Transport and Deposition of Large Aspect Ratio Prolate and Oblate Spheroidal Nanoparticles in Cross Flow
Document identifier: oai:DiVA.org:ltu-76979
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10.3390/pr7120886Keyword: Engineering and Technology,
Mechanical Engineering,
Fluid Mechanics and Acoustics,
Teknik och teknologier,
Maskinteknik,
Strömningsmekanik och akustik,
Transport,
Deposition,
Non-spherical particles,
Stokes flow,
Cross flow,
Boundary layers,
Composite manufacturing,
Strömningslära,
Fluid MechanicsPublication year: 2019Relevant Sustainable Development Goals (SDGs):
The SDG label(s) above have been assigned by OSDG.aiAbstract: The objective of this paper was to study the transport and deposition of non-spherical oblate and prolate shaped particles for the flow in a tube with a radial suction velocity field, with an application to experiments related to composite manufacturing. The transport of the non-spherical particles is governed by a convective diffusion equation for the probability density function, also called the Fokker–Planck equation, which is a function of the position and orientation angles. The flow is governed by the Stokes equation with an additional radial flow field. The concentration of particles is assumed to be dilute. In the solution of the Fokker–Planck equation, an expansion for small rotational Peclet numbers and large translational Peclet numbers is considered. The solution can be divided into an outer region and two boundary layer regions. The outer boundary layer region is governed by an angle-averaged convective-diffusion equation. The solution in the innermost boundary layer region is a diffusion equation including the radial variation and the orientation angles. Analytical deposition rates are calculated as a function of position along the tube axis. The contribution from the innermost boundary layer called steric- interception deposition is found to be very small. Higher order curvature and suction effects are found to increase deposition. The results are compared with results using a Lagrangian tracking method of the same flow configuration. When compared, the deposition rates are of the same order of magnitude, but the analytical results show a larger variation for different particle sizes. The results are also compared with numerical results, using the angle averaged convective-diffusion equation. The agreement between numerical and analytical results is good.
Authors
Hans O. Åkerstedt
Luleå tekniska universitet; Strömningslära och experimentell mekanik
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identifier: oai:DiVA.org:ltu-76979
datestamp: 2021-04-19T12:42:29Z
setSpec: SwePub-ltu
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recordContentSource: ltu
recordCreationDate: 2019-11-29
identifier:
http://urn.kb.se/resolve?urn=urn:nbn:se:ltu:diva-76979
10.3390/pr7120886
2-s2.0-85079675695
titleInfo:
@attributes:
lang: eng
title: Transport and Deposition of Large Aspect Ratio Prolate and Oblate Spheroidal Nanoparticles in Cross Flow
abstract: The objective of this paper was to study the transport and deposition of non-spherical oblate and prolate shaped particles for the flow in a tube with a radial suction velocity field with an application to experiments related to composite manufacturing. The transport of the non-spherical particles is governed by a convective diffusion equation for the probability density function also called the Fokker–Planck equation which is a function of the position and orientation angles. The flow is governed by the Stokes equation with an additional radial flow field. The concentration of particles is assumed to be dilute. In the solution of the Fokker–Planck equation an expansion for small rotational Peclet numbers and large translational Peclet numbers is considered. The solution can be divided into an outer region and two boundary layer regions. The outer boundary layer region is governed by an angle-averaged convective-diffusion equation. The solution in the innermost boundary layer region is a diffusion equation including the radial variation and the orientation angles. Analytical deposition rates are calculated as a function of position along the tube axis. The contribution from the innermost boundary layer called steric- interception deposition is found to be very small. Higher order curvature and suction effects are found to increase deposition. The results are compared with results using a Lagrangian tracking method of the same flow configuration. When compared the deposition rates are of the same order of magnitude but the analytical results show a larger variation for different particle sizes. The results are also compared with numerical results using the angle averaged convective-diffusion equation. The agreement between numerical and analytical results is good.
subject:
@attributes:
lang: eng
authority: uka.se
topic:
Engineering and Technology
Mechanical Engineering
Fluid Mechanics and Acoustics
@attributes:
lang: swe
authority: uka.se
topic:
Teknik och teknologier
Maskinteknik
Strömningsmekanik och akustik
@attributes:
lang: eng
topic: transport
@attributes:
lang: eng
topic: deposition
@attributes:
lang: eng
topic: non-spherical particles
@attributes:
lang: eng
topic: Stokes flow
@attributes:
lang: eng
topic: cross flow
@attributes:
lang: eng
topic: boundary layers
@attributes:
lang: eng
topic: composite manufacturing
@attributes:
lang: swe
authority: ltu
topic: Strömningslära
genre: Research subject
@attributes:
lang: eng
authority: ltu
topic: Fluid Mechanics
genre: Research subject
language:
languageTerm: eng
genre:
publication/journal-article
ref
note:
Published
1
Validerad;2019;Nivå 2;2019-12-06 (johcin)
name:
@attributes:
type: personal
authority: ltu
namePart:
Åkerstedt
Hans O.
role:
roleTerm: aut
affiliation:
Luleå tekniska universitet
Strömningslära och experimentell mekanik
nameIdentifier:
hake
0000-0002-8739-1934
originInfo:
dateIssued: 2019
publisher: MDPI
place:
placeTerm: Basel
relatedItem:
@attributes:
type: host
titleInfo:
title: Processes
identifier: 2227-9717
part:
detail:
@attributes:
type: volume
number: 7
@attributes:
type: issue
number: 12
@attributes:
type: artNo
number: 886
physicalDescription:
form: print
typeOfResource: text