, Rosemar
Cortez, Daniela V.
de Castro, Heizir F.
Keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks
title Keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks
title_full Keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks
title_fullStr Keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks
title_full_unstemmed Keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks
title_short Keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks
title_sort keggin-structure heteropolyacid supported on alumina to be used in trans/esterification of high-acid feedstocks
topic Chemistry
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9069312/
https://www.ncbi.nlm.nih.gov/pubmed/35530583
http://dx.doi.org/10.1039/c9ra04300d
work_keys_str_mv AT daconceicaoleyvisonrafaelv kegginstructureheteropolyacidsupportedonaluminatobeusedintransesterificationofhighacidfeedstocks
AT reiscristianoer kegginstructureheteropolyacidsupportedonaluminatobeusedintransesterificationofhighacidfeedstocks
AT delimarosemar kegginstructureheteropolyacidsupportedonaluminatobeusedintransesterificationofhighacidfeedstocks
AT cortezdanielav kegginstructureheteropolyacidsupportedonaluminatobeusedintransesterificationofhighacidfeedstocks
AT decastroheizirf kegginstructureheteropolyacidsupportedonaluminatobeusedintransesterificationofhighacidfeedstocks