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Intermediate Samples

The obvious questiou now arises What is the impact of the precursor heteroatoms on the end-product at HTT 2800 C The auswer should be obvious from the preceding discussion production of intermediates (i.e., partiaUy graphitized carbons, occurring between the nongraphitized carbons, such as saccharose-based ones, inunature kerogens, and low-rank coals) with P, = 0, or 0.1 and the highly graphitized materials with Pj 0.75. [Pg.65]

FIGURE 1.47 Correlations between x-ray diffraction parameters (a) versus P, (measured from 004) (b) versus 4oo2l 002 versus Pj. (Adapted from N. Iwashita. Intercalation reactions into graphite followed by potential and their application to battery. PhD thesis Hokkaido University, Japan, (1992). N. Iwashita and M. Inagaki. Relations between structural parameters obtained by X-ray powder diffraction of various carbon materials. Carbon 31, 1107-1113 (1993). With permission.) [Pg.65]

Crystallographic Data (t/002 and P ) for Vapor-Grown Carbon Fibers and Mesophase Pitch-Based Carbon Fibers [Pg.67]

VGCF-NVCF ( Q doo2 ( ) MPCF Sample ( C) rfoor (A)  [Pg.67]


Fig. 24. A thin layer chromatography (TLC) image, documenting detection of impurities in a series of dye intermediate samples under near-UV illuinination. Columns 1 and 7 represent reference materials. Photographed with Polaroid Type 339 film in a CU-5 closeup camera. Fig. 24. A thin layer chromatography (TLC) image, documenting detection of impurities in a series of dye intermediate samples under near-UV illuinination. Columns 1 and 7 represent reference materials. Photographed with Polaroid Type 339 film in a CU-5 closeup camera.
For the analysis of nonvolatile compounds, on-line coupled microcolumn SEC-PyGC has been described [979]. Alternatively, on-line p,SEC coupled to a conventional-size LC system can be used for separation and quantitative determination of compounds, in which volatility may not allow analysis via capillary GC [976]. An automated SEC-gradient HPLC flow system for polymer analysis has been developed [980]. The high sample loading capacity available in SEC makes it an attractive technique for intermediate sample cleanup [981] prior to a more sensitive RPLC technique. Hence, this intermediate step is especially interesting for experimental purposes whenever polymer matrix interference cannot be separated from the peak of interest. Coupling of SEC to RPLC is expected to benefit from the miniaturised approach in the first dimension (no broadening). Development of the first separation step in SEC-HPLC is usually quite short, unless problems are encountered with sample/column compatibility. [Pg.556]

Robotic systems in a small analytical laboratory have the greatest application in the intermediate sample manipulation steps. The removal of excess solvent with the Zymark evaporator [492], for example, can be closely controlled, fully automated, and operate in parallel (up to six samples per instrument). This technique has considerable advantages over rotary evaporation, which is prone to loose volatile organic compounds (e.g., chlorobenzenes) under vacuum and rapid vaporization. Automated repetitive manipulations are well served by a robotic system [492]. [Pg.69]

In summary, the study of the basalt dykes shows that the REE of the primary basalt have been mobilized during basalt alteration, most probably by dissolution of primary apatite. This mobilization was strongest in the intermediate samples R 3958 and R 3960 (Fig. 1) and the mobilized REE were subsequently immobilized by precipitation of secondary apatite. [Pg.137]

Afterwards, the percentage calculated in equation (1) has been used together with the REE patterns of the two end members to calculate a hypothetical REE mixing pattern for each of the three intermediate samples according to equation (2) ... [Pg.139]

The hypothetical REE mixing patterns calculated for the three intermediate samples are shown as dashed lines in Fig. 7. They are almost flat and show no similarities with the observed patterns. We therefore conclude that the observed evolution of the REE distributions cannot be attributed to mixing, but must be due to a fractionation process. [Pg.139]

For intermediate sample loads, the sigmoidal calibration curve may be substituted by a linear function, but this statement can surely not be generalized. Balazs et al. assume the ELSD... [Pg.272]

Variation diagrams of major and trace elements vs. SiC>2 (Fig. 8.13) show a bimodal distribution between basalts and rhyolites, with a gap for intermediate compositions (Daly gap). Such a distribution of rock types is typical of volcanoes from continental rift settings (see Peccerillo et al. 2003 and references therein). A few intermediate samples have been found as xenoliths, and these have been suggested to represent hybrids between mafic and felsic magmas (e.g. Mahood and Baker 1986). [Pg.234]

From the above results we can propose the following mechanism for hexagonal MCM-41 synthesis. At low crystallization temperature or short crystallization time a fibrous agglomerate structure is often observed by SEM on intermediate samples. The 100 and 200 reflections are not detected by XRD and the value of the specific surface area is low. This reflects the initial step of synthesis which is generally referred to the nucleation step in zeolite synthesis. After this step, the 100 and 200 reflections are present on the XRD diffraction pattern. The value of the specific surface area is between 700 and 900 m /g. The fibrous agglomerate structure disappears and crystals of MCM-41 appear. This corresponds to the crystallization step. Finally if both the synthesis temperature and time are continuously raised, a triphasic mixture MCM-41, MCM-50 and amorphous phase is identified by XRD. The... [Pg.275]

Any measurement on a real-world sample is always a combination of the free and bound gas sample types. This is because the process of taking the gas sample generally requires that the sediment or rock system is disturbed by some mechanical means which creates the mixing of these sample types. Because of this unavoidable interaction, we have recognised the need to consider an intermediate sample-collection technique that measures the more loosely-bound gases liberated into a container containing the core sample. [Pg.151]

The choice of sample size or bed size in preparative separations deserves as much attention as any other separation variable. Too large a sample for a bed of given size may lead to incomplete separation [e.g.. Fig. 4-1 (d)]. Too small a sample (or rather, too large a bed) frequently means a separation which requires more time, effort, and materials than is necessary. The optimum sample size in preparative separations (at least for sample sizes above 0.1 g) corresponds to the minimum adsorbent/sample ratio which yields adequate separation it is a complex function of separation conditions and of sample type. Samples of less than 0.1 g are commonly separated by thin-layer chromatography, while samples weighing more than 1 g are usually separated on columns. Loose-layer chromatography has been recommended for intermediate sample sizes (JO). As much as 100 g of sample have been separated by means of thin-layer chromatography (i/), but moderately difficult separations by this technique are normally limited to sample sizes of less than 1 g. [Pg.51]

An excipient manufacturer should be able to identify critical or key points in the process where selective intermediate sampling and testing is necessary in order to monitor process performance. As the end of the process approaches, the completeness of the records should increase. [Pg.94]

Regarding details of available analytical solutions for two and more components we refer the reader to the cited references by Helfferich et al, Rhee et al, and Guio-chon et al. Here, a recently derived analytical solution for the prediction of the elution bands of two components in case of Langmuir isotherms and intermediate sample sizes should be mentioned. These explicit equations, which extend the status described by Guiochon et al. (2006), were used for efficient optimization of batch chromatography (Siitonen and Sainio, 2011). [Pg.334]

Robotic systems in a small analytical laboratory have the greatest application to the intermediate sample manipulation steps. The removal of excess sol-... [Pg.344]

TG, DTA and DSC curves of the cadmium peroxotitanate complex Cd2[Ti2(02)20(0H)6] H20 were recorded and used to determine the isothermal conditions suitable for obtaining the intermediate samples corresponding to the phases observed during the thermal decomposition. The experimental results were used to propose a mechanism of thermal decomposition of the investigated compound to CdTiOa. The aim of this study has been to determine the optimum conditions for obtaining CdTiOa with well-defined crystallinity [133],... [Pg.470]

Methods based on electron detection have intermediate sampling depths. The sampled thickness in techniques such as AES and XPS is of the order of 50 A. Since the escape depth of an electron is dependent on its energy, the sampling depth in XPS and... [Pg.381]

Figure 1 Schematic diagram of a multidimensional chromatography system. The two systems correspond to the methods employed, e.g., the GC or LC system. The separation channel may be an elution column or separation plane. Between the two systems is the process for transferring solute from the first to second dimensions. It may be a heart-cut process (GC-GC), a fraction collection step (LC-GC), a modulation process (GC X GC), or a plate positional change for planar TLC. Some systems will allow or require a detection step between the two systems, such as a monitor detector in MDGC. In the figure, step 1 refers to the sample application/injeclion step 2 to the interface or intermediate sample-processing device and step 3 to the elution of the separated sample into a detection system. Figure 1 Schematic diagram of a multidimensional chromatography system. The two systems correspond to the methods employed, e.g., the GC or LC system. The separation channel may be an elution column or separation plane. Between the two systems is the process for transferring solute from the first to second dimensions. It may be a heart-cut process (GC-GC), a fraction collection step (LC-GC), a modulation process (GC X GC), or a plate positional change for planar TLC. Some systems will allow or require a detection step between the two systems, such as a monitor detector in MDGC. In the figure, step 1 refers to the sample application/injeclion step 2 to the interface or intermediate sample-processing device and step 3 to the elution of the separated sample into a detection system.
The batch recycle differential reactor is used to obtain adsorption rate data to evaluate various kinetic models for cadmium ion adsorption on Sol-AD-lV. Approximately 0.25 g of the solid extractant is placed between glass beads inserted in a glass tube of 1.0 cm internal diameter. Solutions of various cadmium ion concentrations (25 to 300 mg/1) are contacted in a batch mode over 720 minutes, with intermediate sample taken for atomic absorption spectroscopic measurements of the cadmium ions. The external mass transfer resistances are minimized by operating at 16 ml/min. Results of the experiments are shown in Figure 7.23. [Pg.251]

The concentration of the standard should be just above the expected maximum sample concentration. If intermediate sample concentrations are expected, calibration between a low and high standard may be preferable. The calibration has to be repeated at regular intervals of from one to several hours depending on the overall performance of the analytical system. [Pg.223]

The sample stability in row A is that reported by Greaves et al. [5], although this is significantly lower than those reported for aerodynamic levitation [2] and combined aerodynamic and electrostatic [9] levitation shown in row B. Row C is an intermediate sample stabdity which stiU causes a significant error in the transmission... [Pg.74]


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