Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst
Autor(a) principal: | |
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Data de Publicação: | 2021 |
Outros Autores: | , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Research, Society and Development |
Texto Completo: | https://rsdjournal.org/index.php/rsd/article/view/15452 |
Resumo: | In There are few simulation studies in the literature focusing on the production of biodiesel from vegetable oil deodorization distillate (VODD), a waste originating from the vegetable oil processing stage, using hydrotalcite-hydroxyapatite as a heterogeneous catalyst. In this study, the simulation process was performed using open interface software DWSIM® Version 6.3. The motivation relied on the positive performance of the catalyst during the experimental studies. So, in the simulator design, the lipid raw material, ethanol, and the catalyst were fed together in a CSTR-01 conversion reactor. The thermodynamic fluid package used for this process was the Non-Random Two-Liquid (NRTL) activity coefficient model. The process flowchart consisted of the reaction step (oil transesterification), and separation steps of the ethyl esters produced, excess ethanol and purification of biodiesel. As a result, different scenarios were simulated, using commercial soybean oil as a comparative form, different types of catalysts and different molar ratios of alcohol and VODD. Among the main differences between the simulated cases, it was demonstrated that the excess of alcohol (1:45) caused greater quantity of VODD consumption, and consequently the greater formation of ethyl esters (biodiesel), resulting higher conversions (> 95%). In addition, the results obtained confirmed the adequacy of VODD as a potential raw material to produce biodiesel, as it is relatively cheaper than edible oils and contributes to the use of waste. Thus, confirming that the chemical catalyst was able to form the main esters of fatty acids even using a residual raw material. |
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Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalystSimulación de proceso de producción de biodiesel a partir de destilado de desodorización de aceites vegetales utilizando hidrotalcita-hidroxiapatita como catalizadorSimulação do processo de produção de biodiesel a partir do destilado de desodorização de óleos vegetais usando hidrotalcita-hidroxiapatita como catalisadorBiodieselDWSIMCatálisis heterogéneaSimulaciónTransesterificación.BiodieselDWSIMCatálise heterogêneaSimulaçãoTransesterificação.BiodieselDWSIMHeterogeneous catalysisSimulationTransesterification.In There are few simulation studies in the literature focusing on the production of biodiesel from vegetable oil deodorization distillate (VODD), a waste originating from the vegetable oil processing stage, using hydrotalcite-hydroxyapatite as a heterogeneous catalyst. In this study, the simulation process was performed using open interface software DWSIM® Version 6.3. The motivation relied on the positive performance of the catalyst during the experimental studies. So, in the simulator design, the lipid raw material, ethanol, and the catalyst were fed together in a CSTR-01 conversion reactor. The thermodynamic fluid package used for this process was the Non-Random Two-Liquid (NRTL) activity coefficient model. The process flowchart consisted of the reaction step (oil transesterification), and separation steps of the ethyl esters produced, excess ethanol and purification of biodiesel. As a result, different scenarios were simulated, using commercial soybean oil as a comparative form, different types of catalysts and different molar ratios of alcohol and VODD. Among the main differences between the simulated cases, it was demonstrated that the excess of alcohol (1:45) caused greater quantity of VODD consumption, and consequently the greater formation of ethyl esters (biodiesel), resulting higher conversions (> 95%). In addition, the results obtained confirmed the adequacy of VODD as a potential raw material to produce biodiesel, as it is relatively cheaper than edible oils and contributes to the use of waste. Thus, confirming that the chemical catalyst was able to form the main esters of fatty acids even using a residual raw material.Existen pocos estudios de simulación en la literatura con enfoque en la producción de biodiesel a partir del destilado de desodorización de aceite vegetal (DDOV), un residuo proveniente de la etapa de procesamiento del aceite vegetal, utilizando hidrotalcita-hidroxiapatita como catalizador heterogéneo. En este estudio, el proceso de simulación se realizó utilizando el software de interfaz abierta DWSIM® Versión 6.3. La motivación se basó en el desempeño positivo del catalizador durante los estudios experimentales. Así, en el proyecto del simulador, la materia prima lipídica, el etanol y el catalizador se alimentaron juntos en un reactor de conversión CSTR-01. El paquete de fluido termodinámico utilizado para este proceso fue el modelo de coeficiente de actividad de dos líquidos no aleatorios (NRTL). El diagrama de flujo del proceso consistió en la etapa de reacción (transesterificación de aceite) y etapas de separación de los ésteres etílicos producidos, etanol en exceso y purificación del biodiesel. Como resultado, se simularon diferentes escenarios, utilizando aceite de soja comercial como forma comparativa, diferentes tipos de catalizadores y diferentes relaciones molares de alcohol y DDOV. Entre las principales diferencias entre los casos simulados, se demostró que el exceso de alcohol (1:45) provocó una mayor cantidad de consumo de DDOV y, en consecuencia, una mayor formación de ésteres etílicos (biodiesel), resultando en mayores conversiones (> 95 %). Además, los resultados obtenidos confirmaron la idoneidad del DDOV como materia prima con potencial para la producción de biodiésel, ya que es relativamente más económico que los aceites comestibles y contribuye al aprovechamiento de residuos. De esta forma, se demostró que el catalizador químico era capaz de formar los principales ésteres de ácidos grasos incluso utilizando una materia prima residual.Existem poucos estudos de simulação na literatura com foco na produção de biodiesel a partir do destilado da desodorização de óleo vegetal (DDOV), um resíduo originado da etapa de processamento do óleo vegetal, utilizando hidrotalcita-hidroxiapatita como catalisador heterogêneo. Neste estudo, o processo de simulação foi realizado no software de interface aberta DWSIM® Versão 6.3. A motivação baseou-se no desempenho positivo do catalisador durante os estudos experimentais. Assim, no projeto do simulador, a matéria-prima lipídica, o etanol e o catalisador foram alimentados juntos em um reator de conversão CSTR-01. O pacote de fluido termodinâmico usado para este processo foi o modelo de coeficiente de atividade de dois líquidos não aleatórios (NRTL). O fluxograma do processo consistiu na etapa de reação (transesterificação do óleo), e etapas de separação dos ésteres etílicos produzidos, excesso de etanol e purificação do biodiesel. Como resultado, diferentes cenários foram simulados, usando óleo de soja comercial como forma comparativa, diferentes tipos de catalisadores e diferentes razões molares de álcool e DDOV. Dentre as principais diferenças entre os casos simulados, foi demonstrado que o excesso de álcool (1:45) ocasionou maior quantidade de consumo de DDOV e, consequentemente, maior formação de ésteres etílicos (biodiesel), resultando em maiores conversões (> 95%). Além disso, os resultados obtidos confirmaram a adequação do DDOV como matéria-prima com potencial para a produção de biodiesel, por ser relativamente mais barato que os óleos comestíveis e contribuir para o aproveitamento de resíduos. Assim, comprovando que o catalisador químico foi capaz de formar os principais ésteres dos ácidos graxos mesmo utilizando uma matéria-prima residual.Research, Society and Development2021-05-26info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionapplication/pdfhttps://rsdjournal.org/index.php/rsd/article/view/1545210.33448/rsd-v10i6.15452Research, Society and Development; Vol. 10 No. 6; e15210615452Research, Society and Development; Vol. 10 Núm. 6; e15210615452Research, Society and Development; v. 10 n. 6; e152106154522525-3409reponame:Research, Society and Developmentinstname:Universidade Federal de Itajubá (UNIFEI)instacron:UNIFEIenghttps://rsdjournal.org/index.php/rsd/article/view/15452/13990Copyright (c) 2021 Laura A. de Almeida; Renata N. Vilas Bôas; Marisa F. Mendeshttps://creativecommons.org/licenses/by/4.0info:eu-repo/semantics/openAccessAlmeida, Laura A. deVilas Bôas, Renata N.Mendes, Marisa F.2021-06-10T22:51:46Zoai:ojs.pkp.sfu.ca:article/15452Revistahttps://rsdjournal.org/index.php/rsd/indexPUBhttps://rsdjournal.org/index.php/rsd/oairsd.articles@gmail.com2525-34092525-3409opendoar:2024-01-17T09:36:16.565453Research, Society and Development - Universidade Federal de Itajubá (UNIFEI)false |
dc.title.none.fl_str_mv |
Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst Simulación de proceso de producción de biodiesel a partir de destilado de desodorización de aceites vegetales utilizando hidrotalcita-hidroxiapatita como catalizador Simulação do processo de produção de biodiesel a partir do destilado de desodorização de óleos vegetais usando hidrotalcita-hidroxiapatita como catalisador |
title |
Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst |
spellingShingle |
Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst Almeida, Laura A. de Biodiesel DWSIM Catálisis heterogénea Simulación Transesterificación. Biodiesel DWSIM Catálise heterogênea Simulação Transesterificação. Biodiesel DWSIM Heterogeneous catalysis Simulation Transesterification. |
title_short |
Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst |
title_full |
Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst |
title_fullStr |
Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst |
title_full_unstemmed |
Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst |
title_sort |
Process simulation of biodiesel production from vegetable oil deodorization distillate using hydrotalcite-hydroxyapatite as catalyst |
author |
Almeida, Laura A. de |
author_facet |
Almeida, Laura A. de Vilas Bôas, Renata N. Mendes, Marisa F. |
author_role |
author |
author2 |
Vilas Bôas, Renata N. Mendes, Marisa F. |
author2_role |
author author |
dc.contributor.author.fl_str_mv |
Almeida, Laura A. de Vilas Bôas, Renata N. Mendes, Marisa F. |
dc.subject.por.fl_str_mv |
Biodiesel DWSIM Catálisis heterogénea Simulación Transesterificación. Biodiesel DWSIM Catálise heterogênea Simulação Transesterificação. Biodiesel DWSIM Heterogeneous catalysis Simulation Transesterification. |
topic |
Biodiesel DWSIM Catálisis heterogénea Simulación Transesterificación. Biodiesel DWSIM Catálise heterogênea Simulação Transesterificação. Biodiesel DWSIM Heterogeneous catalysis Simulation Transesterification. |
description |
In There are few simulation studies in the literature focusing on the production of biodiesel from vegetable oil deodorization distillate (VODD), a waste originating from the vegetable oil processing stage, using hydrotalcite-hydroxyapatite as a heterogeneous catalyst. In this study, the simulation process was performed using open interface software DWSIM® Version 6.3. The motivation relied on the positive performance of the catalyst during the experimental studies. So, in the simulator design, the lipid raw material, ethanol, and the catalyst were fed together in a CSTR-01 conversion reactor. The thermodynamic fluid package used for this process was the Non-Random Two-Liquid (NRTL) activity coefficient model. The process flowchart consisted of the reaction step (oil transesterification), and separation steps of the ethyl esters produced, excess ethanol and purification of biodiesel. As a result, different scenarios were simulated, using commercial soybean oil as a comparative form, different types of catalysts and different molar ratios of alcohol and VODD. Among the main differences between the simulated cases, it was demonstrated that the excess of alcohol (1:45) caused greater quantity of VODD consumption, and consequently the greater formation of ethyl esters (biodiesel), resulting higher conversions (> 95%). In addition, the results obtained confirmed the adequacy of VODD as a potential raw material to produce biodiesel, as it is relatively cheaper than edible oils and contributes to the use of waste. Thus, confirming that the chemical catalyst was able to form the main esters of fatty acids even using a residual raw material. |
publishDate |
2021 |
dc.date.none.fl_str_mv |
2021-05-26 |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
https://rsdjournal.org/index.php/rsd/article/view/15452 10.33448/rsd-v10i6.15452 |
url |
https://rsdjournal.org/index.php/rsd/article/view/15452 |
identifier_str_mv |
10.33448/rsd-v10i6.15452 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
https://rsdjournal.org/index.php/rsd/article/view/15452/13990 |
dc.rights.driver.fl_str_mv |
Copyright (c) 2021 Laura A. de Almeida; Renata N. Vilas Bôas; Marisa F. Mendes https://creativecommons.org/licenses/by/4.0 info:eu-repo/semantics/openAccess |
rights_invalid_str_mv |
Copyright (c) 2021 Laura A. de Almeida; Renata N. Vilas Bôas; Marisa F. Mendes https://creativecommons.org/licenses/by/4.0 |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
application/pdf |
dc.publisher.none.fl_str_mv |
Research, Society and Development |
publisher.none.fl_str_mv |
Research, Society and Development |
dc.source.none.fl_str_mv |
Research, Society and Development; Vol. 10 No. 6; e15210615452 Research, Society and Development; Vol. 10 Núm. 6; e15210615452 Research, Society and Development; v. 10 n. 6; e15210615452 2525-3409 reponame:Research, Society and Development instname:Universidade Federal de Itajubá (UNIFEI) instacron:UNIFEI |
instname_str |
Universidade Federal de Itajubá (UNIFEI) |
instacron_str |
UNIFEI |
institution |
UNIFEI |
reponame_str |
Research, Society and Development |
collection |
Research, Society and Development |
repository.name.fl_str_mv |
Research, Society and Development - Universidade Federal de Itajubá (UNIFEI) |
repository.mail.fl_str_mv |
rsd.articles@gmail.com |
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1797052749454508032 |