Publication:
Laminar-transitional micropipe flows: Energy and exergy mechanisms based on Reynolds number, pipe diameter, surface roughness and wall heat flux

dc.contributor.buuauthorÖzalp, A. Alper
dc.contributor.departmentMühendislik Fakültesi
dc.contributor.departmentMakine Mühendisliği Bölümü
dc.contributor.orcid0000-0002-4976-9027
dc.contributor.researcheridABI-6888-2020
dc.contributor.scopusid6506131689
dc.date.accessioned2022-04-11T12:21:14Z
dc.date.available2022-04-11T12:21:14Z
dc.date.issued2012-01
dc.description.abstractEnergy and exergy mechanisms of laminar-transitional micropipe flows are computationally investigated by solving the variable fluid property continuity, Navier-Stokes and energy equations. Analyses are carried for wide ranges of Reynolds number (Re = 10-2,000), micropipe diameter (d = 0.50-1.00 mm), non-dimensional surface roughness (epsilon* = 0.001-0.01) and wall heat flux (q '' = 1,000-2,000 W/m(2)) conditions. Computations revealed that friction coefficient (C-f) elevates with higher epsilon* and Re and with lower d, where the rise of epsilon* from 0.001 to 0.01 induced the C-f to increase by 0.7 -> 0.9% (d = 1.00 -> 0.50 mm), 3.4 -> 4.2%, 6.6 -> 8.1%, 9.6 -> 11.9% and 12.4 -> 15.2% for Re = 100, 500, 1,000, 1,500 and 2,000, respectively. Earlier transition exposed with stronger micro-structure and surface roughness at the descriptive transitional Reynolds numbers of Re-tra = 1,656 -> 769 (epsilon* = 0.001 -> 0.01), 1,491 -> 699 and 1,272 -> 611 at d = 1.00, 0.75 and 0.50 mm; the corresponding shape factor (H) and intermittency (gamma) data appear in the narrow ranges of H = 3.135-3.142 and gamma = 0.132-0.135. At higher Re and lower d, epsilon* is determined to become more influential on the heat transfer rates, such that the Nu(epsilon*=0.01)/Nu(epsilon*=0.001) ratio attains the values of 1.002 -> 1.023 (d = 1.00 -> 0.50 mm), 1.012 -> 1.039, 1.025 -> 1.056 and 1.046 -> 1.082 at Re = 100, 500, 1,000 and 2,000. As e * comes out to cause minor variations in the cross-sectional thermal entropy generation rates (S'(Delta T)), q '' is confirmed to augment S'(Delta T), where the impact becomes more pronounced at higher Re and d. Frictional entropy generation values (S'(Delta P)) are found to be motivated by lower d, higher Re and epsilon*, such that the S'(Delta Pd=0.50mm)/S'(DPd=1.00mm) ratio is computed as 4.0011 -> 4.0014 (epsilon* = 0.001 -> 0.01), 4.002 -> 4.007, 4.006 -> 4.027 and 4.023 -> 4.102 at Re = 100, 500, 1,000 and 2,000. As the role of q '' on total entropy generation (S') turns out to be more remarkable at higher d and lower Re, the task of epsilon* becomes more sensible at higher Re.
dc.identifier.citationÖzalp, A. A. (2012). "Laminar-transitional micropipe flows: Energy and exergy mechanisms based on Reynolds number, pipe diameter, surface roughness and wall heat flux". Heat and Mass Transfer, 48(1), 17-34.
dc.identifier.endpage34
dc.identifier.issn0947-7411
dc.identifier.issn1432-1181
dc.identifier.issue1
dc.identifier.scopus2-s2.0-84856087520
dc.identifier.startpage17
dc.identifier.urihttps://doi.org/10.1007/s00231-011-0832-6
dc.identifier.urihttps://link.springer.com/article/10.1007%2Fs00231-011-0832-6
dc.identifier.urihttp://hdl.handle.net/11452/25702
dc.identifier.volume48
dc.identifier.wos000300084400002
dc.indexed.wosSCIE
dc.language.isoen
dc.publisherSpringer
dc.relation.bapM(U)-2009/35
dc.relation.journalHeat and Mass Transfer
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.subjectThermodynamics
dc.subjectMechanics
dc.subjectEntropy generation
dc.subjectForced-convection
dc.subject2nd-law analysis
dc.subjectMicrochannels
dc.subjectFriction
dc.subjectDucts
dc.subjectEntropy
dc.subjectExergy
dc.subjectHeat flux
dc.subjectNavier stokes equations
dc.subjectReynolds number
dc.subjectSurface structure
dc.subjectEnergy and exergy
dc.subjectEnergy equation
dc.subjectFriction coefficients
dc.subjectEntropy generation rate
dc.subjectHeat transfer rate
dc.subjectIntermittency
dc.subjectMicropipes
dc.subjectNavier stokes
dc.subjectPipe diameter
dc.subjectShape factor
dc.subjectTotal entropy
dc.subjectVariable fluid properties
dc.subjectWall heat flux
dc.subjectSurface roughness
dc.subject.scopusKnudsen Flow; Microchannels; Brinkman Number
dc.subject.wosThermodynamics
dc.subject.wosMechanics
dc.titleLaminar-transitional micropipe flows: Energy and exergy mechanisms based on Reynolds number, pipe diameter, surface roughness and wall heat flux
dc.typeArticle
dc.wos.quartileQ3
dspace.entity.typePublication
local.contributor.departmentMühendislik Fakültesi/Makine Mühendisliği Bölümü
local.indexed.atScopus
local.indexed.atWOS

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