Modelling of ammonia absorption process: falling film and packed column

Detalhes bibliográficos
Autor(a) principal: Santa Rosa, Licianne Pimentel
Data de Publicação: 2021
Tipo de documento: Tese
Idioma: eng
Título da fonte: Repositório Institucional da UFBA
Texto Completo: http://repositorio.ufba.br/ri/handle/ri/33568
Resumo: Absorbers belong to the group of industrial equipment used for separation/ purification of process streams. Among the equipment to promote the absorption, falling film and packed column have an extensively application in industrial plants. So, this thesis aims to propose a phenomenological model for a falling film absorber and to carry out a comparative study between it and a packed column. The falling film model is described by differential mass and energy balances coupled with algebraic equations representing the mass and energy transfer as well as the phase-equilibrium. This modeling approach based on a full DAE (Differential and Algebraic Equations) set is more robust and flexible than the usual approach reported in the literature, wherein sequential algorithms are specifically tailored to solve them model. A packed absorption column is designed by empirical correlations and simulated in Aspen Plus. This thesis also investigates the rigorous thermodynamic description of two possible working fluids: NH3-H2O and the electrolyte system NH3-H2O-CO2. The absorbers and thermodynamics models results are in accordance with the experimental data from literature. Regarding the comparative study of the absorbers, the technical analysis is based on phenomenological models to predict the efficiency of absorption, monitoring the temperature and concentration profiles. The economic analysis of the absorbers is based on the estimation of the investment and installation cost. The comparative study between the absorbers shows that the falling film type absorber has greater absorption capacity and it is 33% more compact than the column, although at the expense of doubling the investment. For higher concentration, the results suggest that the falling film absorber is preferable than the packed column.
id UFBA-2_78283e650b2ee4d9bb649aadeb052dcc
oai_identifier_str oai:repositorio.ufba.br:ri/33568
network_acronym_str UFBA-2
network_name_str Repositório Institucional da UFBA
repository_id_str 1932
spelling Santa Rosa, Licianne PimentelPontes, Karen ValverdeCosta, Glória Meyberg NunesPontes, Karen ValverdeFontes, Cristiano Hora de OliveiraAlves, Rita Maria de BritoMaciel, Maria Regina WolfPessoa, Fernando Luiz Pellegrini2021-06-14T16:47:19Z2021-06-14T16:47:19Z2021-06-142021-04-16Tesehttp://repositorio.ufba.br/ri/handle/ri/33568Absorbers belong to the group of industrial equipment used for separation/ purification of process streams. Among the equipment to promote the absorption, falling film and packed column have an extensively application in industrial plants. So, this thesis aims to propose a phenomenological model for a falling film absorber and to carry out a comparative study between it and a packed column. The falling film model is described by differential mass and energy balances coupled with algebraic equations representing the mass and energy transfer as well as the phase-equilibrium. This modeling approach based on a full DAE (Differential and Algebraic Equations) set is more robust and flexible than the usual approach reported in the literature, wherein sequential algorithms are specifically tailored to solve them model. A packed absorption column is designed by empirical correlations and simulated in Aspen Plus. This thesis also investigates the rigorous thermodynamic description of two possible working fluids: NH3-H2O and the electrolyte system NH3-H2O-CO2. The absorbers and thermodynamics models results are in accordance with the experimental data from literature. Regarding the comparative study of the absorbers, the technical analysis is based on phenomenological models to predict the efficiency of absorption, monitoring the temperature and concentration profiles. The economic analysis of the absorbers is based on the estimation of the investment and installation cost. The comparative study between the absorbers shows that the falling film type absorber has greater absorption capacity and it is 33% more compact than the column, although at the expense of doubling the investment. For higher concentration, the results suggest that the falling film absorber is preferable than the packed column.Submitted by LICIANNE PIMENTEL ROSA (liciannepimentel@hotmail.com) on 2021-06-11T00:03:47Z No. of bitstreams: 1 TESE_LICIANNE_FINAL.pdf: 7287650 bytes, checksum: 80c9627b9ae51a790412daaf96a18345 (MD5)Approved for entry into archive by Escola Politécnica Biblioteca (biengproc@ufba.br) on 2021-06-14T16:47:19Z (GMT) No. of bitstreams: 1 TESE_LICIANNE_FINAL.pdf: 7287650 bytes, checksum: 80c9627b9ae51a790412daaf96a18345 (MD5)Made available in DSpace on 2021-06-14T16:47:19Z (GMT). No. of bitstreams: 1 TESE_LICIANNE_FINAL.pdf: 7287650 bytes, checksum: 80c9627b9ae51a790412daaf96a18345 (MD5)CAPES e CNPQEngenharia QuímicaEngenharias IIIFalling filmAmmonia and waterPacked columnAbsorptionModelling of ammonia absorption process: falling film and packed columninfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/doctoralThesisEscola PolitécnicaPrograma de Pós Graduação em Engenharia IndustrialUFBABrasilinfo:eu-repo/semantics/openAccessengreponame:Repositório Institucional da UFBAinstname:Universidade Federal da Bahia (UFBA)instacron:UFBAORIGINALTESE_LICIANNE_FINAL.pdfTESE_LICIANNE_FINAL.pdfapplication/pdf7287650https://repositorio.ufba.br/bitstream/ri/33568/1/TESE_LICIANNE_FINAL.pdf80c9627b9ae51a790412daaf96a18345MD51LICENSElicense.txtlicense.txttext/plain1442https://repositorio.ufba.br/bitstream/ri/33568/2/license.txte3e6f4a9287585a60c07547815529482MD52TEXTTESE_LICIANNE_FINAL.pdf.txtTESE_LICIANNE_FINAL.pdf.txtExtracted texttext/plain348298https://repositorio.ufba.br/bitstream/ri/33568/3/TESE_LICIANNE_FINAL.pdf.txt8c5c0cd5f7128ebb151d80abbdc17b67MD53ri/335682022-03-16 22:06:10.828oai:repositorio.ufba.br:ri/33568VGVybW8gZGUgTGljZW4/YSwgbj9vIGV4Y2x1c2l2bywgcGFyYSBvIGRlcD9zaXRvIG5vIFJlcG9zaXQ/cmlvIEluc3RpdHVjaW9uYWwgZGEgVUZCQS4KCiBQZWxvIHByb2Nlc3NvIGRlIHN1Ym1pc3M/Pz8/byBkZSBkb2N1bWVudG9zLCBvIGF1dG9yIG91IHNldSByZXByZXNlbnRhbnRlIGxlZ2FsLCBhbyBhY2VpdGFyIGVzc2UgdGVybW8gZGUgbGljZW4/Pz8/YSwgY29uY2VkZSBhbyBSZXBvc2l0Pz8/P3JpbyBJbnN0aXR1Y2lvbmFsIGRhIFVuaXZlcnNpZGFkZSBGZWRlcmFsIGRhIEJhaGlhIG8gZGlyZWl0byBkZSBtYW50ZXIgdW1hIGM/Pz8/cGlhIGVtIHNldSByZXBvc2l0Pz8/P3JpbyBjb20gYSBmaW5hbGlkYWRlLCBwcmltZWlyYSwgZGUgcHJlc2VydmE/Pz8/Pz8/P28uIAoKRXNzZXMgdGVybW9zLCBuPz8/P28gZXhjbHVzaXZvcywgbWFudD8/Pz9tIG9zIGRpcmVpdG9zIGRlIGF1dG9yL2NvcHlyaWdodCwgbWFzIGVudGVuZGUgbyBkb2N1bWVudG8gY29tbyBwYXJ0ZSBkbyBhY2Vydm8gaW50ZWxlY3R1YWwgZGVzc2EgVW5pdmVyc2lkYWRlLgoKIFBhcmEgb3MgZG9jdW1lbnRvcyBwdWJsaWNhZG9zIGNvbSByZXBhc3NlIGRlIGRpcmVpdG9zIGRlIGRpc3RyaWJ1aT8/Pz8/Pz8/bywgZXNzZSB0ZXJtbyBkZSBsaWNlbj8/Pz9hIGVudGVuZGUgcXVlOgoKIE1hbnRlbmRvIG9zIGRpcmVpdG9zIGF1dG9yYWlzLCByZXBhc3NhZG9zIGEgdGVyY2Vpcm9zLCBlbSBjYXNvIGRlIHB1YmxpY2E/Pz8/Pz8/P2VzLCBvIHJlcG9zaXQ/Pz8/cmlvIHBvZGUgcmVzdHJpbmdpciBvIGFjZXNzbyBhbyB0ZXh0byBpbnRlZ3JhbCwgbWFzIGxpYmVyYSBhcyBpbmZvcm1hPz8/Pz8/Pz9lcyBzb2JyZSBvIGRvY3VtZW50byAoTWV0YWRhZG9zIGRlc2NyaXRpdm9zKS4KCiBEZXN0YSBmb3JtYSwgYXRlbmRlbmRvIGFvcyBhbnNlaW9zIGRlc3NhIHVuaXZlcnNpZGFkZSBlbSBtYW50ZXIgc3VhIHByb2R1Pz8/Pz8/Pz9vIGNpZW50Pz8/P2ZpY2EgY29tIGFzIHJlc3RyaT8/Pz8/Pz8/ZXMgaW1wb3N0YXMgcGVsb3MgZWRpdG9yZXMgZGUgcGVyaT8/Pz9kaWNvcy4KCiBQYXJhIGFzIHB1YmxpY2E/Pz8/Pz8/P2VzIHNlbSBpbmljaWF0aXZhcyBxdWUgc2VndWVtIGEgcG9sPz8/P3RpY2EgZGUgQWNlc3NvIEFiZXJ0bywgb3MgZGVwPz8/P3NpdG9zIGNvbXB1bHM/Pz8/cmlvcyBuZXNzZSByZXBvc2l0Pz8/P3JpbyBtYW50Pz8/P20gb3MgZGlyZWl0b3MgYXV0b3JhaXMsIG1hcyBtYW50Pz8/P20gYWNlc3NvIGlycmVzdHJpdG8gYW9zIG1ldGFkYWRvcyBlIHRleHRvIGNvbXBsZXRvLiBBc3NpbSwgYSBhY2VpdGE/Pz8/Pz8/P28gZGVzc2UgdGVybW8gbj8/Pz9vIG5lY2Vzc2l0YSBkZSBjb25zZW50aW1lbnRvIHBvciBwYXJ0ZSBkZSBhdXRvcmVzL2RldGVudG9yZXMgZG9zIGRpcmVpdG9zLCBwb3IgZXN0YXJlbSBlbSBpbmljaWF0aXZhcyBkZSBhY2Vzc28gYWJlcnRvLgo=Repositório InstitucionalPUBhttp://192.188.11.11:8080/oai/requestopendoar:19322022-03-17T01:06:10Repositório Institucional da UFBA - Universidade Federal da Bahia (UFBA)false
dc.title.pt_BR.fl_str_mv Modelling of ammonia absorption process: falling film and packed column
title Modelling of ammonia absorption process: falling film and packed column
spellingShingle Modelling of ammonia absorption process: falling film and packed column
Santa Rosa, Licianne Pimentel
Engenharia Química
Engenharias III
Falling film
Ammonia and water
Packed column
Absorption
title_short Modelling of ammonia absorption process: falling film and packed column
title_full Modelling of ammonia absorption process: falling film and packed column
title_fullStr Modelling of ammonia absorption process: falling film and packed column
title_full_unstemmed Modelling of ammonia absorption process: falling film and packed column
title_sort Modelling of ammonia absorption process: falling film and packed column
author Santa Rosa, Licianne Pimentel
author_facet Santa Rosa, Licianne Pimentel
author_role author
dc.contributor.author.fl_str_mv Santa Rosa, Licianne Pimentel
dc.contributor.advisor1.fl_str_mv Pontes, Karen Valverde
dc.contributor.advisor-co1.fl_str_mv Costa, Glória Meyberg Nunes
dc.contributor.referee1.fl_str_mv Pontes, Karen Valverde
Fontes, Cristiano Hora de Oliveira
Alves, Rita Maria de Brito
Maciel, Maria Regina Wolf
Pessoa, Fernando Luiz Pellegrini
contributor_str_mv Pontes, Karen Valverde
Costa, Glória Meyberg Nunes
Pontes, Karen Valverde
Fontes, Cristiano Hora de Oliveira
Alves, Rita Maria de Brito
Maciel, Maria Regina Wolf
Pessoa, Fernando Luiz Pellegrini
dc.subject.cnpq.fl_str_mv Engenharia Química
Engenharias III
topic Engenharia Química
Engenharias III
Falling film
Ammonia and water
Packed column
Absorption
dc.subject.por.fl_str_mv Falling film
Ammonia and water
Packed column
Absorption
description Absorbers belong to the group of industrial equipment used for separation/ purification of process streams. Among the equipment to promote the absorption, falling film and packed column have an extensively application in industrial plants. So, this thesis aims to propose a phenomenological model for a falling film absorber and to carry out a comparative study between it and a packed column. The falling film model is described by differential mass and energy balances coupled with algebraic equations representing the mass and energy transfer as well as the phase-equilibrium. This modeling approach based on a full DAE (Differential and Algebraic Equations) set is more robust and flexible than the usual approach reported in the literature, wherein sequential algorithms are specifically tailored to solve them model. A packed absorption column is designed by empirical correlations and simulated in Aspen Plus. This thesis also investigates the rigorous thermodynamic description of two possible working fluids: NH3-H2O and the electrolyte system NH3-H2O-CO2. The absorbers and thermodynamics models results are in accordance with the experimental data from literature. Regarding the comparative study of the absorbers, the technical analysis is based on phenomenological models to predict the efficiency of absorption, monitoring the temperature and concentration profiles. The economic analysis of the absorbers is based on the estimation of the investment and installation cost. The comparative study between the absorbers shows that the falling film type absorber has greater absorption capacity and it is 33% more compact than the column, although at the expense of doubling the investment. For higher concentration, the results suggest that the falling film absorber is preferable than the packed column.
publishDate 2021
dc.date.submitted.none.fl_str_mv 2021-04-16
dc.date.accessioned.fl_str_mv 2021-06-14T16:47:19Z
dc.date.available.fl_str_mv 2021-06-14T16:47:19Z
dc.date.issued.fl_str_mv 2021-06-14
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/doctoralThesis
format doctoralThesis
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://repositorio.ufba.br/ri/handle/ri/33568
dc.identifier.other.none.fl_str_mv Tese
identifier_str_mv Tese
url http://repositorio.ufba.br/ri/handle/ri/33568
dc.language.iso.fl_str_mv eng
language eng
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.publisher.none.fl_str_mv Escola Politécnica
dc.publisher.program.fl_str_mv Programa de Pós Graduação em Engenharia Industrial
dc.publisher.initials.fl_str_mv UFBA
dc.publisher.country.fl_str_mv Brasil
publisher.none.fl_str_mv Escola Politécnica
dc.source.none.fl_str_mv reponame:Repositório Institucional da UFBA
instname:Universidade Federal da Bahia (UFBA)
instacron:UFBA
instname_str Universidade Federal da Bahia (UFBA)
instacron_str UFBA
institution UFBA
reponame_str Repositório Institucional da UFBA
collection Repositório Institucional da UFBA
bitstream.url.fl_str_mv https://repositorio.ufba.br/bitstream/ri/33568/1/TESE_LICIANNE_FINAL.pdf
https://repositorio.ufba.br/bitstream/ri/33568/2/license.txt
https://repositorio.ufba.br/bitstream/ri/33568/3/TESE_LICIANNE_FINAL.pdf.txt
bitstream.checksum.fl_str_mv 80c9627b9ae51a790412daaf96a18345
e3e6f4a9287585a60c07547815529482
8c5c0cd5f7128ebb151d80abbdc17b67
bitstream.checksumAlgorithm.fl_str_mv MD5
MD5
MD5
repository.name.fl_str_mv Repositório Institucional da UFBA - Universidade Federal da Bahia (UFBA)
repository.mail.fl_str_mv
_version_ 1808459628515688448