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Estimators efficient

Topology Power Switch Type Bipolar MOS Overall Estimated Efficiency (%) Estimated Percent of Total Loss (P(%)) ... [Pg.37]

For the model in Exercise 1, suppose, is normally distributed with mean zero and variance g2(1 + (yx)2). Show that g2 and y2 can be consistently estimated by a regression of the least squares residuals on a constant and x2. Is this estimator efficient ... [Pg.45]

The radiotracer method for estimating efficiency of initiation was applied by Bevington and Eaves (32) to polymerization in benzene and in carbon tetrachloride. Whereas they had calculated that about 47% of the radicals from AIBN initiate polymer chains in DMF solvent, efficiency in benzene was about 50% and in carbon tetrachloride about 30%. This low efficiency in carbon tetrachloride is attributed to attack of radicals from AIBN on the carbon tetrachloride solvent, especially at high concentrations of solvent. Chains initiated by secondary radicals derived in this way from the solvent would not be detected by the tracer method. [Pg.421]

The data in Fig. 5 are a little more scattered, but they involve donors and acceptors of various sizes that are quite distinct electronically [64], Taking into account the uncertainties in the determination of the driving force for BET from (sometimes irreversible) cyclic voltammetry experiments, the data of Figs. 4 and 5 are an excellent starting point for semi-quantitative predictions of BET rates within photoinduced ion pairs, and may be used to estimate efficiencies of follow up reactions, including fragmentation reactions. [Pg.14]

For AM 1.5-insolation. Estimated efficiency depends on type of solar conversion system i.e., whether single- or twin-photosystem and whether one- or two-photon driven. 70, 195... [Pg.179]

For multicomponent systems (i.e., those with more than two components) there are c - 1 independent component efficiencies, and there are sound theoretical reasons as well as experimental evidence for not assuming the individual component efficiencies to be alike indeed, they may take values between plus and minus infinity. Component efficiencies are more likely to differ for strongly nonideal mixtures. While models exist for estimating efficiencies in multicomponent systems [see chapter 13 in Taylor and Krishna, (op. cit.) for a review of the literature], they are not widely used and nave not (yet) been included in any of the more widely used commercial simulation programs. [Pg.43]

From the precision of the data, one would estimate that kA/ki > 15, which is quite reasonable if the excess energy of O2 is translational. One has no way at present of estimating efficiencies of energy transfer of the type vibration-vibration. [Pg.403]

The accompanying chart provides a visual means of obtaining this estimated efficiency. The curves are based on the following equation [i] ... [Pg.18]

Schema-based assessment puts the what and the why of assessment first, and it does so by supplying an integrated picture of memory, learning, and assessment. The schema comprises multiple knowledge components, each made up potentially of many different pieces of information. Any test item for a schema will call for some subset of one or more of these knowledge components. The task of the test developer is to create items to test various subsets and thereby estimate efficiently the completeness of an individual s schema knowledge. Schema-based assessment puts the what and the why of assessment first, and it does so by supplying an integrated picture of memory, learning, and assessment. The schema comprises multiple knowledge components, each made up potentially of many different pieces of information. Any test item for a schema will call for some subset of one or more of these knowledge components. The task of the test developer is to create items to test various subsets and thereby estimate efficiently the completeness of an individual s schema knowledge.
Figure 7. Estimated efficiency of a Hydrogen production process as a function of time spent in... [Pg.265]

Numerical methods used to fit experimental data should, ideally, give parameter estimates that are unbiased with reliable estimates of precision. Therefore, determining the reliability of parameter estimates from simulated PPK studies is an absolute necessity since it may affect study outcome. Not only should bias and precision associated with parameter estimation be determined but also the confidence with which these parameters are estimated should be examined. Confidence interval estimates are a function of bias, standard error of parameter estimates, and the distribution of parameter estimates. Use of an informative design can have a significant impact on increasing precision. Paying attention to these measures of parameter estimation efficiency is critical to a simulation study outcome (6, 7). [Pg.305]

STUDY EXECUTION AND IMPACT ON PARAMETER ESTIMATION EFFICIENCY... [Pg.324]

Column efficiency experimental data are usually compiled and saved and are used for estimating efficiencies of similar columns or for developing empirical correlations for predicting the efficiencies. When attempting to estimate a tray efficiency based on data available for another column, it is important to be aware of the factors that influence tray efficiency the most and take them into consideration. For instance, the tray dimensions should be comparable. Of particular importance are the tray diameter, tray spacing, number of passes, and liquid level on the tray. [Pg.518]

FIGURE 13.16 Chart for estimating efficiency of plate-type absorbers and strippers. [H. E. O Connell, 1946. [Pg.1095]

Show that and can be consistently estimated by a regression of the least squares residuals on a constant and X. Is this estimator efficient ... [Pg.45]

Since this work deals with the aggregated simulation and planning of chemical production processes, the focus is laid upon methods to determine estimations of the process models. For process control this task is the crucial one as the estimations accuracy determines the accuracy of the whole control process. The task to find an accurate process model is often called process identification. To describe the input-output behaviour of (continuously operated) chemical production plants finite impulse response (FIR) models are widely used. These models can be seen as regression models where the historical records of input/control measures determine the output measure. The term "finite" indicates that a finite number of historical records is used to predict the process outputs. Often, chemical processes show a significant time-dynamic behaviour which is typically reflected in auto-correlated and cross-correlated process measures. However, classic regression models do not incorporate auto-correlation explicitly which in turn leads to a loss in estimation efficiency or, even worse, biased estimates. Therefore, time series methods can be applied to incorporate auto-correlation effects. According to the classification shown in Table 2.1 four basic types of FIR models can be distinguished. [Pg.23]

The design of the equipment for the non-reactive sections should not pose too great a challenge since existing methods of estimating efficiencies or HETP that are based on key-components could be used. For the reactive section, however, the estimation of HETPS and efficiencies is more problematic. There is no easy way to identify key components. Chemical reactions influence component efficiencies in an unpredictable manner (Fig. 9.22 in [1]). Of course, like the rest of the RD community, we could behave like ostriches and bury our heads in the sand while assuming equal component efficiencies (say, 70%) for individual species and hope for the best ... [Pg.237]

Table 8.1 Operator s skill level (trained task with estimated efficiency in parenthesis /(e)) for different level of skill inventory... Table 8.1 Operator s skill level (trained task with estimated efficiency in parenthesis /(e)) for different level of skill inventory...
Theoretical conversion efficiencies of photovoltaic systems depend on the semiconductor materials used in the cells and on the ambient tanperatuie. The materials currently used to make photovoltaic cells can be grouped into three broad categories 1) expensive, efficient monocrystalline silicon, 2) less efficient but much lower cost polycrystalline silicon, and 3) the lowest cost and poorest performer, amorphous silicon material. Conversion efficiencies of commercial polycrystaUine silicon cells are 10 to 15 percent. Now the primary development areas are in how to use monocrystalline silicon with solar concentrators and making thin-film cells by depositing a 5- to 20-micron film of silicon onto an inexpensive substrate, because the estimated efficiency of these cells is above 20 percent. Work is ongoing with other materials, including amorphous silicon (a-Si), copper indium diselenide (CuInSe2 or CIS) and related materials, and cadmium telluride (CdTe). [Pg.68]

In spectra taken on a mixture of elements, the detection limits for components can be estimated efficiently using a few rules of thumb. The efficiency of the detector between 100 keV and 10 MeV drops by two orders of magnitude. Similarly, the minimum detectable peak area varies from a few hundreds of counts at low energies to a few counts at the highest energies. These peak areas corrected with the counting efficiency can be approximated as being constant... [Pg.1627]

Hybridization of the SOFC witha GT significantly improves the system efficiency and can be beneficial for use in large (hundreds of KWs and higher) power plants. Table 33.4 compares the estimated performances of three SOFC power systems simple cycle, SOFC/GT hybrid, and SOFG/GT hybrid with anode and cathode gas recycle (AGR and CGR) [7]. The simple cycle system and hybrid systems (based on 800 °C planar SOFCs) operate at 1.3 and 4.6 atm, respectively and the fuel is methane. It can be seen that the hybrid system with gas recycle has an estimated efficiency of about 71%, about 26 points higher than the simple cycle system. [Pg.969]


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