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Area change step type

The software driven apparatus allows different types of area changes step and ramp type, square pulse and trapezoidal as well as sinusoidal area deformations. The construction ensures that area changes are almost isotropic. Area changes used in transient and harmonic relaxation experiments are of the order of 1 to 5%. The surface tension response measured via the Wilhelmy balance has an accuracy of better than 0.1 mN/m. [Pg.220]

Polarization equations of the type (14.35) or (14.38) contain the mean values of true current density. However, the rate-determining step is more often concentrated at just a few segments of the electrode the true working area changes continuously and an exact determination of this area is practically impossible. This gives rise to difficulties in an interpretation of polarization data. [Pg.260]

Fig. 6.1. Schematic of different transient area changes (solid lines) and the corresponding interfacial tension responses (dotted lines) (a) - step type, (b) - ramp type, (c) - square pulse, (d) -trapezoidal change... Fig. 6.1. Schematic of different transient area changes (solid lines) and the corresponding interfacial tension responses (dotted lines) (a) - step type, (b) - ramp type, (c) - square pulse, (d) -trapezoidal change...
Very recently examples of rheological studies on blood were published elsewhere [242]. As an example we want to discuss some results of these investigations here. Fig. 4.45 shows the surface tension response after a step-type area change of a pendent drop area by about 10% for 6 serum samples from one and the same patient at different stages of his acute kidney insufficiency [243]. [Pg.377]

As mentioned above the oscillating drop or bubble method, based on profile analysis tensiometry, is the most recently developed method to investigate the surface relaxation of soluble adsorption layers. By increasing/decreasing the volume of a pendent drop or bubble, a variety of area changes can be performed, such as step, square pulse, ramp type, trapezoidal, and of course harmonic area changes at low frequencies. [Pg.103]

Here (0 is the oscillation frequency, and the parameter cOb is the characteristic frequency, which is inverse proportinal to the diffusion relaxation time Xd given in Eq. (35). This characteristic frequency exists also for any transient relaxation processes. The interfacial response functions for a number of transient relaxations were discussed recently by Loglio et al. (2001). Among these, the trapezoidal area change is the most general perturbation which contains area changes such as the step or ramp type and the square pulse as particular cases. [Pg.103]

Drop and bubble shape tensiometry is a modem and very effective tool for measuring dynamic and static interfacial tensions. An automatic instrument with an accurate computer controlled dosing system is discussed in detail. Due to an active control loop experiments under various conditions can be performed constant drop/bubble volume, surface area, or height, trapezoidal, ramp type, step type and sinusoidal area changes. The theoretical basis of the method, the fitting procedure to the Gauss-Laplace equation and the key procedures for calibration of the instrument are analysed and described. [Pg.440]

In some cases standardisation (or closely related scaling) is an essential first step in data analysis. In case study 2, each type of chromatographic measurement is on a different scale. For example, the N values may exceed 10 000, whereas k rarely exceeds 2. If these two types of information were not standardised, PCA will be dominated primarily by changes in N, hence all analysis of case study 2 in this chapter involves preprocessing via standardisation. Standardisation is also useful in areas such as quantitative structure-property relationships, where many different pieces of information are measured on very different scales, such as bond lengths and dipoles. [Pg.215]

Two types of disturbances are used to test the response of the system a step change in toluene recycle flowrate and a step change in the setpoint of the reactor inlet temperature controller. These two variables are the primary manipulators for production rate. In the results presented below we will explore which of the two is better. In addition we will see how several design parameters (FEHE area and heat-exchanger bypassing) impact the load response of the process. [Pg.305]


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See also in sourсe #XX -- [ Pg.538 , Pg.539 ]




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