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A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions

Detalhes bibliográficos
Ano de defesa: 2020
Autor(a) principal: Bassani, Carlos Lange
Orientador(a): Não Informado pela instituição
Banca de defesa: Não Informado pela instituição
Tipo de documento: Tese
Tipo de acesso: Acesso aberto
Idioma: por
Instituição de defesa: Universidade Tecnológica Federal do Paraná
Curitiba
Brasil
Programa de Pós-Graduação em Engenharia Mecânica e de Materiais
UTFPR
Programa de Pós-Graduação: Não Informado pela instituição
Departamento: Não Informado pela instituição
País: Não Informado pela instituição
Palavras-chave em Português:
Link de acesso: http://repositorio.utfpr.edu.br/jspui/handle/1/24699
Resumo: A worldwide problem reported by oil companies is the plugging of flowlines because of gas hydrates, a crystal that forms and agglomerates causing partial or complete obstructions. This incurs in revenue losses because of production stop, and also relates to safety and environmental risks. The main production strategy consists in avoiding gas hydrates by, e.g., injecting a high volume of chemical inhibitors. In order to reduce production costs, a new strategy called hydrate management is at research, where hydrates are let form, but its stable flow needs to be assured. In this sense, a deep knowledge on off-equilibrium processes such as growth kinetics, agglomeration and transportability is required to design and manage pipelines. This thesis quantitatively describes part of these processes. Several multiscale concepts are gathered from multidisciplinary fields (heat and mass transfer, crystallization, porous media, multiphase flow), leading to new interpretations. Hydrates are porous, hydrophilic particles that act as sponges entrapping water, where crystallization occurs mainly in the capillary walls (1st new assumption). Permeation through the porous particles furnishes water to its outer surface, promoting liquid bridge formation after particles’ collision, which leads to agglomeration (2nd new assumption). Higher subcoolings are shown to promote faster sealing-up of the particles, decreasing permeation rates and causing the particles to be inert in the agglomeration-sense (called dry particles). Furthermore, additives with surfactant properties decrease the permeation rate, which explains their anti-agglomerant effects. Several mechanisms are discussed upon modeling growth kinetics and agglomeration and by further coupling with a steadystate multiphase flow model. The model sensitivity evidences that a general classification of the system can be done in four distinct types of limiting phenomena: active surface-limited, dissolution-limited, heat transfer-limited, and pressure drop-limited. For engineering purposes, the model is simplified into a dimensionless criterion that determines stable production in oil-dominant systems, having the shape of Ba ∞ Da Re -n , which relates the Damköhler and Reynolds dimensionless groups graphical abstract). This expression still needs future testing in order to retrieve the exact shape of the dimensionless groups. An absolute form that depends on subcooling, water cut, mixture velocity and interfacial properties is nevertheless proposed and preliminary test shows agreement with experimental data. This criterion evidences that, once hydrates form in oil-continuous systems, the faster the particles seal-up, the quicker the particles turn dry, and the smaller the stable agglomerate size, thus requiring smaller mixture velocities in order for particles to remain suspended. Another dimensionless group La = f (Da,Re) is proposed to further explain particle-wall interactions into predicting deposition for future studies. If ever these two new dimensionless groups show consistent in future testing and fitting against larger databases, they will represent an important advance on how engineers design flowlines using the hydrate management strategy.
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spelling A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditionsAbordagem multiescala de hidratos de gás considerando estrutura, cinética de crescimento, aglomeração e transportabilidade em condições de escoamento multifásicoEscoamento multifásicoHidratosCristalizaçãoTransferência de calorAglomeraçãoFluidodinâmica computacionalMétodos de SimulaçãoMultiphase flowHydratesCrystallizationHeat transferAgglomerationComputational fluid dynamicsSimulation methodsCNPQ::ENGENHARIAS::ENGENHARIA MECANICA::ENGENHARIA TERMICAEngenharia MecânicaA worldwide problem reported by oil companies is the plugging of flowlines because of gas hydrates, a crystal that forms and agglomerates causing partial or complete obstructions. This incurs in revenue losses because of production stop, and also relates to safety and environmental risks. The main production strategy consists in avoiding gas hydrates by, e.g., injecting a high volume of chemical inhibitors. In order to reduce production costs, a new strategy called hydrate management is at research, where hydrates are let form, but its stable flow needs to be assured. In this sense, a deep knowledge on off-equilibrium processes such as growth kinetics, agglomeration and transportability is required to design and manage pipelines. This thesis quantitatively describes part of these processes. Several multiscale concepts are gathered from multidisciplinary fields (heat and mass transfer, crystallization, porous media, multiphase flow), leading to new interpretations. Hydrates are porous, hydrophilic particles that act as sponges entrapping water, where crystallization occurs mainly in the capillary walls (1st new assumption). Permeation through the porous particles furnishes water to its outer surface, promoting liquid bridge formation after particles’ collision, which leads to agglomeration (2nd new assumption). Higher subcoolings are shown to promote faster sealing-up of the particles, decreasing permeation rates and causing the particles to be inert in the agglomeration-sense (called dry particles). Furthermore, additives with surfactant properties decrease the permeation rate, which explains their anti-agglomerant effects. Several mechanisms are discussed upon modeling growth kinetics and agglomeration and by further coupling with a steadystate multiphase flow model. The model sensitivity evidences that a general classification of the system can be done in four distinct types of limiting phenomena: active surface-limited, dissolution-limited, heat transfer-limited, and pressure drop-limited. For engineering purposes, the model is simplified into a dimensionless criterion that determines stable production in oil-dominant systems, having the shape of Ba ∞ Da Re -n , which relates the Damköhler and Reynolds dimensionless groups graphical abstract). This expression still needs future testing in order to retrieve the exact shape of the dimensionless groups. An absolute form that depends on subcooling, water cut, mixture velocity and interfacial properties is nevertheless proposed and preliminary test shows agreement with experimental data. This criterion evidences that, once hydrates form in oil-continuous systems, the faster the particles seal-up, the quicker the particles turn dry, and the smaller the stable agglomerate size, thus requiring smaller mixture velocities in order for particles to remain suspended. Another dimensionless group La = f (Da,Re) is proposed to further explain particle-wall interactions into predicting deposition for future studies. If ever these two new dimensionless groups show consistent in future testing and fitting against larger databases, they will represent an important advance on how engineers design flowlines using the hydrate management strategy.Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Petróleo Brasileiro (Petrobrás)Um problema reportado mundialmente pelas companhias de petróleo é a obstrução das linhas de produção devido à formação de hidratos de gás, um cristal que se forma e aglomera ocasionando restrições parciais ou totais. Isso leva à perda de ganho de capitais devido à parada de produção, e também pode ocasionar riscos ambientais e de segurança. A principal estratégia de produção consiste em evitar a formação de hidratos pela injeção de um volume consideravelmente grande de inibidores químicos. Visando a redução dos custos de produção, uma nova estratégia está em pesquisa, chamada de gerenciamento de hidratos (hydrate management). Esta consiste em deixar os hidratos se formar, porém em garantir (gerenciar) o seu escoamento estável sem nenhuma obstrução. Esta estratégia necessita de um conhecimento mais aprofundado dos processos fora do equilíbrio, tais como a cinética de crescimento, a aglomeração e a transportabilidade dos cristais. Esta tese descreve de uma maneira quantitativa parte destes processos. Vários conceitos multidisciplinares (transferência de calor e massa, cristalização, meio poroso, escoamento multifásico) e provenientes de diferentes escalas são explorados nesta tese, o que leva a novas interpretações dos fenômenos físicos. Os cristais de hidratos são porosos e hidrofílicos e portanto atuam como esponjas que aprisionam água, sendo que a cristalização ocorre principalmente nas paredes dos seus capilares (1ª nova consideração). A permeabilidade através da partícula porosa fornece água à sua superfície externa, promovendo a formação de pontes de líquido após a colisão entre partículas, o que leva à aglomeração (2ª nova consideração). Subresfriamentos mais altos se mostram capazes de promover um selamento rápido das partículas, diminuindo a taxa de permeabilidade e promovendo partículas inertes à aglomeração, chamadas partículas secas (dry particles). Além disso, aditivos com propriedades surfactantes diminuem a taxa de permeabilidade, o que explica o efeito antiaglomerante dos mesmos. Diversos mecanismos são discutidos a partir da modelagem da cinética de crescimento e da aglomeração de hidratos a partir de um balanço populacional acoplado a um modelo de escoamento multifásico em regime permanente. Testes de sensibilidade do modelo evidenciam uma classificação geral dos sistemas em função de quatro tipos de processos de limitação da cristalização: pelo decrescimento da superfície ativa de cristalização, pela dissolução de gás, pela transferência de calor ou pela queda de pressão. Para aplicações de engenharia, o modelo é simplificado a um critério adimensional que determina a produção estável em sistema óleo-dominante, possuindo a forma Ba ∞ Da Re -n , que relaciona os números de Damköhler e Reynolds (resumo gráfico). Esta expressão ainda necessita de mais testes para determinar o formato exato dos grupos adimensionais. Porém, uma forma absoluta (dimensional) para este critério é proposta em função do subresfriamento, da fração de água, da velocidade da mistura e das propriedades interfaciais, e apresenta concordância em comparações preliminares com dados experimentais. Este critério evidencia que, quando os hidratos de gás se formam em sistemas óleo-dominante, quanto mais rápido for o selamento da partícula, mais rápido a mesma se tornará seca, promovendo aglomerados menores e, portanto, requerendo menores velocidades para estabilizar a suspensão. Outro grupo adimensional La = f (Da,Re) é proposto para explicar interações entre partícula e parede e com aplicação para modelagem de deposição de hidratos em trabalhos futuros. Se o uso destes dois novos grupos adimensionais se mostrar consistente quando comparados e regredidos com bases de dados mais extensas, espera-se atingir um novo marco em como as linhas de produção de óleo e gás são projetadas.Universidade Tecnológica Federal do ParanáCuritibaBrasilPrograma de Pós-Graduação em Engenharia Mecânica e de MateriaisUTFPRMorales, Rigoberto Eleazar Melgarejohttps://orcid.org/0000-0003-3297-7361http://lattes.cnpq.br/5156573817670917Cameirão, Anahttps://orcid.org/0000-0001-9214-9950Morales, Rigoberto Eleazar Melgarejohttps://orcid.org/0000-0003-3297-7361http://lattes.cnpq.br/5156573817670917Marcelino Neto, Moises Alveshttps://orcid.org/0000-0001-5492-6640http://lattes.cnpq.br/2071333457212415Orlande, Helcio Rangel Barretohttps://orcid.org/0000-0002-3511-322Xhttp://lattes.cnpq.br/4195594302858278Herri, Jean Michelhttps://orcid.org/0000-0003-2285-9070Sum, Amadeu Kun WanBassani, Carlos Lange2021-04-08T18:41:15Z2021-04-08T18:41:15Z2020-12-17info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/doctoralThesisapplication/pdfBASSANI, Carlos Lange. Abordagem multiescala de hidratos de gás considerando estrutura, cinética de crescimento, aglomeração e transportabilidade em condições de escoamento multifásico. 2020. Tese (Doutorado em Engenharia Mecânica e de Materiais) - Universidade Tecnológica Federal do Paraná, Curitiba, 2020.http://repositorio.utfpr.edu.br/jspui/handle/1/24699porhttp://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessreponame:Repositório Institucional da UTFPR (da Universidade Tecnológica Federal do Paraná (RIUT))instname:Universidade Tecnológica Federal do Paraná (UTFPR)instacron:UTFPR2021-04-09T06:11:50Zoai:repositorio.utfpr.edu.br:1/24699Repositório InstitucionalPUBhttp://repositorio.utfpr.edu.br:8080/oai/requestriut@utfpr.edu.br || sibi@utfpr.edu.bropendoar:2021-04-09T06:11:50Repositório Institucional da UTFPR (da Universidade Tecnológica Federal do Paraná (RIUT)) - Universidade Tecnológica Federal do Paraná (UTFPR)false
dc.title.none.fl_str_mv A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions
Abordagem multiescala de hidratos de gás considerando estrutura, cinética de crescimento, aglomeração e transportabilidade em condições de escoamento multifásico
title A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions
spellingShingle A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions
Bassani, Carlos Lange
Escoamento multifásico
Hidratos
Cristalização
Transferência de calor
Aglomeração
Fluidodinâmica computacional
Métodos de Simulação
Multiphase flow
Hydrates
Crystallization
Heat transfer
Agglomeration
Computational fluid dynamics
Simulation methods
CNPQ::ENGENHARIAS::ENGENHARIA MECANICA::ENGENHARIA TERMICA
Engenharia Mecânica
title_short A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions
title_full A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions
title_fullStr A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions
title_full_unstemmed A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions
title_sort A multiscale approach for gas hydrates considering structure, growth kinetics, agglomeration, and transportability under multiphase flow conditions
author Bassani, Carlos Lange
author_facet Bassani, Carlos Lange
author_role author
dc.contributor.none.fl_str_mv Morales, Rigoberto Eleazar Melgarejo
https://orcid.org/0000-0003-3297-7361
http://lattes.cnpq.br/5156573817670917
Cameirão, Ana
https://orcid.org/0000-0001-9214-9950
Morales, Rigoberto Eleazar Melgarejo
https://orcid.org/0000-0003-3297-7361
http://lattes.cnpq.br/5156573817670917
Marcelino Neto, Moises Alves
https://orcid.org/0000-0001-5492-6640
http://lattes.cnpq.br/2071333457212415
Orlande, Helcio Rangel Barreto
https://orcid.org/0000-0002-3511-322X
http://lattes.cnpq.br/4195594302858278
Herri, Jean Michel
https://orcid.org/0000-0003-2285-9070
Sum, Amadeu Kun Wan
dc.contributor.author.fl_str_mv Bassani, Carlos Lange
dc.subject.por.fl_str_mv Escoamento multifásico
Hidratos
Cristalização
Transferência de calor
Aglomeração
Fluidodinâmica computacional
Métodos de Simulação
Multiphase flow
Hydrates
Crystallization
Heat transfer
Agglomeration
Computational fluid dynamics
Simulation methods
CNPQ::ENGENHARIAS::ENGENHARIA MECANICA::ENGENHARIA TERMICA
Engenharia Mecânica
topic Escoamento multifásico
Hidratos
Cristalização
Transferência de calor
Aglomeração
Fluidodinâmica computacional
Métodos de Simulação
Multiphase flow
Hydrates
Crystallization
Heat transfer
Agglomeration
Computational fluid dynamics
Simulation methods
CNPQ::ENGENHARIAS::ENGENHARIA MECANICA::ENGENHARIA TERMICA
Engenharia Mecânica
description A worldwide problem reported by oil companies is the plugging of flowlines because of gas hydrates, a crystal that forms and agglomerates causing partial or complete obstructions. This incurs in revenue losses because of production stop, and also relates to safety and environmental risks. The main production strategy consists in avoiding gas hydrates by, e.g., injecting a high volume of chemical inhibitors. In order to reduce production costs, a new strategy called hydrate management is at research, where hydrates are let form, but its stable flow needs to be assured. In this sense, a deep knowledge on off-equilibrium processes such as growth kinetics, agglomeration and transportability is required to design and manage pipelines. This thesis quantitatively describes part of these processes. Several multiscale concepts are gathered from multidisciplinary fields (heat and mass transfer, crystallization, porous media, multiphase flow), leading to new interpretations. Hydrates are porous, hydrophilic particles that act as sponges entrapping water, where crystallization occurs mainly in the capillary walls (1st new assumption). Permeation through the porous particles furnishes water to its outer surface, promoting liquid bridge formation after particles’ collision, which leads to agglomeration (2nd new assumption). Higher subcoolings are shown to promote faster sealing-up of the particles, decreasing permeation rates and causing the particles to be inert in the agglomeration-sense (called dry particles). Furthermore, additives with surfactant properties decrease the permeation rate, which explains their anti-agglomerant effects. Several mechanisms are discussed upon modeling growth kinetics and agglomeration and by further coupling with a steadystate multiphase flow model. The model sensitivity evidences that a general classification of the system can be done in four distinct types of limiting phenomena: active surface-limited, dissolution-limited, heat transfer-limited, and pressure drop-limited. For engineering purposes, the model is simplified into a dimensionless criterion that determines stable production in oil-dominant systems, having the shape of Ba ∞ Da Re -n , which relates the Damköhler and Reynolds dimensionless groups graphical abstract). This expression still needs future testing in order to retrieve the exact shape of the dimensionless groups. An absolute form that depends on subcooling, water cut, mixture velocity and interfacial properties is nevertheless proposed and preliminary test shows agreement with experimental data. This criterion evidences that, once hydrates form in oil-continuous systems, the faster the particles seal-up, the quicker the particles turn dry, and the smaller the stable agglomerate size, thus requiring smaller mixture velocities in order for particles to remain suspended. Another dimensionless group La = f (Da,Re) is proposed to further explain particle-wall interactions into predicting deposition for future studies. If ever these two new dimensionless groups show consistent in future testing and fitting against larger databases, they will represent an important advance on how engineers design flowlines using the hydrate management strategy.
publishDate 2020
dc.date.none.fl_str_mv 2020-12-17
2021-04-08T18:41:15Z
2021-04-08T18:41:15Z
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 BASSANI, Carlos Lange. Abordagem multiescala de hidratos de gás considerando estrutura, cinética de crescimento, aglomeração e transportabilidade em condições de escoamento multifásico. 2020. Tese (Doutorado em Engenharia Mecânica e de Materiais) - Universidade Tecnológica Federal do Paraná, Curitiba, 2020.
http://repositorio.utfpr.edu.br/jspui/handle/1/24699
identifier_str_mv BASSANI, Carlos Lange. Abordagem multiescala de hidratos de gás considerando estrutura, cinética de crescimento, aglomeração e transportabilidade em condições de escoamento multifásico. 2020. Tese (Doutorado em Engenharia Mecânica e de Materiais) - Universidade Tecnológica Federal do Paraná, Curitiba, 2020.
url http://repositorio.utfpr.edu.br/jspui/handle/1/24699
dc.language.iso.fl_str_mv por
language por
dc.rights.driver.fl_str_mv http://creativecommons.org/licenses/by-nc-nd/4.0/
info:eu-repo/semantics/openAccess
rights_invalid_str_mv http://creativecommons.org/licenses/by-nc-nd/4.0/
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv Universidade Tecnológica Federal do Paraná
Curitiba
Brasil
Programa de Pós-Graduação em Engenharia Mecânica e de Materiais
UTFPR
publisher.none.fl_str_mv Universidade Tecnológica Federal do Paraná
Curitiba
Brasil
Programa de Pós-Graduação em Engenharia Mecânica e de Materiais
UTFPR
dc.source.none.fl_str_mv reponame:Repositório Institucional da UTFPR (da Universidade Tecnológica Federal do Paraná (RIUT))
instname:Universidade Tecnológica Federal do Paraná (UTFPR)
instacron:UTFPR
instname_str Universidade Tecnológica Federal do Paraná (UTFPR)
instacron_str UTFPR
institution UTFPR
reponame_str Repositório Institucional da UTFPR (da Universidade Tecnológica Federal do Paraná (RIUT))
collection Repositório Institucional da UTFPR (da Universidade Tecnológica Federal do Paraná (RIUT))
repository.name.fl_str_mv Repositório Institucional da UTFPR (da Universidade Tecnológica Federal do Paraná (RIUT)) - Universidade Tecnológica Federal do Paraná (UTFPR)
repository.mail.fl_str_mv riut@utfpr.edu.br || sibi@utfpr.edu.br
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