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Plating cell

Mass Transport. Probably the most iavestigated physical phenomenon ia an electrode process is mass transfer ia the form of a limiting current. A limiting current density is that which is controlled by reactant supply to the electrode surface and not the appHed electrode potential (42). For a simple analysis usiag the limiting current characteristics of various correlations for flow conditions ia a parallel plate cell, see Reference 43. [Pg.88]

Eig. 5. Options for electrolyte flow through parallel plate cells (a), parallel, and (b), series flow. [Pg.90]

Two-Dimensional Electrode Flow Cells. The simplest and least expensive cell design is the undivided parallel plate cell with electrolyte flow by some form of manifold. Electrical power is monopolar to the cell pack (72). An exploded view of the Foreman and Veatch cell is shown in Figure 7. Note that electrolyte flow is in series and that it is not easily adapted for divided cell operation. [Pg.90]

Testing and Control. Analysis and testing are required whenever a new plating solution is made up, and thereafter at periodic intervals. The analyses are relatively simple and require Httie equipment (78—80). Trace metal contaminants can be analy2ed using spot tests, colorimetricaHy, and with atomic absorption spectrophotometry (see Trace and residue analysis). Additives, chemical balance, impurity effects, and many other variables are tested with small plating cells, such as the Hull cell developed in 1937 (81,82). [Pg.155]

In order to select the instmmental conditions for carrying out the ATR measurements several parameters including the number of accumulated scans per spectra or nominal resolution were tested. To avoid the crosscontamination and to establish an appropriate strategy for cleaning the ATR cell between samples, several procedures were tested using background and blank controls. Moreover, the possible sample sedimentation on the ATR plate cell due to the complexity of the sample matrix during the spectra acquisition was also checked. [Pg.142]

The metallic substrate, clean and rinsed, is immersed wet in the plating cell. The base metals which are usually plated present an essentially metallic surface to the electrolyte, and the slight corrosive action of the rinse water in preventing the formation of any substantial oxide film is important. A critical balance of corrosion processes in the initial stages is vital to successful electroplating, and for this reason there is a severe restriction on the composition of the electroplating bath which may be used for a particular substrate. This will be discussed later. The substrate is made the cathode of the cell it may be immersed without applied potential ( dead entry) or may be already part of a circuit which is completed as soon as the substrate touches the electrolyte ( live entry). Live entry reduces the tendency for the plating electrolyte to corrode the substrate in the period before the surface... [Pg.339]

Without switching the power on, connect the power supply and ammeter in a circuit with the plating cell. The copper anode is connected, via the ammeter, to the positive (red) terminal of the power supply. The key acts as the cathode and is connected to the negative (black) terminal. [Pg.166]

Another approximation to planar Couette conditions can be found in the cone-and-plate cell, shown in Figure 2.8.3. The angular speed of rotation of the cone is taken to be Q (in radians per second) while the angle of the cone is a (in radians) and is generally small, say 4-8°. A point in the fluid is defined by spherical polar (r, 0, ()>), cylindrical polar (q, z, cj)) or Cartesian (%, y, z) coordinates, where Q = y = rsin0 and z = rcos0. [Pg.188]

The gold-standard assay used for all chemokine receptor inhibitors that reach clinical-phase trials is the chemotaxis functional assay. This assay relies on the ability of chemokines to recruit cells expressing their respective receptor to areas of inflammation. In vitro, this assay was first described in detail by Taub et al. (16) for 24/48-well plates currently, this can be achieved by using 96-well plates. Cells are incubated in the upper chamber with an antagonist for a particular receptor (at different concentrations or with buffer) and challenged to migrate to the lower chamber, which has the relevant chemokine. After 2 to 4 hours of incubation at 37°C, the upper chamber inlet is removed and the cells in the lower chamber quantified by fluorescence with, for example, Calcein AM (Invitrogen, Carlsbad, CA). [Pg.379]

Fig. 11.2 Effect of HU on ET-1 release in the supernatant of the TrHBMEC (a) and EA hy 926 (b) cell cultures. Results of the quantitative assessment of ET-1 by Elisa, from at least four independent experiments in duplicates, are expressed in pg of ET-1 mb supernatant per 5x10s plated cells. Control basal culture conditions, HU cells treated with HU 250 mM during 48 h, Cyto cells treated with cytokines TNFa and IFNy at 100 U/mL 1 during 48 h, HU+cyto combination of HU and cytokines. Fig. 11.2 Effect of HU on ET-1 release in the supernatant of the TrHBMEC (a) and EA hy 926 (b) cell cultures. Results of the quantitative assessment of ET-1 by Elisa, from at least four independent experiments in duplicates, are expressed in pg of ET-1 mb supernatant per 5x10s plated cells. Control basal culture conditions, HU cells treated with HU 250 mM during 48 h, Cyto cells treated with cytokines TNFa and IFNy at 100 U/mL 1 during 48 h, HU+cyto combination of HU and cytokines.
Wash plated cells with PBS and replace with 300 fd of optiMEM. [Pg.121]

Liem, K. J., Tremmel, G., Roelink, H. and Jessel, T. Dorsal differentiation of neural plate cells induced by BMP-mediated signals from epidermal ectoderm. Cell 82 969-979, 1995. [Pg.515]

Because of its advantages (high sensitivity and selectivity, low cost and miniaturization) amperometric detection has been frequently used in flow injection analysis (FIA) and RP-HPLC. However, it has been established that the peak area (detector response) considerably depends on the flow rate. A general approach has been proposed to predict the effect of flow rate on the peak area in FIA and RP-HPLC. The general form of the correlation describing the flow in a parallel plate cell with short rectangular electrodes is... [Pg.30]

Other important parts of the cell are 1) the structure for distributing the reactant gases across the electrode surface and which serves as mechanical support, shown as ribs in Figure 1-4, 2) electrolyte reservoirs for liquid electrolyte cells to replenish electrolyte lost over life, and 3) current collectors (not shown) that provide a path for the current between the electrodes and the separator of flat plate cells. Other arrangements of gas flow and current flow are used in fuel cell stack designs, and are mentioned in Sections 3 through 8 for the various type cells. [Pg.22]

Remove and plate cells into warm (37°C) medium with the required composition for growth including serum. [Pg.66]

Figure 27. Schematic view of SOFC cyiindrical and fiat plate cell constructions. Figure 27. Schematic view of SOFC cyiindrical and fiat plate cell constructions.
In brief, deposited metal distribution depends on the shape and dimensions of the object, the geometry of the plating cell, the conductivity of the bath, the shapes of the polarization curves, CE-current density (or similar) curves, and the effect of agitation. [Pg.212]

Plate cells in 96-well flat-bottom tissue culture plates. [Pg.102]

Generate a titration curve, by plating cells at different densities and by performing MTT assays at the same time point, e.g., 2 h after plating. The absorbance value for each cell density will allow estimating the number of cells survived/proliferated at the end of your experiment. [Pg.274]

Plate cells at the appropriate density in a 96-well white/black plate. Seed 4 wells for each clone (see Note 12). [Pg.331]

Figure 12.10 Examples of structured catalytic reactors for kinetic measurements (a) annular reactor [47, 61] (b) plate cell reactor [75]. Figure 12.10 Examples of structured catalytic reactors for kinetic measurements (a) annular reactor [47, 61] (b) plate cell reactor [75].
Ye W, Shimamura K, Rubenstein JL, Hynes MA, Rosenthal A (1998) FGF and Shh signals control dopaminergic and serotonergic cell fate in the anterior neural plate. Cell 93 755-766... [Pg.112]

In most instances the specimens will be self-evident (e.g., samples of blood, plasma, serum, urine, spinal fluid, aqueous humor, organs, tissues, and tissue fractions that are taken from a test system with the intention of performing an examination or analysis). In other instances the definition may not be as clear. For example, the assay plates used in the mammalian cell transformation assay and the mammalian point mutation assay are considered specimens even though they bear many of the attributes of a test system. For these assays, the originally plated cells plus media and excipients are the test system. After treatment with the test or... [Pg.46]


See other pages where Plating cell is mentioned: [Pg.580]    [Pg.548]    [Pg.92]    [Pg.94]    [Pg.282]    [Pg.336]    [Pg.365]    [Pg.378]    [Pg.188]    [Pg.201]    [Pg.275]    [Pg.91]    [Pg.240]    [Pg.107]    [Pg.182]    [Pg.214]    [Pg.148]    [Pg.187]    [Pg.187]    [Pg.407]    [Pg.163]    [Pg.22]    [Pg.10]    [Pg.85]    [Pg.380]   
See also in sourсe #XX -- [ Pg.383 ]




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