Production of sucroesters using solvent-free reactive systems containing emulsifiers

The transesterification reaction of sucrose and fatty acid methyl esters to produce sucroesters was experimentally evaluated using commercial emulsifiers as compatibility agents. Reactions were carried out at temperatures between 100 and 140°C, using emulsifier concentrations in the range of 5 to 15...

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Main Authors: Alvaro Orjuela, Maria fernanda Gutierrez, Andrea Suaza, Jose Luis Rivera
Format: Article
Language:English
Published: Universidad Nacional de Colombia 2018-04-01
Series:Ingeniería e Investigación
Subjects:
Online Access:https://revistas.unal.edu.co/index.php/ingeinv/article/view/61432
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spelling doaj-afdd92941ac442bd876deb74f24b05b92020-11-25T00:48:42ZengUniversidad Nacional de ColombiaIngeniería e Investigación0120-56092248-87232018-04-01381162310.15446/ing.investig.v38n1.6143247987Production of sucroesters using solvent-free reactive systems containing emulsifiersAlvaro Orjuela0Maria fernanda Gutierrez1Andrea Suaza2Jose Luis Rivera3Universidad Nacional de ColombiaUniversidad Nacional de ColombiaUniversidad Nacional de ColombiaUniversidad Nacional de ColombiaThe transesterification reaction of sucrose and fatty acid methyl esters to produce sucroesters was experimentally evaluated using commercial emulsifiers as compatibility agents. Reactions were carried out at temperatures between 100 and 140°C, using emulsifier concentrations in the range of 5 to 15 %wt, and potassium carbonate as catalyst. Fatty acid methyl esters consumption and sucroesters production was monitored by HPLC analysis of samples. Methyl esters conversions around 40 % were obtained with 68 %wt monoester content in sucroesters mixture. Despite the reaction times were reduced by operating at high temperatures and high emulsifier’s concentration, multiple substitution and color degradation were observed. Higher productivities of sucroester and higher selectivity to monoesters were obtained when potassium palmitate was used as contacting agent. The lower monoester content in the final product was obtained when using a commercial sucroester emulsifier. Results of this study can be used for preliminary process design in a solvent-free production of biobased sucroesters.https://revistas.unal.edu.co/index.php/ingeinv/article/view/61432Sucroestersolvent-freetransesterificationemulsifiersHeterogeneous
collection DOAJ
language English
format Article
sources DOAJ
author Alvaro Orjuela
Maria fernanda Gutierrez
Andrea Suaza
Jose Luis Rivera
spellingShingle Alvaro Orjuela
Maria fernanda Gutierrez
Andrea Suaza
Jose Luis Rivera
Production of sucroesters using solvent-free reactive systems containing emulsifiers
Ingeniería e Investigación
Sucroester
solvent-free
transesterification
emulsifiers
Heterogeneous
author_facet Alvaro Orjuela
Maria fernanda Gutierrez
Andrea Suaza
Jose Luis Rivera
author_sort Alvaro Orjuela
title Production of sucroesters using solvent-free reactive systems containing emulsifiers
title_short Production of sucroesters using solvent-free reactive systems containing emulsifiers
title_full Production of sucroesters using solvent-free reactive systems containing emulsifiers
title_fullStr Production of sucroesters using solvent-free reactive systems containing emulsifiers
title_full_unstemmed Production of sucroesters using solvent-free reactive systems containing emulsifiers
title_sort production of sucroesters using solvent-free reactive systems containing emulsifiers
publisher Universidad Nacional de Colombia
series Ingeniería e Investigación
issn 0120-5609
2248-8723
publishDate 2018-04-01
description The transesterification reaction of sucrose and fatty acid methyl esters to produce sucroesters was experimentally evaluated using commercial emulsifiers as compatibility agents. Reactions were carried out at temperatures between 100 and 140°C, using emulsifier concentrations in the range of 5 to 15 %wt, and potassium carbonate as catalyst. Fatty acid methyl esters consumption and sucroesters production was monitored by HPLC analysis of samples. Methyl esters conversions around 40 % were obtained with 68 %wt monoester content in sucroesters mixture. Despite the reaction times were reduced by operating at high temperatures and high emulsifier’s concentration, multiple substitution and color degradation were observed. Higher productivities of sucroester and higher selectivity to monoesters were obtained when potassium palmitate was used as contacting agent. The lower monoester content in the final product was obtained when using a commercial sucroester emulsifier. Results of this study can be used for preliminary process design in a solvent-free production of biobased sucroesters.
topic Sucroester
solvent-free
transesterification
emulsifiers
Heterogeneous
url https://revistas.unal.edu.co/index.php/ingeinv/article/view/61432
work_keys_str_mv AT alvaroorjuela productionofsucroestersusingsolventfreereactivesystemscontainingemulsifiers
AT mariafernandagutierrez productionofsucroestersusingsolventfreereactivesystemscontainingemulsifiers
AT andreasuaza productionofsucroestersusingsolventfreereactivesystemscontainingemulsifiers
AT joseluisrivera productionofsucroestersusingsolventfreereactivesystemscontainingemulsifiers
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