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Further Considerations

Following the generation of a macrocyclic ring by a template reaction it has often been the practice to modify the ring by further reaction. Examples of such modification are given by the formation of the derivative complexes (71) and (72) discussed in Section 2.3. Other examples are described in subsequent chapters - in particular, ligand redox reactions have been widely used and a range of such reactions is presented in Chapter 8. [Pg.48]

The ligand reaction step may occur either with the template metal still intact or may take place after removal of the metal ion from the ring. As already mentioned, many of the Schiff-base macrocycles are unstable in the absence of a coordinated metal ion. However, for such systems, it has often been possible to hydrogenate the coordinated imine functions directly. The resulting saturated ligands will not be subject to the hydrolytic degradation which occurs for the imine precursors in the absence of their metal ion. [Pg.48]

Typically, the imine linkages can be reduced chemically (for example, using sodium borohydride in methanol), catalytically (for example, using H2 in the presence of a catalyst such as Pd/C) or electrochemically. The reduced ligands can normally be removed from their respective metal ions using one of a number of procedures. [Pg.48]

Generation of free macrocycles from their metal complexes The removal of a macrocycle from its coordinated metal ion is a frequent procedure in macrocyclic ligand synthesis - conditions for inducing such demetallations are now briefly discussed  [Pg.48]

Multidimensional planar chromatographic separations, as we have seen, require not only a multiplicity of separation stages, but also that the integrity of separation achieved in one stage be transferred to the others. The process of separation on a two-dimensional plane is the clearest example of multidimensional separations. The greatest strength of MD-PC, when properly applied, is that compounds are distributed widely over two-dimensional space of high zone (peak) capacity. Another [Pg.193]

On the basis of theory and experimental observations it can be predicted that a zone capacity of ca. 1500 could be achieved by 2-D multiple development. Because the same result can be achieved by application of 2-D forced-flow development on HPTLC plates, it can be stated that the combination of stationary phases, FFPC and D offers a fruitful future in modem, instmmental planar chromatography. [Pg.194]

Femado, T. A. Dean, H. D. Ahmed and J. A. Berndt, Multidimensional and multimodal tliin-layer chromatography pathway to the future , ]. PlanarChromatogr. 2 336-345 (1989). [Pg.194]

Giddings, Two-dimensional separations concept and promise . Anal. Chem. 56 1258A-1270A(1984). [Pg.194]

Giddings, Concepts and comparisons in multidimensional separation , ]. High Resolut. Chromatogr. 10 319-323 (1987). [Pg.194]

For various process reasons, horizontal drums often are furnished with what appears to be a small vertical drum, called a boot, attached to the underside of the vessel. Because the boot is inaccessible to the main drum platforming, special consideration must be [Pg.107]

In certain cases, drums must slope, as shown in Exhibit 5-34. If the nozzles are not perpendicfilar to the horizontal plane, all vertical piping runs from these nozzles must be calculated because they will be offset at an angle. [Pg.107]

Heat exchangers are similar to pumps and vessels in that they are widely used in most process plants. The control of heat within any facility is an important part of plant operation, whether by direct application (e.g., in a furnace) or by heat interchange (e.g., in a shell and tube exchanger). The principal application of a heat exchanger is to maintain a heat balance through the addition or removal of heat by exchange with outside sources or between streams of two different operating temperatures. [Pg.109]

This chapter highlights the general layout requirements for heat exchangers. It also identifies the infor- [Pg.109]

While this metric is very useful, it is obviously not the last word on complexity metrics. [Pg.129]

For future development, similar ideas could be applied not just to the halting complexity, but also to the complexity that variables are derived from. When the value of a variable is determined by multiple loops, or conditions within loops, or other sorts of non-linear mechanisms, the value of variables can be chaotic, even when they are not themselves what determines if the problem halts. Extending these ideas to variable calculation could allow for an even more comprehensive look at where program complexity lies. [Pg.129]

Calculating Software Complexity Using the Halting Problem [Pg.130]

Bartlett, J. (2014). Using Turing oracles in cognitive models of problem-solving. In J. Bartlett, D. Halsmer, M. R. Hall (Eds.), Engineering and the ultimate (pp. 99-122). Broken Arrow, OK Blyth Institute Press. [Pg.130]

Bringsjord, S., Kellett, 0., Shilliday, A., Taylor, J., van Heuveln, B., Yang, Y., Baumes, J., Ross, K. (2006). A new Godelian argument for hypercomputing minds based on the busy beaver problem. Applied Mathematics and Computations, 176(2), 516-530. Available from http //citeseerx.ist.psu.edu/ viewdoc / download doi=10.1.1.91.5786 rep=rep 1 type=p df [Pg.130]


Further consideration of the reaction system reveals that the ammonia feed takes part only in the primary reaction and in neither of the secondary reactions. Consider the rate equation for the primary reaction ... [Pg.50]

This process could be continued and possible sequences identified for further consideration. Some possible sequences would he eliminated, narrowing down the number suggested by Table 5.1. [Pg.134]

From the above discussion, we might expect that endothermic reactions for which the enthalpy change is large cannot take place. However, a further consideration of the equation... [Pg.67]

Moreover, we want the resulting numerical method to remain time-reversible, which precludes the most obvious projection schemes from further consideration. [Pg.283]

A drawback of this approach is that it typically generates enormous and imwieldy synthesis trees which contain a large number of dead-end branches which are not worth further consideration. Furthermore, the chemist is forced to follow a rigid scheme during the planning process, alternating between the application of transforms, the derivation of new precursors, and again the application of further transforms to these precursors. [Pg.577]

Although there are only three principal sources for the analytical signal—potential, current, and charge—a wide variety of experimental designs are possible too many, in fact, to cover adequately in an introductory textbook. The simplest division is between bulk methods, which measure properties of the whole solution, and interfacial methods, in which the signal is a function of phenomena occurring at the interface between an electrode and the solution in contact with the electrode. The measurement of a solution s conductivity, which is proportional to the total concentration of dissolved ions, is one example of a bulk electrochemical method. A determination of pH using a pH electrode is one example of an interfacial electrochemical method. Only interfacial electrochemical methods receive further consideration in this text. [Pg.462]

The basic instrumentation for capillary electrophoresis is shown in Figure 12.41 and includes a power supply for applying the electric field, anode and cathode compartments containing reservoirs of the buffer solution, a sample vial containing the sample, the capillary tube, and a detector. Each part of the instrument receives further consideration in this section. [Pg.601]

Nonemptiness of the set depends on the values of the function (p on T. For further consideration we should note that the following inequality holds in... [Pg.109]

This form of (2.224) is more convenient for further consideration and, moreover, (2.225), (2.226) imply the following equilibrium equations in in the sense of distributions ... [Pg.140]

The desorptive process may be analyzed before boiling. The key assumption is that the vapor and adsorbed phases are ia equiUbrium ia the bulk of the bed. This assumption eliminates iatraparticle resistances from further consideration and is reasonable for rotary kiln appHcations. The two remaining resistances are associated with hydrocarbon diffusion out of the bed and with convection from the bed surface to the bulk gases. The flux of species Fi from the desorbiag bed becomes... [Pg.50]

Because of destmetive nature, catalytic conversion can be eliminated from further consideration if impurities are desired product. [Pg.458]

No single value for a profitability estimate should be accepted without further consideration. An inteUigent consideration of the cumula-tive-cash-flow and cumulative-discounted-cash-flow curves such as those shown in Fig. 9-10, together with experience and good judgment, is the best way of assessing the financial merit of aprojec t. [Pg.815]

Initial comparison of diyers. The diyers so selected should be evaluated approximately from available cost and performance data. From this evaluation, those diyers which appear to be uneconomical or unsuitable from the standpoint of performance should be eliminated from further consideration. [Pg.1186]

The first step in assessing the candidate tollers is to notify the candidates they are being considered for this toll, and determine their interest in further evaluation. Pending mutual interest in further consideration, the companies must establish lines of communication with commercial representatives, technical/manufacturing representatives, and health, safety and environmental (HS E) representatives. There may be one person in a candidate company that funnels the communication from these three groups or several, especially if the HS E function is split. Tollers should recognize these discrete needs and be prepared to respond accurately and efficiently to enhance their merited consideration. [Pg.23]

Further Consideration of Addition Polymerisation 31 the rate equation, where [S] is the concentration of transfer agent SH, is... [Pg.31]

If the oxygen content of the contaminated air is deficient (refer to page 72), breathing apparatus is essential. The degree of protection required is determined by the level of contamination, the hygiene standard for the contaminant(s), the efficiency of any filter or adsorber available, and the efficiency with which the facepiece of the device seals to the user s face (this is reduced by beards, spectacles etc.). The level of comfort and user acceptability are further considerations. [Pg.433]

Site data should be reviewed to identify conditions that may limit or promote the use of certain technologies. Technologies whose use is clearly precluded by site characteristics should be eliminated from further consideration. [Pg.139]

Further considerations include skimmers and weir overflow rates. Skimmers should be provided on all units since even secondary effluents contain some floatable solids and grease. Overflow rates and sludge scraper design should conform to the requirements of other clarification units. [Pg.265]


See other pages where Further Considerations is mentioned: [Pg.78]    [Pg.169]    [Pg.304]    [Pg.8]    [Pg.598]    [Pg.104]    [Pg.433]    [Pg.39]    [Pg.548]    [Pg.511]    [Pg.287]    [Pg.1548]    [Pg.1763]    [Pg.1970]    [Pg.2425]    [Pg.2547]    [Pg.82]    [Pg.344]    [Pg.299]    [Pg.244]    [Pg.24]    [Pg.25]    [Pg.27]    [Pg.29]    [Pg.33]    [Pg.35]    [Pg.37]    [Pg.175]    [Pg.933]    [Pg.92]    [Pg.510]    [Pg.307]    [Pg.139]   


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