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Flexibility of scale

PNA assembly with t-Boc synthesis chemistry may be employed by either manual or automated methods (Fig. 4). Manual synthesis based on the r-Boc chemistry yields PNA of very high quality but is labor intensive and requires a chemist trained in t-Boc SPPS. Manual synthesis has the advantage of being easily monitored at each monomer inclusion and also allows great flexibility of scale. [Pg.552]

In the discovery phase, a reaction route is developed to allow synthesis of a maximum number of analogues for pharmacological testing. Since the focus is on synthetic flexibility, issues of scale are not central. Once a lead compound exhibits a useful pharmacological activity and is identified as a candidate for further development, larger scale synthesis is required to evaluate stability, bioavailability, toxicity, physicochemical properties, and other compound properties. The Chemical Development Department is usually involved in the preparation of supplies for these activities. [Pg.173]

In continuous processes the reactants are fed to the reactor and the products withdrawn continuously the reactor operates under steady-state conditions. Continuous production will normally give lower production costs than batch production, but lacks the flexibility of batch production. Continuous reactors will usually be selected for large-scale production. Processes that do not fit the definition of batch or continuous are often referred to as... [Pg.483]

Development of automated batch process control systems has lagged behind that of continuous process control. Flexible factory scale commercial systems have only begun to appear in the last five years (1-4). Increases in the performance/price ratio of small computers are now making automation of laboratory scale batch processes more practical. [Pg.179]

The simplified scaling relationships, Eq. (53), offer some flexibility in the model design since fewer parameters must be matched than with the full set of scaling relationships. When the fluidizing gas, the pressure and temperature of the scale model are chosen, the gas density and viscosity for the scale model are set. The model must still be geometrically similar to the commercial bed. There is still one free parameter. Generally this will be the linear scale of the model. For the simplified scaling relationships, the gas-to-solid density ratio must be maintained constant... [Pg.61]

It has been found repeatedly [1, 43, 45] that scalar relativistic contributions are overestimated by about 20 - 25 % in absolute value at the SCF level. Hence inclusion of electron correlation is essential we found the ACPF method (which is both variational and approximately size extensive) to be an excellent compromise between quality and cost. It is reasonable to suppose that for a property that becomes more important as one approaches the nucleus, one wants maximum flexibility of the wavefunction near the nucleus as well as correlation of all electrons thus we finally opted for ACPF/MTsmall as our approach of choice. Typically the cost of the scalar relativistic step is a fairly small fraction of that of the core correlation step, since only n2N4 scaling is involved in the ACPF calculations. [Pg.42]

Abstract Layered double hydroxides (LDHs) comprise au extensive class of materials that are very easy to synthesize in the laboratory, albeit not always as pure phases. In this chapter, we review the wide variety of methods that are available for the synthesis of LDHs and focus on the way in which the physicochemical properties of the materials (such as phase piuity, crystallinity and surface area) vary with synthesis method. The flexibility of the different methods is also discussed some methods can be used to synthesize LDHs containing a wide range of constituent cations and anions, whilst others are more limited in scope. In some cases, the potential for scale-up of a method to produce larger quantities of material is also noted. [Pg.89]

Fuel flexibility. Sub-scale tests at 1 MPa proved the viability of RCL technology to natural gas, landfill gas (70% CH4, 30% CO2), refinery gas (70% CH4, 30%H2), pre-vaporized diesel No. 2 and gasoline or blast furnace gas with a low heating... [Pg.371]


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See also in sourсe #XX -- [ Pg.8 , Pg.232 ]




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