Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

AT Values

Table 2.26a Ordinates (V) of the Normal Distribution Curve at Values of z 2.121... Table 2.26a Ordinates (V) of the Normal Distribution Curve at Values of z 2.121...
One strong caution is that the assumption of a constant U is usually inaccurate for boiling appHcations. Simulation is generally needed to fix AT accurately, particularly at AT values below 15°C. [Pg.89]

Because of its value, refrigeration justifies thicker insulation, lower AT values in heat exchange, and generally much more care in engineering (12). [Pg.92]

By buffering the metal ion concentration using a chelant, E can be adjusted to and stabilized at values that give desirable properties to the deposit. Selective buffering can sequester the properties of interfering ions or can be used to regulate the potentials of two or more ions to approximately the same value in order to effect codeposition. [Pg.392]

The chronoamperometric technique illustrates the principle that analytically useful current responses depend critically on the efficiency of analyte mass transport within the solution. The analyte mass transport in turn depends on the efficiency with which an appHed voltage can maintain the surface concentrations of oxidized and reduced species at values specified by the Nemst equation. It is generally the case in chronoamperometry that the bulk concentration of one of the species is zero whereas the surface concentration of the other species is forced to zero by the appHed potential, but this is not always so. [Pg.52]

If Vo is the volume at 0 , then at the expansion formula is Vj = Vo(l + OCf + + yf"). The table gives values of (X, (3, and y, and of C, the true coefficient of cubical expansion at 20 for some liquids and solutions. The temperature range of the observation is At. Values for the coefficient of cubical expansion of hquids can be derived from the tables of speciBc volumes of the saturated hquid given as a function of temperature later in this section. [Pg.175]

X = distance from tube entrance. Good agreement with experiment at values... [Pg.608]

The major variable in setting entrainment (E, weight of liquid entrained per weight of vapor) is vapor velocity. As velocity is increased, the dependence of E on velocity steepens. In the lowest velocity regime, E is proportional to velocity. At values of E of about 0.001 (around 10 percent of flood), there is a shift to a region where the dependence is with (velocity) ". Near flood, the dependence rises to approximately (velocity). In this regime, the kinetic energy of the vapor dominates, and the bulk of the dispersion on the plate is often in the form of a coarse spray. [Pg.1413]

A very important feature of solid-state technology is energy conservation in the process of speed control. The slip losses that appear in the rotor circuit are now totally eliminated. With the application of this technology, we can change the characteristics of the motor so that the voltage and frequency are set at values just sufficient to meet the speed and power requirements of the load. The power drawn from the mains is completely utilized in doing useful work rather than appearing as stator losses, rotor slip losses or external resistance losses of the rotor circuit. [Pg.134]

The evaluation of At/ values together with off potentials are aids in deciding whether coating damage should be repaired. In addition, by comparison with previous results, intensive measurements indicate whether new coating defects have arisen. These could be the result of external foreign forces on the pipeline. [Pg.134]

A further objective is the evaluation in group (c) of the local polarization state by taking account of IR errors due to direct currents. Here Eq. (3-28) and the further explanations in the second half of Section 3.3.1 are relevant. In practical application, the error effect of A /<,ff must be estimated [2]. When foreign fields are present, it is necessary to substitute for the At/ value the average of the measurements made on both sides of the pipeline [2,52]. Figure 3-30 gives an example of... [Pg.134]

ISO viscosity number. Table 12.1 compares typical correlations between number and weight average molecular weights with ISO numbers, AT-values and ASTM viscosity measurements. [Pg.321]

The basic assumptions of fracture mechanics are (1) that the material behaves as a linear elastic isotropic continuum and (2) the crack tip inelastic zone size is small with respect to all other dimensions. Here we will consider the limitations of using the term K = YOpos Ttato describe the mechanical driving force for crack extension of small cracks at values of stress that are high with respect to the elastic limit. [Pg.494]

Simple asphyxiant. Some gases and vapours present at high concentrations act as asphyxiants by reducing the oxygen content of air. Many of these are odourless and colourless. Many also pose a fire or explosion risk, often at values below which asphyxiation can occur. (Although capable of asphyxiation, they are not considered to be substances hazardous to health under COSHH.)... [Pg.176]

Equations 10-1 through 10-14 only hold for laminar flow. At values of Reynolds number above a eomplieated situation emerges... [Pg.792]

If an isotropic material is subjected to multi-axial stresses then the situation is slightly more complex but there are well established procedures for predicting failure. If a,i and Oy are applied it is not simply a question of ensuring that neither of these exceed ar- At values of and Oy below oj there can be a plane within the material where the stress reaches ot and this will initiate failure. [Pg.232]

Multidimensional (or eoupled) eolumn ehromatography is a teehnique in whieh frae-tions from a separation system are seleetively transferred to one or more seeondary separating systems to inerease resolution and sensitivity, and/or to reduee analysis time. The applieation of seeondary eolumns is illustrated sehematieally in Figure 8.1. The smaller the At, value applied, then the greater is the resolution and number of runs needed to eheek a eertain portion of the sample (5). [Pg.172]

The MW at values above a critical MW has the following relationship with melt viscosity (tj) ... [Pg.277]

The glass stability of the Pd-Ni-P system is wider than that of the Pd-Cu-P system. For most bulk Pd-Ni-P glasses (10-mm diameter), AT> 90 K. The AT values of bulk amorphous Pd-Cu-P alloys are considerably smaller, ranging from 27 to 73 K. [Pg.298]

Using Figure 3-56 or 3-57 enter GPM at value corresponding to peak efficiency, 1.0 Qnws and follow up to the corresponding head value, Hw, then move to the viscosity value of the liquid, and up to the correction factors Cg, Cq, Cj. ... [Pg.206]

Estimate stripping and rectifying pinch temperatures at values one-third and two-thirds of the interval between the column bottoms and overhead, respectively. [Pg.74]

Reading the abscissa of Figure 9-21C at value 0.0756 for ordinate at flooding line for dumped packing ... [Pg.314]

Often, a reasonable and convenient way to understand the heat transfer process in a heat exchanger unit is to break down the types of heat transfer that must occur such as, vapor subcooling to dew point, condensation, and liquid subcooling. Each of these demands heat transfer of a different type, using different AT values, film coefficients, and fouling factors. This is illustrated in Figure 10-36. It is possible to properly determine a weighted overall temperature... [Pg.58]

Subscripts 1,2, and 3 = segments of heat exchanger corresponding to the Qand AT values. [Pg.72]

Figure 10-101. Maximum AT values occur at the indicated threshold of film boiling, a typical example using 100% ethyl alcohol from a clean surface. (Used by permission Cichelli, M. T. and Bonilla, C. F. Transactions. AlChE, V. 41, No. 6, 1945. American Institute of Chemical Engineers. All rights reserved.)... Figure 10-101. Maximum AT values occur at the indicated threshold of film boiling, a typical example using 100% ethyl alcohol from a clean surface. (Used by permission Cichelli, M. T. and Bonilla, C. F. Transactions. AlChE, V. 41, No. 6, 1945. American Institute of Chemical Engineers. All rights reserved.)...

See other pages where AT Values is mentioned: [Pg.56]    [Pg.628]    [Pg.634]    [Pg.657]    [Pg.1117]    [Pg.12]    [Pg.50]    [Pg.55]    [Pg.89]    [Pg.446]    [Pg.509]    [Pg.152]    [Pg.1434]    [Pg.1471]    [Pg.2009]    [Pg.320]    [Pg.571]    [Pg.49]    [Pg.371]    [Pg.491]    [Pg.185]    [Pg.171]    [Pg.356]    [Pg.166]    [Pg.207]   
See also in sourсe #XX -- [ Pg.515 , Pg.516 ]




SEARCH



Adsorption at interfaces values

At various pH values

Buffer Solutions Giving Round Values of pH at

Business Value from Sustainable Development at shell

Conditional value-at-risk

Epsilon values for individual rocks at the present day

Estimations based on experimental values of equilibrium constants at different ionic strength

GCM Values for VM at 20 and

Heat capacity values of Se4(g) at

Heat capacity values of Se5(g) at

Heat capacity values of Se6(g) at

Ions at various pH values

Limit Values at the Workplace

Limiting Values for Thermal Properties at Zero Kelvin

Response time as a function of the thermal driving force for an idealized heat exchanger at different hold-up values

Standard Thermodynamic Values for Selected Substances at

Value at Stake Environmental and Social Issues in the Chemical Industry

Value-at-Risk (VaR) Models

Value-at-risk

© 2024 chempedia.info