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Exit peaks

The results to be expected from a typical TAP experiment have been simulated (35) for a simple irreversible adsorption and are shown in Fig. 2. If there is no adsorption, the pulse at the reactor outlet is represented by curv e A. For > 0, some of the inlet pulse (N a moles of A) remains on the catalyst, and the amount is proportional to the difference between the areas under curve A and curve B, for example. Figure 3 shows what happens with reversible adsorption. For fast adsorption and slow desorption, there may be two peaks as shown by curve C. After a sufficient length of time, all the gas that was initially adsorbed will have left in the exit peak. Cleaves et al. (35) also show that for values of k. and kj that are sufficiently high so that the gas and adsorbed phases are everywhere in equilibrium, the response curve has the shape of curv e A but the peak height is reduced to 1.85/(1 + Keq). [Pg.342]

Fritz and Scott (23) derived simple statistical expressions for calculating the mean and variance of chromatographic peaks that are still on a column (called position peaks) and these same peaks as they emerge from the column (called exit peaks). The classical plate theory is derived by use of simple concepts from probability theory and statistics. In this treatment, each sample chemical substance molecule is examined separately, whereas its movement through the colunm is described as a stochastic process. Equations are given for both discrete- and continuous-flow models. They are derived by calculating the mean and variance of a chromatographic peak as a function of the capacity factor k. [Pg.47]

Metastable Peaks. If the mass spectrometer has a field-free region between the exit of the ion source and the entrance to the mass analyzer, metastable peaks m may appear as a weak, diffuse (often humped-shape) peak, usually at a nonintegral mass. The one-step decomposition process takes the general form ... [Pg.814]

Direct-reading polychromators (Figure 3b) have a number of exit slits and photomultiplier tube detectors, which allows one to view emission from many lines simultaneously. More than 40 elements can be determined in less than one minute. The choice of emission lines in the polychromator must be made before the instrument is purchased. The polychromator can be used to monitor transient signals (if the appropriate electronics and software are available) because unlike slew-scan systems it can be set stably to the peak emission wavelength. Background emission cannot be measured simultaneously at a wavelength close to the line for each element of interest. For maximum speed and flexibility both a direct-reading polychromator and a slew-scan monochromator can be used to view emission from the plasma simultaneously. [Pg.641]

If the mobile phase is a liquid, and can be considered incompressible, then the volume of the mobile phase eluted from the column, between the injection and the peak maximum, can be easily obtained from the product of the flow rate and the retention time. For more precise measurements, the volume of eluent can be directly measured volumetrically by means of a burette or other suitable volume measuring vessel that is placed at the end of the column. If the mobile phase is compressible, however, the volume of mobile phase that passes through the column, measured at the exit, will no longer represent the true retention volume, as the volume flow will increase continuously along the column as the pressure falls. This problem was solved by James and Martin [3], who derived a correction factor that allowed the actual retention volume to be calculated from the retention volume measured at the column outlet at atmospheric pressure, and a function of the inlet/outlet pressure ratio. This correction factor can be derived as follows. [Pg.29]

The XRD pattern of the catalyst. Fig. 3. can be understood as thermal treatment lead to the crystallization of the catalyst and mixture of a majority of nanocrystalline MosOu-type oxide with minor amounts of nanocrystalline M0O3 and Mo02-type material [5]. The crystallization of the catalyst takes place only in a small temperature range and above which decomposes. The FTIR pattern. Fig. 4. shows the peak at 711 cm suggests that there exits a multi phase component like Mo (or V or W)-0- Mo bond [6]. [Pg.275]

Figure 2. Relative GC peak areas of exit gases from N,0 pulses over 0.5% RhO /CeOj at 623 K (2A) Complete conversion to N,-only from pulses 1 —10 over prereduced coprecipitated material followed by a switch to Nj plus Oj products for pulses 12 27 ... Figure 2. Relative GC peak areas of exit gases from N,0 pulses over 0.5% RhO /CeOj at 623 K (2A) Complete conversion to N,-only from pulses 1 —10 over prereduced coprecipitated material followed by a switch to Nj plus Oj products for pulses 12 27 ...

See other pages where Exit peaks is mentioned: [Pg.222]    [Pg.222]    [Pg.69]    [Pg.196]    [Pg.384]    [Pg.424]    [Pg.11]    [Pg.17]    [Pg.1548]    [Pg.62]    [Pg.138]    [Pg.641]    [Pg.17]    [Pg.19]    [Pg.306]    [Pg.483]    [Pg.359]    [Pg.126]    [Pg.88]    [Pg.238]    [Pg.277]    [Pg.386]    [Pg.54]    [Pg.275]    [Pg.175]    [Pg.221]    [Pg.337]    [Pg.353]    [Pg.354]    [Pg.135]    [Pg.135]    [Pg.683]    [Pg.129]    [Pg.215]    [Pg.295]    [Pg.560]    [Pg.834]    [Pg.914]    [Pg.524]    [Pg.235]    [Pg.28]    [Pg.88]    [Pg.189]   
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