Buried Waveguides With Nearly Circular Cross-Sections Produced By Solid Phase Silver Ion Exchange

1989 ◽  
Author(s):  
C. Gunther ◽  
D. Jestel ◽  
H. J. Lilienhof
2021 ◽  
pp. e00246
Author(s):  
Ana Laura Anibaletto dos Santos ◽  
Anne Caroline Cezimbra da Silva ◽  
Lilian de Lima Feltraco Lizot ◽  
Anelise Schneider ◽  
Roberta Zilles Hahn ◽  
...  

2004 ◽  
Author(s):  
Zhimei Su ◽  
Tong Liu ◽  
Lijun Kang ◽  
Yu'e Kong
Keyword(s):  

2013 ◽  
Vol 378 ◽  
pp. 213-226 ◽  
Author(s):  
Evgenii M. Sgibnev ◽  
Alexander I. Ignatiev ◽  
Nikolay V. Nikonorov ◽  
Andrei M. Efimov ◽  
Evgenii S. Postnikov

Author(s):  
Kaushik Das ◽  
Debashis Basu ◽  
Todd Mintz

The present study makes a comparative assessment of different turbulence models in simulating the flow-assisted corrosion (FAC) process for pipes with noncircular cross sections and bends, features regularly encountered in heat exchangers and other pipeline networks. The case study investigates material damage due to corrosion caused by dissolved oxygen (O2) in a stainless steel pipe carrying an aqueous solution. A discrete solid phase is also present in the solution, but the transport of the solid particles is not explicitly modeled. It is assumed that the volume fraction of the solid phase is low, so it does not affect the continuous phase. Traditional two-equation models are compared, such as isotropic eddy viscosity, standard k-ε and k-ω models, shear stress transport (SST) k-ω models, and the anisotropic Reynolds Stress Model (RSM). Computed axial and radial velocities, and turbulent kinetic energy profiles predicted by the turbulence models are compared with available experimental data. Results show that all the turbulence models provide comparable results, though the RSM model provided better predictions in certain locations. The convective and diffusive motion of dissolved O2 is calculated by solving the species transport equations. The study assumes that solid particle impingement on the pipe wall will completely remove the protective film formed by corrosion products. It is also assumed that the rate of corrosion is controlled by diffusion of O2 through the mass transfer boundary layer. Based on these assumptions, corrosion rate is calculated at the internal pipe walls. Results indicate that the predicted O2 corrosion rate along the walls varies for different turbulence models but show the same general trend and pattern.


1979 ◽  
Vol 25 (11) ◽  
pp. 1975-1977 ◽  
Author(s):  
L R Witherspoon ◽  
S E Shuler ◽  
M M Garcia ◽  
L A Zollinger

Abstract Diagnostic radionuclide imaging procedures are often used in patients whose sera are later assayed by use of 125I-labeled radioligands; thus, it is important to identify those assays that potentially may be affected by contaminating radioactivity. Results obtained with assays in which specific separation methods (solid-phase primary antibody, second antibody) or small (10--25 micdo L) sample volumes are used are little affected by the presence of such contaminating radioactivity. Less-specific techniques (polyethylene glycol, charcoal, ion-exchange resin) segregate some of the contaminant activity into the bound fraction. The degree to which such activity is protein bound and the concentration of endogenous ligand then contribute to the resulting error in dose estimation. Samples for these assays should be screened for radioactivity before the assay is begun. Inclusion of nonspecific binding tubes for patients' samples when contamination is present permits the contaminating radioactivity to be evaluated and the patient's dose concentration to be more accurately estimated.


1993 ◽  
Vol 32 (S2) ◽  
pp. 667 ◽  
Author(s):  
J. Marie Inman ◽  
Susan N. Houde-Walter ◽  
G. Neville Greaves ◽  
Andrew J. Dent ◽  
Barry R. Dobson

2009 ◽  
Vol 43 (1) ◽  
pp. 43-49 ◽  
Author(s):  
O. H. Altshuler ◽  
N. V. Malyshenko ◽  
G. J. Shkurenko ◽  
H. N. Altshuler

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