Big Chemical Encyclopedia

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

Articles Figures Tables About

Simulated five section

This book aims is to treat the most important conceptual aspects of Process Design and Simulation in a unified frame of principles, techniques and tools. Accordingly, the material is organised in five sections. Process Simulation, Thermodynamic Methods, Process Synthesis, Process Integration, Design Project, and covered in 17 Chapters. Numerous examples illustrate both theoretical concepts and design issues. The work refers also to the newest scientific developments in the field of Computer Aided Process Engineering. [Pg.704]

This chapter consists of five sections. Section 7.2 presents the development of the PID controller tuning rules for first order plus delay processes. Sections 7.3 and 7.4 illustrate the new tuning rules using simulation and experimental studies, respectively, and compares the results with those obtained using the IMC-PID tuning rules. Section 7.5 presents the development of the PID tuning rules for integrating plus delay processes. [Pg.171]

In order to probe cation occupation in the active site in the absence of Mg2+ ions, we examined Na+ distributions in the reactant and activated precursor (deprotonated 20H nucleophile) states. It has been noted in the recent literature that the modeling of ions in highly charged systems such as HHR affords tremendous challenges with regard to simulation time scales [129], This section presents the results of series of five 300 ns simulations of the full length HHR, in both the reactant and activated precursor states, in order to ascertain the cation occupation requirement of the active site to maintain catalytic integrity. [Pg.397]

An interesting combined use of discrete molecular and continuum techniques was demonstrated by Floris et al.181,182 They used the PCM to develop effective pair potentials and then applied these to molecular dynamics simulations of metal ion hydration. Another approach to such systems is to do an ab initio cluster calculation for the first hydration shell, which would typically involve four to eight water molecules, and then to depict the remainder of the solvent as a continuum. This was done by Sanchez Marcos et al. for a group of five cations 183 the continuum model was that developed by Rivail, Rinaldi et al.14,108-112 (Section III.2.ii). Their results are compared in Table 14 with those of Floris et al.,139 who used a similar procedure but PCM-based. In... [Pg.68]

There has been recent widespread interest in simulating semiconductors. This has been especially true for silicon, and to a lesser extent for germanium. Prior to 1984, no general potential energy expressions were available which could be used to model the chemical dynamics of semiconductors. Between 1984 and 1986, at least five different expressions were introduced which can successfully model condensed phases of silicon . These potential energy schemes, which were discussed in section 1.2, have made possible the use of molecular dynamics to study atomic-scale motion on semiconductor surfaces. [Pg.316]

The performance metrics of interest are the key storage cost (both at the member side and at the GCKS side) and rekey communication cost. We repeat each simulation with different seed five times and take the average. The key storage cost is measured as the key storage described in the previous section. More specifically, we assume to use 3DES for encryption and each label has 128-bits of storage. [Pg.16]

Fig. 10.50 Location of the pressure gauge (P) and the thermocouples (7) at the five axial barrel positions. The three cross sections A-A, B-B and C-C are used for contour plots of the numerical results. [Reprinted by permission from T. Ishikawa, S. Kihara, K. Funatsu, T. Amaiwa, and K. Yano, Numerical Simulation and Experimental Verification of Nonisothermal Flow in Counterrotating Nonintermeshing Continuous Mixers, Polym. Eng. Sci., 40, 365 (2000).]... Fig. 10.50 Location of the pressure gauge (P) and the thermocouples (7) at the five axial barrel positions. The three cross sections A-A, B-B and C-C are used for contour plots of the numerical results. [Reprinted by permission from T. Ishikawa, S. Kihara, K. Funatsu, T. Amaiwa, and K. Yano, Numerical Simulation and Experimental Verification of Nonisothermal Flow in Counterrotating Nonintermeshing Continuous Mixers, Polym. Eng. Sci., 40, 365 (2000).]...
The As calculations (Equation (3.95)) were based on the Poisson equation, solved for a five-zone model (Section 3.5.4, Inhomogeneous Media) in which the solute (zone 1) was surrounded by four dielectric zones (2-5). A simplified schematic picture is given in Figure 3.26, but in the actual calculations, the zone boundaries were based on structures obtained from classical molecular dynamics (MD) simulations (with inclusion of a few thousand TIP3P water molecules and Na+ counterions to neutralize the negative charge from the DNA). Each zone was assigned optical and static dielectric constants (sxk and e0k, k = 1, 5). For the solute (zone 1), = e0k = 1.0 was adopted. For zones 2,3,... [Pg.405]

Figure 4.15 Hebeloma danicum (arrowhead) and H. mdicosoides (the rest) fruiting on buried uric acid, which simulates their growth on abandoned nests of wasps underground (see Section 3.4). Twenty-five g of uric acid was buried together with humus (arrow) at the bottom (20 x 20 cm) of a 20 cm deep hole on December 8, 1984, in a Pinus-Quercus forest, Shiga, Japan photograph taken on October 17, 1985. Figure 4.15 Hebeloma danicum (arrowhead) and H. mdicosoides (the rest) fruiting on buried uric acid, which simulates their growth on abandoned nests of wasps underground (see Section 3.4). Twenty-five g of uric acid was buried together with humus (arrow) at the bottom (20 x 20 cm) of a 20 cm deep hole on December 8, 1984, in a Pinus-Quercus forest, Shiga, Japan photograph taken on October 17, 1985.
Figure 3 shows the flowsheet of Figure 2 expressed in terms of the five modules. Lower case letters are used to distinguish modules from plant sections which are denoted by capitals. Some modules are identical with equipment units, e.g. filters and thickeners are distribution modules. In other cases, one piece of equipment is simulated by two or more modules. For example, absorber A is represented by a, c, d and b modules. [Pg.328]

In this section we will present results33 from the MD simulations along the IRC performed for five model reactions the HCN CNH isomerization reaction, the conrotatory ring opening of cyclobutene, ethylene-butadiene cycloaddition, the prototype SN2 reaction Cl +CII3CI C1CH3- -Cr, and the chloropropene isomerization Cl - CH2 - CH=CH2 - CH2=CH - CH2C1. [Pg.241]

A second example of the utility of galvanostatic testing is from an investigation of surface treatments and alloying on the dealloying of aluminum bronzes. Kelly and Scully (56) used a 150 pA/cm2 applied anodic current density for 7 days in simulated ocean water followed by cross-sectional metallography to differentiate the susceptibilities of five aluminum- and nickel-aluminum-... [Pg.114]

Because the Pt3 triangle of the triplatinum cluster is an isosceles triangle— that is, two kinds of Pt exist in the cluster core— the cluster shows a comphcated Pt NMR spectrum similar to that of the uns3un-metric Pt4 cluster (Section II,D). The spectrum consists of a summation of the spectra of five isotopomers (A, A2, B, AB, and A2B) and involves two main singlets with an intensity ratio of 3 1 and an AB pattern in addition to weak signals. Figure 33 shows the observed and simulated... [Pg.244]

The space/time over which the problem is formulated is covered with a mesh of points, often referred to as nodes . At each point, the derivatives in the material balance equation are approximated as differences of the concentrations at the given and surrounding points. This leads to a set of linear equations (based on a five-point stencil in two dimensions - each node is related to its four nearest neighbours) which can be solved to give the solution to the PDE. The methods are well suited to simulations in rectangular regions, which is often compatible with an electrochemical cell. These are by far the most popular methods for electrochemical simulations and will therefore be the focus of the remainder of this section. [Pg.86]

In this array form, these equations can easily be solved on a computer. But, for many cases, the number of sieves used in analysis is relatively small, often less than five, making manual manipulation also possible. In addition, the coefficients of the T J(f) T matrix can be determined for a mill if the input and output size distribution on a mass basis is known [21], In addition to its usefulness in batch mill simulation, this equation plays a role in the description of continuous grinding as we will see in the next section. [Pg.111]


See other pages where Simulated five section is mentioned: [Pg.124]    [Pg.3]    [Pg.4]    [Pg.467]    [Pg.314]    [Pg.841]    [Pg.398]    [Pg.256]    [Pg.80]    [Pg.393]    [Pg.272]    [Pg.103]    [Pg.401]    [Pg.285]    [Pg.714]    [Pg.642]    [Pg.1097]    [Pg.295]    [Pg.69]    [Pg.78]    [Pg.168]    [Pg.210]    [Pg.63]    [Pg.122]    [Pg.192]    [Pg.66]    [Pg.393]    [Pg.232]    [Pg.272]    [Pg.580]    [Pg.285]    [Pg.20]    [Pg.27]   
See also in sourсe #XX -- [ Pg.196 ]




SEARCH



© 2024 chempedia.info