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Standard phase system

Since the kW developed by a 3-0 winding is 50% more than by a 2-0 winding for the same value of stator current /, the economics of this principle is employed in an induction motor for general and industrial use. As standard practice, therefore, in a multi-phase system, only 3-0 induction motors are manufactured and employed, except for household appliances and applications, where mostly single-phase motors are ttsed. [Pg.6]

Nominal system voltage Rated max. system voltage One-minute power frequency voltage withstand at a frequency between 45 and 65 Hz for LT and 25 and 100 Hz for HT systems Standard lightning impulse, 1.2/50 fis voltage withstand (phase to ground)... [Pg.955]

Special resins consist of a two-phase system composed of a mix of a highly condensed, and no longer soluble, PF-resin with a standard type PF-resin [63]. Another two-phase resin is composed of a highly condensed PF-resin, still in an aqueous solution, and of a PF dispersion [64]. The purpose of such special resins is the gluing of wet wood, where the danger of overpenetration of the resin into the wood surface exists and would cause a starved glue line. [Pg.1054]

In a special case involving a C-ring aza steroid, it was found that epoxida-tion of a A -20-keto grouping using a two-phase system (t-butyl alcohol-aqueous potassium hydroxide-30 % hydrogen peroxide) was much superior to the standard hydrogen peroxide-aqueous methanolic alkali conditions. [Pg.196]

The material in this section is divided into three parts. The first subsection deals with the general characteristics of chemical substances. The second subsection is concerned with the chemistry of petroleum it contains a brief review of the nature, composition, and chemical constituents of crude oil and natural gases. The final subsection touches upon selected topics in physical chemistry, including ideal gas behavior, the phase rule and its applications, physical properties of pure substances, ideal solution behavior in binary and multicomponent systems, standard heats of reaction, and combustion of fuels. Examples are provided to illustrate fundamental ideas and principles. Nevertheless, the reader is urged to refer to the recommended bibliography [47-52] or other standard textbooks to obtain a clearer understanding of the subject material. Topics not covered here owing to limitations of space may be readily found in appropriate technical literature. [Pg.297]

Two types of redox systems (Fig. 7) are used for batteries [14]. The standard potential (E°) of MnO 2 should be a good representation of the total energy of the oxide. For two-phase systems such as Pb02, Ag20, HgO, etc., the initial potential (E ) and middle potential (Em ) are equal to E°, from which we can calculate AF (-nFE°). For MnOz, a one-phase system, as shown in Fig. 7(A), the E (initial potential) cannot be used as E°. Ko-zawa proposed the middle potential (Em) of the S-shaped curve to be used as the E°... [Pg.118]

However, it must be emphasized that retention data, whether they be corrected retention volumes, capacity ratios or separation ratios, do not provide unambiguous solute identification. Matching retention data between a solute and a standard obtained from two columns employing different phase systems would be more significant. Even... [Pg.43]

The partition coefficient of a substance between several Immiscible solvent pairs can be combined with retention time data to confirm the identity of a substance when a pure standard is available [706]. Devised by Bowman and Beroza, the substance specific partition coefficient ("p-value") was defined as the fractional amount of substance partitioning into the less polar phase of an equal-volume, two-phase system. Only nanogram quantities of sample are required for the measurement and p-values are often sufficiently characteristic to distinguish between closely related substances. [Pg.453]

Use of a Morton flask and an overhead stirrer allows for better mixing of the two-phase system and gives conversion to product faster than does use of a standard round-bottomed flask with an overhead stirrer. [Pg.248]

In equations 7.27 and 7.28 m(BA), m(cot), m(crbl), and m(wr) are the masses of benzoic acid sample, cotton thread fuse, platinum crucible, and platinum fuse wire initially placed inside the bomb, respectively n(02) is the amount of substance of oxygen inside the bomb n(C02) is the amount of substance of carbon dioxide formed in the reaction Am(H20) is the difference between the mass of water initially present inside the calorimeter proper and that of the standard initial calorimetric system and cy (BA), cy(Pt),cy (cot), Cy(02), and Cy(C02)are the heat capacities at constant volume of benzoic acid, platinum, cotton, oxygen, and carbon dioxide, respectively. The terms e (H20) and f(sin) represent the effective heat capacities of the two-phase systems present inside the bomb in the initial state (liquid water+water vapor) and in the final state (final bomb solution + water vapor), respectively. In the case of the combustion of compounds containing the elements C, H, O, and N, at 298.15 K, these terms are given by [44]... [Pg.96]

Figure 3.11 illustrates the effect of varying the flow rate of the mobile phase on the efficiency of the separation process and provides a standard method of determining the optimum flow rate for a specific column and mobile phase system. [Pg.109]

In one of the earliest studies of phase-transfer catalysed reactions, Makosza and his research group generated dichlorocarbene using a catalytic amount of benzyltriethyl-ammonium chloride in an aqueous sodium hydroxiderchloroform two-phase system [2, 3] and it has become the standard method for the phase-transfer catalytic production of dichlorocarbene and related dihalocarbenes. [Pg.303]

A degree of stereoselective control of the course of a reaction, which is absent or different from that prevalent when the reaction is conducted in the absence of quaternary ammonium salts, may be achieved under standard phase-transfer catalysed reaction conditions. The reactions, which are influenced most by the phase-transfer catalyst, are those involving anionic intermediates whose preferred conformations or configurations can be controlled by the cationic species across the interface of the two-phase system. For example, in the base-catalysed Darzens condensation of aromatic aldehydes with a-chloroacetonitriles to produce oxiranes (Section 6.3), the intermediate anion may adopt either of the two conformations, (la) or (lb) which are stabilized by interaction across the interface by the cations (Scheme 12.1) [1-4]. [Pg.515]

Here fif (T) is the Gibbs free energy per mole of an ideal gas at temperature T and standard pressure P°. Thus the condition of equilibrium for a gas phase system subject to a chemical reaction (Equation 4.36), whether at constant T and P or constant T and V, is given by... [Pg.85]

Statistical mechanics enables one to express the chemical potential i, for an ideal gas phase system in terms of the spectroscopic properties of individual gas phase molecules. The reader is referred to standard statistical mechanics texts (e.g. D. A. McQuarrie Statistical Mechanics , reading list) for the development of the relationship between the system Helmholtz free energy, A , and the corresponding canonical partition function Qi... [Pg.86]

Fig. 10.13 Distribution coefficients of several proteins in the dextran-polyethylene glycol system in 0.0005 M KH2PO4, 0.0005 M K2HPO4, and with increasing concentration of NaCl the latter is expressed as moles NaCl added per kilogram standard phase system. [Pg.445]

The standard language used to describe rate phenomena in condensed phases has evolved from Kramers one dimensional model of a particle moving on a one dimensional potential, feeling a random and a related friction force. In Section II, we will review the classical Generalized Langevin Equation (GEE) underlying Kramers model and its application to condensed phase systems. The GLE has an equivalent Hamiltonian representation in terms of a particle which is bilinearly coupled to a harmonic bath. The Hamiltonian representation, also reviewed in Section II is the basis for a quantum representation of rate processes in condensed phases. Eas also been very useful in obtaining solutions to the classical GLE. Variational estimates for the classical reaction rate are described in Section III. [Pg.2]

Solvents can cause enzyme inactivation (decrease the number of active enzyme molecules). The exact mechanisms are not so well known, but it is clear that solvent polarity plays an important role. Several solvent parameters have been used to try to rationalise the influence of solvents on enzymes. The parameter which has been used most for this purpose is the log P value, which is defined as the logarithm of the partition coefficient of a substance in the standard 1-octanol/water two-phase system (Table 9.4). Log P values can be determined experimentally by measuring the partitioning of the solvent between octanol and water. Alternatively, log P values... [Pg.354]

Lactobacillus kefir (ADH E.C. 1.1.1.1) for use in organic solvents [11, 12]. Both biocatalysts are characterized by a very low stability in pure organic solvents or standard aqueous-organic two-phase systems [20], though their broad substrate ranges include many hydrophobic compounds [21, 22]. Figure 3.2.2 illustrates the denaturation of native BAL at the interface between a buffered aqueous solution and octanone. [Pg.430]


See other pages where Standard phase system is mentioned: [Pg.158]    [Pg.240]    [Pg.1476]    [Pg.7]    [Pg.108]    [Pg.251]    [Pg.96]    [Pg.125]    [Pg.257]    [Pg.339]    [Pg.281]    [Pg.106]    [Pg.8]    [Pg.401]    [Pg.276]    [Pg.98]    [Pg.170]    [Pg.65]    [Pg.186]    [Pg.142]    [Pg.422]    [Pg.426]    [Pg.428]    [Pg.429]    [Pg.431]    [Pg.14]    [Pg.196]    [Pg.3]    [Pg.10]    [Pg.79]    [Pg.813]   
See also in sourсe #XX -- [ Pg.119 ]

See also in sourсe #XX -- [ Pg.119 ]




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Standard system

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