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Filters derivative

A fourth solution is the internal standard method. In this procedure, a sample is counted that is known to have solubility or pointquenching problems (e.g., aqueous samples, insoluble materials embedded in paper or cellulose derivative filters, etc.). A known amount of isotope (labeled) is added to the sample (i.e., to the fluid or dried paper) and the counting process is repeated. Evaluation of the counting efficiency of the added isotope (the internal standard) allows determination of the counting efficiency of the original sample. (NOTE Alternatively, the internal standard method may employ addition of internal standard to one pair of duplicate samples). [Pg.54]

Recently, Kono (72) suggested use of the Gaussian derivative filter,... [Pg.83]

Pyrimidine derivatives. NaN02 added to a soln. of l,2-dihydro-l-methyl-2-thio-4-hydroxy-6-aminopyrimidine in 5%-NaOH, warmed to 40°, acetic acid added slowly with stirring, heated 2 hrs. at 75° and 10 min. at 100°, cooled, the resulting 5-nitroso derivative filtered, and while still wet, added portionwise with stirring to water alternately with portions of Na-hydrosulfite in such a manner that reduction of each charge is effected before introduction of a fresh lot of nitroso derivative 1,2-dihydro-l-methyl-2-thio-4-hydroxy-5,6-diaminopyrimi-... [Pg.94]

It is designed for the control algorithm. Our preferred algorithm is the noninteractive, proportional-on-PV, derivative-on-PV version. The method must also be suited to any DCS-specific features in the algorithm, particularly if these cannot be disabled. For instance the derivative filter term (a) is not adjustable in many DCS and should therefore be taken account of by the tuning technique. [Pg.65]

Figures 3.31 to 3.33 give the recommended tuning for the preferred algorithm (noninter-active, proportional-on-PV, integral-on-Zin, derivative-on-PV and no derivative filtering). It is assumed that the scan interval is small compared to the process dynamics. The mning is designed to minimise ITAE subject to a maximum MV overshoot of 15 % on a self-... Figures 3.31 to 3.33 give the recommended tuning for the preferred algorithm (noninter-active, proportional-on-PV, integral-on-Zin, derivative-on-PV and no derivative filtering). It is assumed that the scan interval is small compared to the process dynamics. The mning is designed to minimise ITAE subject to a maximum MV overshoot of 15 % on a self-...
Fredriksson, M.J., Petersson, R, Axelsson, B.O., Bylund, D. (2009) An automatic peak finding method for LC-MS data using Gaussian second derivative filtering. J. Sep. Sci. 32, 3906-3918. [Pg.146]

Spectral filtering In more complex classification tasks the utilisation of spectral (frequency) filters turned out to be essential. Popular filters are noise filters for de-noising, Savitzky-Golay derivative filters for resolution enhancement and various types of frequency filter in the Fourier space (Fourier self-deconvolution). A common aspect of these filters is that the person conducting the experiment must consider a trade-off between noise and the detectability of spectral fine structures, i.e. between SNR and the resolution. [Pg.207]

Derivative filters The main advantage of derivative spectroscopy lies in the enhancement of the spectral fine structures combined with a reduction of broad baseline effects. Unfortunately, derivative spectroscopy requires a high SNR, which is sometimes hard to achieve, particularly if the IR microspectra are acquired with high spatial resolution. The example of Figure 6.8, panels C and D, demonstrates that the application of a first derivative Savitzky-Golay filter with nine smoothing points to the raw spectral data in combination with vector normalisation dramatically enhances the number of discriminative spectral features. We consider this combination to be the most effective and robust combination of pre-processing routines for classification analysis. ... [Pg.209]

When noise is present in the measured process output, any derivative action should be accompanied by a filter. However, the problem is often that, as the time constant of the derivative filter is increased to cope with the measurement noise, the closed-loop performance degrades, requiring re-tuning of the controller parameters. This problem is illustrated using the IMC-PID rules appUed to Process A with fd = 0.67. Figure 7.7 shows the closed-loop responses to a negative unit step load disturbance with a derivative filter time constant equal to O.lrp. Figure 7.8 shows the closed-loop responses... [Pg.184]

Figure 7.7 PID control with derivative filter time constant of O.Itjj for Process A (solid new rules dashed IMG). Upper diagram control signal lower diagram process output... Figure 7.7 PID control with derivative filter time constant of O.Itjj for Process A (solid new rules dashed IMG). Upper diagram control signal lower diagram process output...
Figure 8.8 Block diagram of the parallel form of PID control (without a derivative filter). Figure 8.8 Block diagram of the parallel form of PID control (without a derivative filter).
The parallel form of the PID control algorithm (without a derivative filter) is given by... [Pg.140]

Historically, it was convenient to construct early analog controllers (both electronic and pneumatic) so that a PI element and a PD element operated in series. The series form of PID control without a derivative filter is shown in Fig. 8.9. In principle, it makes no difference whether the PD element or the PI element comes first. Commercial versions of the series-form controller have a derivative filter that is applied to either the derivative term, as in Eq. 8-12, or to the PD term, as in Eq. 8-15 ... [Pg.140]

The consequences of adding a derivative filter are analyzed in Exercise 14.16. [Pg.140]

What differential equation model represents the parallel PID controller with a derivative filter (Hint Find a common denominator for the transfer function first.)... [Pg.148]

Figure 14,6. Bode plots of ideal parallel PID controller and series PID controller with derivative filter (a = 1)... Figure 14,6. Bode plots of ideal parallel PID controller and series PID controller with derivative filter (a = 1)...
Assume that the two PID controllers are implemented in the parallel form with a derivative filter (a = 0.1) in Table 8.1. Plot the open-loop Bode diagram and determine the gain and phase margins for each controller. [Pg.267]

Determine sensitivity peaks M and Mj for each controller. Compare the closed-loop responses to step changes in the set-point and the disturbance using the parallel form of the PID controller without a derivative filter ... [Pg.588]


See other pages where Filters derivative is mentioned: [Pg.239]    [Pg.60]    [Pg.479]    [Pg.65]    [Pg.199]    [Pg.186]    [Pg.190]    [Pg.190]    [Pg.139]    [Pg.140]    [Pg.140]    [Pg.142]    [Pg.148]    [Pg.259]    [Pg.259]    [Pg.259]    [Pg.259]    [Pg.259]    [Pg.259]    [Pg.262]    [Pg.263]    [Pg.591]    [Pg.133]   
See also in sourсe #XX -- [ Pg.208 , Pg.209 ]




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