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SCRs

Harris J 1987 Notes on the theory of atom-surface scattering Phys.scr. 36 156... [Pg.916]

III an SCF calculation. many iterations may beneetled to achieve SCr con vergeiice. In each iteration all the two-electron integrals are retrieved to form a Fock matrix. Fast algorith m s to retrieve the two-cicetron s integrals arc important. [Pg.263]

Coordin ates of atom s can he set by n orm al translation orrotation of HyperCh cm molecules, fo set initial velocities, however, it is necessary to edit th e H l. file explicitly. The tin it o f velocity in the HIN file is. An gstrom s/picosecon d.. Areact.hin file and a script react.scr are in eluded with HyperChem to illustrate one simple reacting trajectory. In order to have these initial velocities used in a trajectory the Restart check box of the Molecular Dynamics Option s dialog box must he checked. If it is n ot, the in itial velocities in the HIN file will be ignored and a re-equilibration to the tern peratiire f of th e Molecular Dyn am ics Option s dialog box will occur. This destroys any imposed initial conditions on the molecular dynamics trajectory. [Pg.329]

A sequence alignment establishes the correspondences between the amino adds in th unknown protein and the template protein (or proteins) from wliich it will be built. Th three-dimensional structures of two or more related proteins are conveniently divided int structurally conserved regions (SCRs) and structurally variable regions (SVRs). Ihe structural conserved regions correspond to those stretches of maximum sequence identity or sequenc... [Pg.555]

Backbone generation is the first step in building a three-dimensional model of the protein. First, it is necessary to find structurally conserved regions (SCR) in the backbone. Next, place them in space with an orientation and conformation best matching those of the template. Single amino acid exchanges are assumed not to affect the tertiary structure. This often results in having sections of the model compound that are unconnected. [Pg.188]

SCR (structurally conserved regions) sections of a biopolymer sequence that are identical to that of another sequence, for which there is a known three-dimensional structure... [Pg.368]

In an economic comparison of these three common abatement systems, a 1991 EPA study (58) indicates extended absorption to be the most cost-effective method for NO removal, with selective reduction only matching its performance for small-capacity plants of about 200—250 t/d. Nonselective abatement systems were indicated to be the least cost-effective method of abatement. The results of any comparison depend on the cost of capital versus variable operating costs. A low capital cost for SCR is offset by the ammonia required to remove the NO. Higher tail gas NO... [Pg.43]

Process Licensors. Some of the well-known nitric acid technology licensors are fisted in Table 3. Espindesa, Grande Paroisse, Humphreys and Glasgow, Rhfyne Poulenc, Uhde, and Weatherly are all reported to be licensors of weak acid technology. Most weak acid plant licensors offer extended absorption for NO abatement. Espindesa, Rhfyne Poulenc, Weatherly, and Uhde are also reported (53,57) to offer selective catalytic reduction (SCR) technology. [Pg.45]

A schematic of a SCR system is shown in Figure 7. Systems capable of operating at higher temperatures than those shown in Figure 7b were under development as of 1995. [Pg.9]

Fig. 7. NO reduction using selective catalytic recovery (SCR) (a) basic principles of the SCR process where represent gas particles and (b) effect of... Fig. 7. NO reduction using selective catalytic recovery (SCR) (a) basic principles of the SCR process where represent gas particles and (b) effect of...
Similar to oil-fired plants, either low NO burners, SCR, or SNCR can be appHed for NO control at PC-fired plants. Likewise, fabric filter baghouses or electrostatic precipitators can be used to capture flyash (see Airpollution controlmethods). The collection and removal of significant levels of bottom ash, unbumed matter that drops to the bottom of the furnace, is a unique challenge associated with coal-fired faciUties. Once removed, significant levels of both bottom ash and flyash may require transport for landfilling. Some beneficial reuses of this ash have been identified, such as in the manufacture of Pordand cement. [Pg.10]


See other pages where SCRs is mentioned: [Pg.144]    [Pg.172]    [Pg.172]    [Pg.172]    [Pg.95]    [Pg.157]    [Pg.123]    [Pg.223]    [Pg.237]    [Pg.281]    [Pg.282]    [Pg.349]    [Pg.204]    [Pg.295]    [Pg.391]    [Pg.391]    [Pg.433]    [Pg.567]    [Pg.90]    [Pg.30]    [Pg.30]    [Pg.43]    [Pg.44]    [Pg.206]    [Pg.9]    [Pg.91]    [Pg.338]    [Pg.25]    [Pg.150]    [Pg.276]    [Pg.181]    [Pg.378]    [Pg.135]    [Pg.135]    [Pg.264]    [Pg.530]   
See also in sourсe #XX -- [ Pg.146 ]




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Ammonia Storage and Release in SCR Systems for Mobile Applications

Analysis of the Enhanced SCR Chemistry

Beneficial Modification of HC-SCR DeNOx Catalysts to Improve Hydrothermal Stability

Catalyst for the SCR Process

Combined LNT-SCR Concepts

Control-Oriented SCR Model

DPF + SCR

Deactivation behavior of SCR DeNO

Deactivation behavior of SCR DeNO catalysts

Deactivation of SCR Catalysts

Denox SCR catalyst

Detailed Kinetic Models for SCR Over Cu-Zeolites

Dimensioning of SCR System

Fast-SCR

Furnace Controllers and SCRs

Global Kinetic Models for SCR Over Cu-Zeolites

H-Mordenite Deactivation during the SCR of NOx. Adsorption and

H2-SCR

HC-SCR

HC-SCR DeNOx Catalysts

Higher Temperatures The NO2-SCR Reaction

Hydrogen-Selective Catalytic Reduction (H2-SCR)

Hydrothermal Stability of HC-SCR DeNOx Catalysts

Investigation on the Superior Hydrothermal Stability of Small-Pore Zeolite Supported Cu SCR Catalyst

Kinetic Modeling of Ammonia SCR for Cu-Zeolite Catalysts

Low-temperature SCR

Main SCR Reactions

Mechanism of Fast SCR

Model-Based DPF SCR System Optimization

Modeling of the SCR Reactor

Monolith SCR reactor

Monoliths SCR catalysts

Multifunctional Materials to Combine NH3-SCR and NSR Cycles

NH3-SCR

NH3-SCR processes

NH3-SCR technology

New Opportunity for HC-SCR Technology to Control NOX Emission from Advanced Internal Combustion Engines

Overview of SCR System Mixing Devices

Properties of Vanadia SCR Catalyst

SCR

SCR Applications Past and Future

SCR Catalyst Ammonia Coverage Ratio Estimation

SCR Catalyst Testing

SCR Control

SCR Mechanism

SCR Reaction Kinetics

SCR Sensing and Estimation Systems

SCR System Design

SCR System Mixing Devices Ford Practical Example

SCR Technologies

SCR catalyst

SCR experiments

SCR of NO by propene

SCR process

SCR reactor

SCR-Urea Reactions

SCRs and Triacs

Selective Catalytic Reduction The SCR Process

Selective catalytic reduction (SCR

Shim-pack SCR

Silicon Control Rectifier (SCR)

Standard SCR Process

Standard SCR reaction

Standard-SCR

Steady-state Modeling of the SCR Reactor

Unsteady-state Kinetics of the Standard SCR Reaction

Unsteady-state Models of the Monolith SCR Reactor

Urea SCR

Vanadia-Based Catalysts for Mobile SCR

Water Tolerance of HC-SCR Catalysts

Zeolites SCR catalysts

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