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in Computational Modeling of Induction Melting and Experimental Verification
> Induction Heating and Heat Treatment
Published: 09 June 2014
Fig. 23 Turbulent flow eddies of large and small scales: (a) transition of laminar flow to turbulent behind a sieve and (b) turbulent boundary layer near a flat plane and laminar flow far from the plane. Source: Ref 52
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in Computational Modeling of Induction Melting and Experimental Verification
> Induction Heating and Heat Treatment
Published: 09 June 2014
Fig. 24 Turbulent flow energy spectrum for energy containing large eddies, inertial subrange, and energy dissipation
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in Computational Modeling of Induction Melting and Experimental Verification
> Induction Heating and Heat Treatment
Published: 09 June 2014
Fig. 26 Parts of the full spectrum of turbulent flow energy resolved and/or modeled by Reynolds-averaged Navier-Stokes (RANS) equations, large-eddy simulation (LES) models, and direct numerical simulation (DNS)
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Published: 31 October 2011
Fig. 12 Effect of geometry on commercial gas cup laminar and turbulent flow as detected by real-time holographic interferometry
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Published: 31 October 2011
Fig. 13 Effect of geometry on converging cone cup laminar and turbulent flow as detected by real-time holographic interferometry
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Published: 31 October 2011
Fig. 14 Effect of geometry on venturi gas cup laminar and turbulent flow as detected by real-time holographic interferometry
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Published: 31 August 2017
Fig. 29 Oxide film inclusion stringer from turbulent flow in the gating system. Used with permission from Ref 13
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Published: 01 January 1993
Fig. 12 Effect of geometry on commercial gas cup laminar and turbulent flow as detected by real-time holographic interferometry
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Image
Published: 01 January 1993
Fig. 13 Effect of geometry on converging cone cup laminar and turbulent flow as detected by real-time holographic interferometry
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Image
Published: 01 January 1993
Fig. 14 Effect of geometry on venturi gas cup laminar and turbulent flow as detected by real-time holographic interferometry
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Series: ASM Handbook
Volume: 4C
Publisher: ASM International
Published: 09 June 2014
DOI: 10.31399/asm.hb.v04c.a0005898
EISBN: 978-1-62708-167-2
... Abstract This article focuses on the basic turbulent flow, and the thermal, mass-transfer, and hydrodynamic phenomena for use in modeling physical processes during induction melting. It provides a discussion on transport phenomena equations that includes the approximation of convective terms...
Abstract
This article focuses on the basic turbulent flow, and the thermal, mass-transfer, and hydrodynamic phenomena for use in modeling physical processes during induction melting. It provides a discussion on transport phenomena equations that includes the approximation of convective terms in the transport equation and computational schemes for the fluid dynamics equation. The aspects of computational algorithms for specific magnetohydrodynamic problems with mutual influence of the magnetic field and melt flow due to the changing shape of the free surface are also considered. The article illustrates the application of the basic equations and approaches formulated for electromagnetic field and melt turbulent flow for the numerical study of an induction crucible furnace.
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Published: 01 December 2008
Fig. 5 Reynold's number, N R , and its relationship to flow characterization. (a) N R < 2000, laminar flow. (b) 2000 ≤ N R < 20,000, turbulent flow. (c) N R ≥ 20,000, severe turbulent flow
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in Failures of Pressure Vessels and Process Piping
> Analysis and Prevention of Component and Equipment Failures
Published: 30 August 2021
Fig. 69 (a) Schematic representation of the production system. (b) Location of the pit plug and metal loss and transition of laminar fluid flow to turbulent flow
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Published: 01 January 2006
Fig. 6 Erosion-corrosion related to high coolant flow. (a) Radiator tank erosion on wall opposite inlet. (b) Tube narrowing causes increased velocity and turbulent flow.
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Published: 01 January 2002
Fig. 10 Erosion pitting caused by turbulent river water flowing through copper pipe. The typical horseshoe-shaped pits point upstream. 0.5×
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Published: 01 January 2002
Fig. 49 Erosion pitting caused by turbulent river water flowing through copper pipe. The typical horseshoe-shaped pits point upstream. Approximately 0.5× actual size
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Published: 15 January 2021
Fig. 10 Erosion pitting caused by turbulent river water flowing through copper pipe. The typical horseshoe-shaped pits point upstream. Original magnification: 0.5×
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Published: 15 January 2021
Fig. 49 Erosion pitting caused by turbulent river water flowing through copper pipe. The typical horseshoe-shaped pits point upstream. Original magnification: ~0.5× actual size
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Published: 01 February 2024
Fig. 44 Computational fluid dynamics examination of the flow and turbulence exhibited by the ASTM D6482 Tensi unit. Source: Ref 33
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Published: 01 January 2006
Fig. 25 Erosion-corrosion related to high coolant flow. (a) Radiator tank erosion on wall opposite inlet. (b) Tube narrowing causes increased velocity and turbulent flow. See the article “Engine Coolants and Coolant System Corrosion” in this Volume.
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