Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber

Detalhes bibliográficos
Autor(a) principal: Freitas, Laize Nalli de
Data de Publicação: 2023
Tipo de documento: Dissertação
Idioma: por
Título da fonte: Repositório Institucional da Universidade Federal do Espírito Santo (riUfes)
Texto Completo: http://repositorio.ufes.br/handle/10/17083
Resumo: Odorous compounds are pollutants present in the air, originating from various sources. Diffuse sources, in particular, pose a challenge when it comes to quantifying their emissions. Different techniques, categorized as indirect and direct methods, have been developed to measure emissions from these sources. One commonly used device is the Dynamic Flux Chamber (DFC) developed by the United States Environmental Protection Agency (USEPA), which allows for enclosed measurements. In the context of this study, the main objective was to investigate the global mass transfer coefficient of hydrogen sulfide (H2S) within the USEPA DFC. Spectrophotometry was employed to analyze the liquid phase during laboratory experiments conducted using the DFC. The calculated mass transfer coefficient values for H2S ranged from 2.72E-06 m/s to 10.19E-06 m/s. The impact of the mass transfer coefficient was evaluated under three different flow rates (2.5 and 10 L/min), as well as the influence of the insertion of internal fans in the chamber. The results revealed that the mass transfer coefficient was significantly affected by the flow rates (p < 0.005), with higher flow rates leading to increased coefficient values. Additionally, the presence of larger ventilators, in both flow rates, also had a significant impact (p < 0.005) on the coefficient. These findings align with previous studies, supporting the hypothesis that for hydrogen sulfide, which primarily volatilizes through the liquid phase, the friction velocities at the liquid-gas interface and in the liquid phase contribute to increased pollutant emissions and, consequently, higher mass transfer coefficients. Another important variable that influenced the coefficient was temperature, with higher values in both the liquid and gaseous phases resulting in higher mass transfer coefficient values. Overall, this study contributes to a better understanding of the mass transfer process and its influencing factors, providing valuable insights for odor control and air quality management strategies.
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spelling Furieri, Brunohttps://orcid.org/0000000297360250http://lattes.cnpq.br/6585455298349085Freitas, Laize Nalli dehttps://orcid.org/0000-0001-8737-2875http://lattes.cnpq.br/2591707240424771Santos, Jane Merihttps://orcid.org/0000000339332849http://lattes.cnpq.br/0120226021957540Paula, Igor Braga dehttps://orcid.org/0000-0002-1149-0784http://lattes.cnpq.br/1814779476910411Galvão, Elson Silvahttps://orcid.org/0000-0002-0991-877Xhttp://lattes.cnpq.br/9129029345894560Prata Junior, Ademir Abdala2024-05-30T01:42:19Z2024-05-30T01:42:19Z2023-08-02Odorous compounds are pollutants present in the air, originating from various sources. Diffuse sources, in particular, pose a challenge when it comes to quantifying their emissions. Different techniques, categorized as indirect and direct methods, have been developed to measure emissions from these sources. One commonly used device is the Dynamic Flux Chamber (DFC) developed by the United States Environmental Protection Agency (USEPA), which allows for enclosed measurements. In the context of this study, the main objective was to investigate the global mass transfer coefficient of hydrogen sulfide (H2S) within the USEPA DFC. Spectrophotometry was employed to analyze the liquid phase during laboratory experiments conducted using the DFC. The calculated mass transfer coefficient values for H2S ranged from 2.72E-06 m/s to 10.19E-06 m/s. The impact of the mass transfer coefficient was evaluated under three different flow rates (2.5 and 10 L/min), as well as the influence of the insertion of internal fans in the chamber. The results revealed that the mass transfer coefficient was significantly affected by the flow rates (p < 0.005), with higher flow rates leading to increased coefficient values. Additionally, the presence of larger ventilators, in both flow rates, also had a significant impact (p < 0.005) on the coefficient. These findings align with previous studies, supporting the hypothesis that for hydrogen sulfide, which primarily volatilizes through the liquid phase, the friction velocities at the liquid-gas interface and in the liquid phase contribute to increased pollutant emissions and, consequently, higher mass transfer coefficients. Another important variable that influenced the coefficient was temperature, with higher values in both the liquid and gaseous phases resulting in higher mass transfer coefficient values. Overall, this study contributes to a better understanding of the mass transfer process and its influencing factors, providing valuable insights for odor control and air quality management strategies.Compostos odorantes são poluentes presentes no ar, provenientes de diversas fontes. As fontes difusas, em particular, representam um desafio quando se trata de quantificar suas emissões. Diferentes técnicas, categorizadas como métodos indiretos e diretos, foram desenvolvidas para medir as emissões dessas fontes. Um dispositivo comumente usado é a Câmara de Fluxo Dinâmica (DFC) desenvolvida pela Agência de Proteção Ambiental dos Estados Unidos (USEPA), que permite medições diretas. Neste contexto, o objetivo principal deste foi investigar o coeficiente de transferência de massa global de sulfeto de hidrogênio (H2S) dentro da USEPA DFC. A espectrofotometria foi empregada para analisar a fase líquida durante os experimentos de laboratório realizados com a DFC. Os valores calculados do coeficiente de transferência de massa para H2S variaram de 2,72E-06 m/s a 10,19E-06 m/s. O impacto do coeficiente de transferência de massa foi avaliado sob três diferentes vazões (2,5 e 10 L/min), bem como a influência da inserção de ventiladores internos na câmara. Os resultados revelaram que o coeficiente de transferência de massa foi significativamente afetado pelas vazões (p < 0,005), com vazões maiores levando a maiores valores de coeficiente. Além disso, a presença de ventiladores maiores, em ambos os fluxos, também teve impacto significativo (p < 0,005) no coeficiente. Esses achados corroboram com estudos anteriores, apoiando a hipótese de que para o sulfeto de hidrogênio, cuja volatilização é dominada pela fase líquida, as velocidades de atrito na interface líquido-gás e na fase líquida contribuem para o aumento das emissões de poluentes e, consequentemente, no aumento dos valores do KL. Outra variável importante que influenciou o coeficiente foi a temperatura: quanto mais alta as temperaturas das fases líquidas e gasosas, mores foram os valores de KL. No geral, este estudo contribui para uma melhor compreensão do processo de transferência de massa e seus fatores de influência, fornecendo informações valiosas para estratégias de controle de odor e gestão da qualidade do ar.Fundação Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Texthttp://repositorio.ufes.br/handle/10/17083porUniversidade Federal do Espírito SantoMestrado em Engenharia AmbientalPrograma de Pós-Graduação em Engenharia AmbientalUFESBRCentro Tecnológicosubject.br-rjbnEngenharia SanitáriaCâmara de fluxo dinâmicaCoeficiente global de transferência de massaSulfeto de hidrogênioCompostos odorantesEspectofotometriaDetermination of the mass transfer coefficient of an odorant compound in a dynamic flow chambertitle.alternativeinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisinfo:eu-repo/semantics/openAccessreponame:Repositório Institucional da Universidade Federal do Espírito Santo (riUfes)instname:Universidade Federal do Espírito Santo (UFES)instacron:UFESORIGINALdissertation_laizenalli_compressed.pdfapplication/pdf1130213http://repositorio.ufes.br/bitstreams/53797c15-ce9b-4e9e-bc27-c48f28c18ec5/downloadbf1aaab3b36190af7625609684cd38adMD5110/170832024-09-11 14:57:42.962oai:repositorio.ufes.br:10/17083http://repositorio.ufes.brRepositório InstitucionalPUBhttp://repositorio.ufes.br/oai/requestopendoar:21082024-10-15T18:01:16.166257Repositório Institucional da Universidade Federal do Espírito Santo (riUfes) - Universidade Federal do Espírito Santo (UFES)false
dc.title.none.fl_str_mv Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber
dc.title.alternative.none.fl_str_mv title.alternative
title Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber
spellingShingle Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber
Freitas, Laize Nalli de
Engenharia Sanitária
Câmara de fluxo dinâmica
Coeficiente global de transferência de massa
Sulfeto de hidrogênio
Compostos odorantes
Espectofotometria
subject.br-rjbn
title_short Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber
title_full Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber
title_fullStr Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber
title_full_unstemmed Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber
title_sort Determination of the mass transfer coefficient of an odorant compound in a dynamic flow chamber
author Freitas, Laize Nalli de
author_facet Freitas, Laize Nalli de
author_role author
dc.contributor.authorID.none.fl_str_mv https://orcid.org/0000-0001-8737-2875
dc.contributor.authorLattes.none.fl_str_mv http://lattes.cnpq.br/2591707240424771
dc.contributor.advisor1.fl_str_mv Furieri, Bruno
dc.contributor.advisor1ID.fl_str_mv https://orcid.org/0000000297360250
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/6585455298349085
dc.contributor.author.fl_str_mv Freitas, Laize Nalli de
dc.contributor.referee1.fl_str_mv Santos, Jane Meri
dc.contributor.referee1ID.fl_str_mv https://orcid.org/0000000339332849
dc.contributor.referee1Lattes.fl_str_mv http://lattes.cnpq.br/0120226021957540
dc.contributor.referee2.fl_str_mv Paula, Igor Braga de
dc.contributor.referee2ID.fl_str_mv https://orcid.org/0000-0002-1149-0784
dc.contributor.referee2Lattes.fl_str_mv http://lattes.cnpq.br/1814779476910411
dc.contributor.referee3.fl_str_mv Galvão, Elson Silva
dc.contributor.referee3ID.fl_str_mv https://orcid.org/0000-0002-0991-877X
dc.contributor.referee3Lattes.fl_str_mv http://lattes.cnpq.br/9129029345894560
dc.contributor.referee4.fl_str_mv Prata Junior, Ademir Abdala
contributor_str_mv Furieri, Bruno
Santos, Jane Meri
Paula, Igor Braga de
Galvão, Elson Silva
Prata Junior, Ademir Abdala
dc.subject.cnpq.fl_str_mv Engenharia Sanitária
topic Engenharia Sanitária
Câmara de fluxo dinâmica
Coeficiente global de transferência de massa
Sulfeto de hidrogênio
Compostos odorantes
Espectofotometria
subject.br-rjbn
dc.subject.por.fl_str_mv Câmara de fluxo dinâmica
Coeficiente global de transferência de massa
Sulfeto de hidrogênio
Compostos odorantes
Espectofotometria
dc.subject.br-rjbn.none.fl_str_mv subject.br-rjbn
description Odorous compounds are pollutants present in the air, originating from various sources. Diffuse sources, in particular, pose a challenge when it comes to quantifying their emissions. Different techniques, categorized as indirect and direct methods, have been developed to measure emissions from these sources. One commonly used device is the Dynamic Flux Chamber (DFC) developed by the United States Environmental Protection Agency (USEPA), which allows for enclosed measurements. In the context of this study, the main objective was to investigate the global mass transfer coefficient of hydrogen sulfide (H2S) within the USEPA DFC. Spectrophotometry was employed to analyze the liquid phase during laboratory experiments conducted using the DFC. The calculated mass transfer coefficient values for H2S ranged from 2.72E-06 m/s to 10.19E-06 m/s. The impact of the mass transfer coefficient was evaluated under three different flow rates (2.5 and 10 L/min), as well as the influence of the insertion of internal fans in the chamber. The results revealed that the mass transfer coefficient was significantly affected by the flow rates (p < 0.005), with higher flow rates leading to increased coefficient values. Additionally, the presence of larger ventilators, in both flow rates, also had a significant impact (p < 0.005) on the coefficient. These findings align with previous studies, supporting the hypothesis that for hydrogen sulfide, which primarily volatilizes through the liquid phase, the friction velocities at the liquid-gas interface and in the liquid phase contribute to increased pollutant emissions and, consequently, higher mass transfer coefficients. Another important variable that influenced the coefficient was temperature, with higher values in both the liquid and gaseous phases resulting in higher mass transfer coefficient values. Overall, this study contributes to a better understanding of the mass transfer process and its influencing factors, providing valuable insights for odor control and air quality management strategies.
publishDate 2023
dc.date.issued.fl_str_mv 2023-08-02
dc.date.accessioned.fl_str_mv 2024-05-30T01:42:19Z
dc.date.available.fl_str_mv 2024-05-30T01:42:19Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/masterThesis
format masterThesis
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dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv Text
dc.publisher.none.fl_str_mv Universidade Federal do Espírito Santo
Mestrado em Engenharia Ambiental
dc.publisher.program.fl_str_mv Programa de Pós-Graduação em Engenharia Ambiental
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dc.publisher.country.fl_str_mv BR
dc.publisher.department.fl_str_mv Centro Tecnológico
publisher.none.fl_str_mv Universidade Federal do Espírito Santo
Mestrado em Engenharia Ambiental
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