Título: | STARTUP FLOW OF GELLED CRUDE OILS IN PIPELINES: THE ROLES OF SHRINKAGE AND IRREVERSIBLE TIME DEPENDENCE | ||||||||||||
Autor: |
BEHBOOD ABEDI |
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Colaborador(es): |
PAULO ROBERTO DE SOUZA MENDES - Orientador |
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Catalogação: | 09/NOV/2020 | Língua(s): | ENGLISH - UNITED STATES |
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Tipo: | TEXT | Subtipo: | THESIS | ||||||||||
Notas: |
[pt] Todos os dados constantes dos documentos são de inteira responsabilidade de seus autores. Os dados utilizados nas descrições dos documentos estão em conformidade com os sistemas da administração da PUC-Rio. [en] All data contained in the documents are the sole responsibility of the authors. The data used in the descriptions of the documents are in conformity with the systems of the administration of PUC-Rio. |
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Referência(s): |
[pt] https://www.maxwell.vrac.puc-rio.br/projetosEspeciais/ETDs/consultas/conteudo.php?strSecao=resultado&nrSeq=50268&idi=1 [en] https://www.maxwell.vrac.puc-rio.br/projetosEspeciais/ETDs/consultas/conteudo.php?strSecao=resultado&nrSeq=50268&idi=2 |
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DOI: | https://doi.org/10.17771/PUCRio.acad.50268 | ||||||||||||
Resumo: | |||||||||||||
Throughout the wax gelation, the network of parafinn crystals modifies
the behavior of waxy crude oil. It changes from a low viscosity Newtonian
to a high viscosity time-dependent material with yield strength. Now, it is
totally challenging to find out the restart pressure for gelled crude oil ow
with such a complex microstructure. Through my Master s dissertation, we
investigated two viscoplastic materials, namely a hair gel with a negligible
thixotropy and a quite thixotropic 2 percent aqueous suspension of Laponite to
mimic the startup flow of waxy crude oils. For both materials, the minimum
axial pressure gradient required for the onset of flow was measured, and the
measured values were in good agreement with the prediction of a conventional
force balance. On the other hand, industry cases have exhibited that the just
mentioned force balance leads to an overestimation of the minimum startup
pressure gradient. In some studies, an elicited explanation is the thixotropic
behavior of the gelled crude, but our results above-mentioned served to falsify
it. Over the first part of my PhD thesis, we aimed to verify in the laboratory
that why the force balance does not hold for gelled crude oil and then we
sought a physically proper explanation for this discrepancy and also a reliable
way to predict the minimum startup pressure gradient. Along these lines,
we show the role of gelled crude oil s shrinkage in the discordance between
static yield strength and required minimum pressure gradient to onset the
flow, through rheometry and fluid flow in a tube. Then, we introduce a
modified force balance equation with the role of shrinkage included to best
estimate the minimum restart pressure gradient. Another essential element
through the restart flow of gelled waxy crude is to find out a reliable strategy
to mathematically model the material s rheology. In most models that
aim at predicting the rheological behavior of gelled waxy crude oil, the
microstructure changes during ow are assumed to be thixotropic (reversible
time dependent). But, we observed in our experiments with well-controlled
flow and thermal histories that the irreversible character of time dependence
is quite evident. Thus, in the second part of thesis we propose a model based
on previous developments by Souza Mendes and co-workers that accounts for
the irreversible time dependence observed experimentally in a waxy crude
oil. The predictive capability of the proposed model is then assessed via
comparisons with experimental data.
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