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Rate dependence

The convergence rate depends somewhat on the problem and on the initial estimates used. For mixtures that are not extremely wide-boiling, convergence is usually accomplished in three or four iterations,t even in the presence of relatively strong liquid-phase nonidealities. For example, cases 1 through 4 in Table 1 are typical of relatively close-boiling mixtures the latter three exhibit significant liquid-phase nonidealities. [Pg.122]

Keywords compressibility, primary-, secondary- and enhanced oil-recovery, drive mechanisms (solution gas-, gas cap-, water-drive), secondary gas cap, first production date, build-up period, plateau period, production decline, water cut, Darcy s law, recovery factor, sweep efficiency, by-passing of oil, residual oil, relative permeability, production forecasts, offtake rate, coning, cusping, horizontal wells, reservoir simulation, material balance, rate dependent processes, pre-drilling. [Pg.183]

The number and shape of the grid blocks in the model depend upon the objectives of the simulation. A 100 grid block model may be sufficient to confirm rate dependent processes described in the previous section, but a full field simulation to be used to optimise well locations and perforation intervals for a large field may contain up to 100,000 grid blocks. The larger the model, the more time consuming to build, and slower to run on the computer. [Pg.205]

As a guideline, the plateau rate is usually between 2 to 5% of the STOMP per year. The lower end of the range would apply to shallow dip reservoirs with an unfavourable mobility ratio, creating a rate dependent displacement process. [Pg.209]

Neumann has adapted the pendant drop experiment (see Section II-7) to measure the surface pressure of insoluble monolayers [70]. By varying the droplet volume with a motor-driven syringe, they measure the surface pressure as a function of area in both expansion and compression. In tests with octadecanol monolayers, they found excellent agreement between axisymmetric drop shape analysis and a conventional film balance. Unlike the Wilhelmy plate and film balance, the pendant drop experiment can be readily adapted to studies in a pressure cell [70]. In studies of the rate dependence of the molecular area at collapse, Neumann and co-workers found more consistent and reproducible results with the actual area at collapse rather than that determined by conventional extrapolation to zero surface pressure [71]. The collapse pressure and shape of the pressure-area isotherm change with the compression rate [72]. [Pg.114]

Theoretical models of the film viscosity lead to values about 10 times smaller than those often observed [113, 114]. It may be that the experimental phenomenology is not that supposed in derivations such as those of Eqs. rV-20 and IV-22. Alternatively, it may be that virtually all of the measured surface viscosity is developed in the substrate through its interactions with the film (note Fig. IV-3). Recent hydrodynamic calculations of shape transitions in lipid domains by Stone and McConnell indicate that the transition rate depends only on the subphase viscosity [115]. Brownian motion of lipid monolayer domains also follow a fluid mechanical model wherein the mobility is independent of film viscosity but depends on the viscosity of the subphase [116]. This contrasts with the supposition that there is little coupling between the monolayer and the subphase [117] complete explanation of the film viscosity remains unresolved. [Pg.120]

From stochastic molecnlar dynamics calcnlations on the same system, in the viscosity regime covered by the experiment, it appears that intra- and intennolecnlar energy flow occur on comparable time scales, which leads to the conclnsion that cyclohexane isomerization in liquid CS2 is an activated process [99]. Classical molecnlar dynamics calcnlations [104] also reprodnce the observed non-monotonic viscosity dependence of ic. Furthennore, they also yield a solvent contribntion to the free energy of activation for tlie isomerization reaction which in liquid CS, increases by abont 0.4 kJ moC when the solvent density is increased from 1.3 to 1.5 g cm T Tims the molecnlar dynamics calcnlations support the conclnsion that the high-pressure limit of this unimolecular reaction is not attained in liquid solntion at ambient pressure. It has to be remembered, though, that the analysis of the measnred isomerization rates depends critically on the estimated valne of... [Pg.860]

Einstein derived the relationship between spontaneous emission rate and the absorption intensity or stimulated emission rate in 1917 using a thennodynamic argument [13]. Both absorption intensity and emission rate depend on the transition moment integral of equation (B 1.1.1). so that gives us a way to relate them. The symbol A is often used for the rate constant for emission it is sometimes called the Einstein A coefficient. For emission in the gas phase from a state to a lower state j we can write... [Pg.1131]

Ruths M and Granick S 1998 Rate-dependent adhesion between opposed perfluoropoly (alkyl ether) layers dependence on chain-end functionality and chain length J. Rhys. Chem. B 102 6056-63... [Pg.1749]

Stripping voltammetry involves the pre-concentration of the analyte species at the electrode surface prior to the voltannnetric scan. The pre-concentration step is carried out under fixed potential control for a predetennined time, where the species of interest is accumulated at the surface of the working electrode at a rate dependent on the applied potential. The detemiination step leads to a current peak, the height and area of which is proportional to the concentration of the accumulated species and hence to the concentration in the bulk solution. The stripping step can involve a variety of potential wavefomis, from linear-potential scan to differential pulse or square-wave scan. Different types of stripping voltaimnetries exist, all of which coimnonly use mercury electrodes (dropping mercury electrodes (DMEs) or mercury film electrodes) [7, 17]. [Pg.1932]

Under diffusion controlled conditions tire reaction rate depends, tlien, only on tire supply of 02(g) to the surface which is detennined by Pick s law ... [Pg.2721]

It is wortli noting tliat under activation control tlie reaction rate depends on crystal orientation as tlie strengtli of tlie... [Pg.2721]

Corrosion suppression by inhibitors can be achieved by adding chemical species to tlie environment, which lead to a strong reduction of tlie dissolution rate. Depending on tlieir specific action, corrosion inliibitors can be divided into tlie following groups. [Pg.2730]

Zhang H and Banfieid J F 1999 New kinetic modei for the nanocrystaiiine anatase-to-rutiie transformation reveaiing rate dependence on number of particies Am. Miner. 84 528... [Pg.2924]

In particular if the reaction rate depends only on Cj, which is the case, for example, if the reaction is irreversible with mass,-action kinetics, then these reduce further to a pair of equations, namely... [Pg.164]

When the solvent around the spot has evaporated, the plate is placed ertically in a glass developing tank (a cylinder for small slides) which contains a small quantity of the solvent and is lined with filter-paper dipping into the solvent the level of the latter is adjusted, preferably with a pipette, so that the lower edge of the absorbent layer is under the soh ent but the spot is above this level, and the top of the cylinder is then firmly closed. The solvent rises through the adsorbent layer, and the components of the mixture ascend at different rates depending on their affinities for the adsorbent. [Pg.58]

When large concentrations of water are added to the solutions, nitration according to a zeroth-order law is no longer observed. Under these circumstances, water competes successfully with the aromatic for the nitronium ions, and the necessary condition for zeroth-order reaction, namely that all the nitronium ions should react with the aromatic as quickly as they are formed, no longer holds. In these strongly aqueous solutions the rates depend on the concentrations and reactivities of the aromatic compound. This situation is reminiscent of nitration in aqueous nitric acid in which partial zeroth-order kinetics could be observed only in the reactions of some extremely reactive compounds, capable of being introduced into the solution in high concentrations ( 2.2.4). [Pg.44]

The anticatalytic effect of nitrous acid in nitration The effect of nitrous acid was first observed for zeroth-order nitrations in nitromethane ( 3.2). The effect was a true negative catalysis the kinetic order was not affected, and nitrous acid was neither consumed nor produced by the nitration. The same was true for nitration in acetic acid. In the zeroth-order nitrations the rate depended on the reciprocal of the square root of the concentration of nitrous acid =... [Pg.55]

Irrespective of the precision of these quantitative correlations, this approach is useful in emphasizing that relative rates depend on the nature of the reaction as well as of the aromatic compound. [Pg.137]

The kinetics of the nitration of benzene, toluene and mesitylene in mixtures prepared from nitric acid and acetic anhydride have been studied by Hartshorn and Thompson. Under zeroth order conditions, the dependence of the rate of nitration of mesitylene on the stoichiometric concentrations of nitric acid, acetic acid and lithium nitrate were found to be as described in section 5.3.5. When the conditions were such that the rate depended upon the first power of the concentration of the aromatic substrate, the first order rate constant was found to vary with the stoichiometric concentration of nitric acid as shown on the graph below. An approximately third order dependence on this quantity was found with mesitylene and toluene, but with benzene, increasing the stoichiometric concentration of nitric acid caused a change to an approximately second order dependence. Relative reactivities, however, were found to be insensitive... [Pg.224]

Rate of substitution is independent of both concentration and nature of nucleophile Nucleophile does not participate until after rate determining step (Section 8 8) Rate depends on both nature of nucleophile and its concentration (Sections 8 3 and 8 7)... [Pg.356]

First-Order Reactions The simplest case is a first-order reaction in which the rate depends on the concentration of only one species. The best example of a first-order reaction is an irreversible thermal decomposition, which we can represent as... [Pg.751]

When results are compared for polymerization experiments carried out at different frequencies of blinking, it is found that the rate depends on that frequency. To see how this comes about, we must examine the variation of radical concentration under non-stationary-state conditions. This consideration dictates the choice of photoinitiated polymerization, since in the latter it is almost possible to turn on or off—with the blink of a light—the source of free radicals. The qualifying almost in the previous sentence is actually the focus of our attention, since a short but finite amount of time is required for the radical concentration to reach [M-] and a short but finite amount of time is required for it to drop back to zero after the light goes out. [Pg.374]

Chemical Applications. Courtaulds has developed a series of acryHc-based fibers for controUed release of chemical reagents. The trade name of these fibers is Actipore. The reagents are entrapped within the fiber and slowly released at a rate dependent on the exact porosity of the fiber (102). [Pg.285]

As coagulation proceeds into the center of the forming fiber, the outside regenerates to cellulose at a rate dependent on the temperature and composition of the bath. [Pg.348]

Tin reacts completely with fluorine above 190°C to form tin tetrafluoride [7783-62-2] SnF. Titanium reacts appreciably above 150°C at a rate dependent on the size of the particles the conversion to titanium tetrafluoride [7783-63-3] TiF, is complete above 200°C. Fluorine reacts with zirconium metal above 190°C. However, the formation of a coating of zirconium tetrafluoride [7783-64 ] ZrF, prevents complete conversion, the reaction reaching... [Pg.123]

This is essentially a corrosion reaction involving anodic metal dissolution where the conjugate reaction is the hydrogen (qv) evolution process. Hence, the rate depends on temperature, concentration of acid, inhibiting agents, nature of the surface oxide film, etc. Unless the metal chloride is insoluble in aqueous solution eg, Ag or Hg ", the reaction products are removed from the metal or alloy surface by dissolution. The extent of removal is controUed by the local hydrodynamic conditions. [Pg.444]

Three-dimensional webs can be made on air-forming machines, provided the fibers used are relatively short and stiff and the webs made ate of relatively low density. Air-forming machines allow for production of web thicknesses up to several centimeters, and weights ranging from 30 to 3000 g/m at widths from one to several meters. Production rates, depending on web weight, range from 5 to 150 m /min. [Pg.151]

Disinfection. Ozone is a more effective broad-spectmm disinfectant than chlorine-based compounds (105). Ozone is very effective against bacteria because even concentrations as low as 0.01 ppm are toxic to bacteria. Whereas disinfection of bacteria by chlorine involves the diffusion of HOGl through the ceU membrane, disinfection by ozone occurs with the lysing (ie, mpture) of the ceU wall. The disinfection rate depends on the type of organism and is affected by ozone concentration, temperature (106), pH, turbidity, clumping of organisms, oxidizable substances, and the type of contactor employed (107). The presence of oxidizable substances in ordinary water can retard disinfection until the initial ozone demand is satisfied, at which point rapid disinfection is observed. [Pg.501]

For prolonged action therapy, granular-sized encapsulated particles, ie, beads, are used and can be both uncoated or coated. The uncoated beads provide the initial dose the others are made to dissolve at various rates depending on the coating type and thickness. [Pg.230]


See other pages where Rate dependence is mentioned: [Pg.50]    [Pg.246]    [Pg.205]    [Pg.206]    [Pg.395]    [Pg.1311]    [Pg.2502]    [Pg.3035]    [Pg.163]    [Pg.39]    [Pg.340]    [Pg.378]    [Pg.256]    [Pg.354]    [Pg.367]    [Pg.333]    [Pg.121]    [Pg.171]    [Pg.445]    [Pg.153]    [Pg.350]   
See also in sourсe #XX -- [ Pg.187 , Pg.241 ]




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Activation Energy and Temperature Dependence of Rate Constants

Activation Energy and the Temperature Dependence of Rates

Application to the Temperature Dependence of Steady Reaction Rate

Aqueous layer acid-dependent dissolution rate

Arrhenius Temperature Dependence of the Rate Constant

Asymptotic analysis for strongly temperature-dependent rates

Base strength, rate dependence

Burning rate pressure dependence

Catalysts rate depending

Catalytic Rate Dependence on UWr and

Chain Length Dependence of Propagation Rate Constants

Chemical reaction rate constant temperature dependence

Chemical reaction rates viscosity dependence

Coils rate dependence

Cold-drawing rate dependence

Composition-dependent rate coefficients

Concentration dependence of reaction rates

Concentration rate dependence

Concentration-Dependent Term of a Rate Equation

Condensation rate concentration dependence

Controlling the Growth Speed Evaporation Rate and Temperature Dependence

Conversion rate density temperature dependence

Cooling rate dependence

Cooling rate effects temperature dependence

Coverage-dependent rate constants

Creep rate stress dependence

Cure rate dependence

Dependence of Enzyme Reaction Rate on Substrate Concentration

Dependence of Polymerization Rate on Initiator

Dependence of Propagation Rate Constant on Monomer Structure

Dependence of Rate on Concentration

Dependence of Reaction Rate on Reactant Concentration

Dependence of rate constant

Dependence of rate constant on pressure

Dependence of rate on temperature

Dependence of reaction rate

Dependence of reaction rates on

Dependence of transformation rate

Dependence of viscosity on shear rate

Dependence on liquid flow rate

Deposition rate temperature dependence

Distance dependence of electron transfer rates

Electron transfer rate-distance dependence

Emulsifier polymer rate dependence

Emulsifier rate dependence

Example. Fitting a kinetic rate law to time-dependent data

Failure rate time-dependent

Fatigue rate dependence

Ferroelectric properties, rate dependencies

First-order rate constant, temperature dependence

First-order rate constants pressure dependence

Flow rate dependence

Frequency-dependent scattering rate

Gap-Dependent Apparent Shear Rate

Glass transition heating rate dependence

Growth rate pressure dependence

Growth rate temperature dependence

Growth rate, linear, concentration dependence

Hydrogenation rates, substrate dependence

Inhibited rate dependence

Initial rates total pressure dependence

Interfacial electron-transfer rates dependence

Ionic strength dependence of rate constants

Isomerization rate, solvent viscosity dependence

Kinetic rate constant pressure dependence

Kinetics rate temperature dependence

Kinetics temperature dependence, rate reaction

Loading rate dependence

Measurements of reaction rate and its dependence on experimental conditions

Molecular Weight Dependence of Crystal Growth Rate

Naphthalene decay rate, excitation energy dependence

Negative rate-dependence

Nonlinear Potential Dependence of Electrochemical Reaction Rates

Nonthermal reaction rate time-dependent

Nuclear spin relaxation rate, temperature dependence

Nucleation rate temperature dependence

Nucleation rate-overvoltage dependence

Onset of Shear Rate Dependence

Overall temperature-dependent decay rate constant

Oxidation rate temperature dependence

PH dependence of rates

Phase transformation rate temperature dependence

Polymerization rate, dependence

Polymers strain-rate dependence

Position-dependent rate

Position-dependent rate Potential energy functions

Position-dependent rate molecular dynamics simulation

Position-dependent rate simulation

Position-dependent rate thermodynamics

Potential Dependence of Interfacial Rate Constants

Potential dependence of the electrochemical reaction rate

Pressure dependence of rate constant

Pressure dependence of reaction rate

Pressure sensitive adhesive rate dependence

Primary normal stress coefficient shear rate dependence

Process rate-dependent

Quenching rate constants, free energy dependence

Quenching rate temperature dependence

Rate Dependence Upon Ligand Size

Rate Dependent Yielding

Rate coefficient time dependent

Rate coefficients temperature dependence

Rate constant apparent concentration dependence

Rate constant apparent pressure dependence

Rate constant dependence

Rate constant dependence on temperature

Rate constant energy dependence

Rate constant frequency dependent

Rate constant ionic strength dependence

Rate constant pressure dependence

Rate constant pressure dependent

Rate constant space dependent

Rate constant temperature dependence

Rate constant time dependence

Rate constant time-dependent

Rate constant wavelength dependence

Rate constant, dependence, pyridinium

Rate dependency

Rate dependency

Rate equations, governing time dependence

Rate laws continued temperature dependence

Rate laws temperature dependence

Rate pH dependence

Rate potential-dependent electrochemical

Rate, dependence on temperature

Rate-controlled processes, dependence

Rate-controlled processes, dependence surface structure

Rate-dependent adhesion effect

Rate-dependent plastic flow

Rate-dependent plasticity

Rates Depend on Temperature

Rates of reactions and their temperature dependence

Reaction Rates Depend on Temperature

Reaction rate constant dependence on temperature

Reaction rate constant temperature dependence

Reaction rate constant time dependence

Reaction rate constant, temperature dependency

Reaction rate dependence on concentrations

Reaction rate dependence on temperature

Reaction rate pressure dependence

Reaction rate temperature dependence

Reaction rate temperature dependent

Reaction rate time dependent

Reaction rate, conversion dependence

Reaction rate, field dependence

Reaction rates, potential dependence

Reduction rate constant dependence

Relaxation rate, temperature dependence

Scan Rate Dependencies

Sequence dependence, charge transfer rate

Shear rate dependence of viscosity

Shear rate dependent solution

Shear rate dependent solution micelles

Shear rate time dependent

Shear rate, dependence

Shear rate, dependence viscosity

Shear rate-dependent viscosity

Shear-rate dependent viscosity, spin

Shear-rate-dependent flow

Shrinkage heating rate dependence

Sintering heating rate dependence

Size-dependent aggregation rates

Software for the calculation of pressure-dependent rate constants

Specific reaction rate temperature dependence

Steady-state reaction rate temperature dependence

Suspension polymerization viscosity-shear rate dependence

Suspension viscosity-shear rate dependence

Sweep-rate dependence

TEMPERATURE DEPENDANCE OF RATE

Temperature Dependence of Linear Crystal Growth Rate

Temperature Dependence of Nucleation Rate

Temperature Dependence of Rate Coefficients

Temperature Dependence of Rate Constants Activation Energies

Temperature Dependence of Rate and Chain Length

Temperature Dependence of Reaction Rate Constant

Temperature Dependence of the Chain Reaction Rates

Temperature and strain-rate dependences of yield

Temperature dependence cytochrome oxidation rate

Temperature dependence electron transfer rates

Temperature dependence of electrode reaction rates

Temperature dependence of rate

Temperature dependence of rate constants

Temperature dependence of reaction rate

Temperature dependence of the rate

Temperature dependence of the rate coefficient

Temperature dependence of the rate constant

Temperature dependence rates

Temperature dependency of degradation rate

Temperature dependency of reaction rate

Temperature dependency, reaction rate

Temperature-Dependent Term of a Rate Equation

Termolecular Reactions and Pressure Dependence of Rate Constants

The distance dependence of electron transfer rates

The temperature dependence of reaction rates

The time-dependent rate coefficient

Thermogravimetric analysis reaction rate temperature dependence

Time dependence effects corrosion-rate measurements

Time-dependent escape rate

Time-dependent nonthermal rate

Time-dependent rate constant, changing

Transformation rate temperature dependence

Viscosity rate dependence

Viscosity strain-rate-dependent

Water radiolysis temperature dependent rate constants

Yield strain-rate dependence

Yield stress strain-rate dependence

Zero-shear-rate viscosity molar mass dependence

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