2019
DOI: 10.1155/2019/5061216
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Effects of Fine-Grained Particles’ Migration and Clogging in Porous Media on Gas Production from Hydrate-Bearing Sediments

Abstract: The migration of fine particles in porous media has been studied for different applications, including gas production from hydrate-bearing sediments. The clogging behavior of fine particles is affected by fine particle-pore throat size ratio, fine particle concentration, ionic concentration of fluids, and single/multiphase fluid flow. While previous studies presented valuable results, the data are not enough to cover a broad range of particle types and sizes and pore throat size in natural hydrate-bearing sedi… Show more

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Cited by 15 publications
(3 citation statements)
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“…In contrast, a broad PSD would be characteristic of a catalyst with a range of particle sizes. Such catalysts tend to segment into size fractions, creating irregularities in the bed, with migration of finer particles to the bottom of the bed filling in the voids between particles increasing the pressure drop. …”
Section: Particle Size Distributionmentioning
confidence: 99%
“…In contrast, a broad PSD would be characteristic of a catalyst with a range of particle sizes. Such catalysts tend to segment into size fractions, creating irregularities in the bed, with migration of finer particles to the bottom of the bed filling in the voids between particles increasing the pressure drop. …”
Section: Particle Size Distributionmentioning
confidence: 99%
“…During early research studies and to date, a single fine particle of spherical shape on a sand grain flat surface (sphere–plate model) has been extensively used for the calculation of DLVO interactions because of the simplicity of the approach. ,,,,, A few researchers have utilized a plate–plate model for the quantification of interaction energies. , The single sphere model can be accurately used for synthetic fines and glass bead configurations, but when it comes to natural kaolinite and sand grain configurations, it can provide erroneous results because natural kaolinite has a platelet structure and must be modeled with a kaolinite platelets–IT plate model. In some studies during the last few years, ,, clustered fine particles’ detachment and combined movement were assumed instead of a single fine particle model. Recently, Chequer et al used this new idea to show that the single-colloid single-surface system is not an accurate representation of colloidal behavior in porous media and significantly underestimates the critical velocity of the fluid to initiate the fine migration.…”
Section: Fine–brine–rock Systemmentioning
confidence: 99%
“…Disadvantages of this approach include potential leaching as well as catalyst particle size distribution (Koekemoer and Luckos, 2015), which can lead to high pressure drops. (Gray et al, 2002;Rabbani et al, 2017;Jung et al, 2019) An alternative to avoid issues with the catalyst breakdown is to pump a solution of slurry through the reactor and have it mixed within the system with the substrate and hydrogen (Buisson et al, 2009), such as in the Fischer-Tropsch process (Savchenko et al, 2016) or other hydrogenation reactions (Marie et al, 2010;Hofferb et al, 2006). In this case, the catalyst is always prepared and used "fresh" and there is a potential for catalyst recycling (Molnár and Papp 2017).…”
Section: Introductionmentioning
confidence: 99%