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Steady state calculations

Quality-assurance procedures have to be established for the checking of both input and results checks of energy balances, plausibility tests, and comparison with steady-state calculations and with results from similar cases. These checks are demanding and time consuming and thus prone to be omitted but are mandatory for reliable simulations. [Pg.1080]

Airflows are determined basically by a steady-state calculation for each time step. At each time step, first, pressures at external nodes are calculated on the basis of the wind pressure coefficients and the actual wind speed and direction. Then, for all conductances, the local pressures at each side of the link are calculated. At internal links, this pressure is dependent on the (unknown) zone pressure p and the aerostatic pressure variation due to the height of the link with respect to the zone reference height. At external links, this pressure is dependent on the external node pressure and the aerostatic pressure variation due to the height of the link with respect to the stack reference height. For the aerostatic pressure, the air density is determined considering the temperature, the humidity, and (if relevant) the contaminant concentrations in the zone or in the outside air, respectively. From this, the pressure differences across each conductance can be calculated, and from this the mass airflow tor each conductance /. [Pg.1086]

The humidity and contaminant transport calculation is based on the previously calculated airflows, applying again the principle of mass conservation for the species under consideration. For each time step, the concentrations are calculated on the basis of the airflows, the source and sink strengths in the zones, and the concentration values at the previous time step. In contrast to the airflow calculation, which is a steady-state calculation at each time step, the contaminant transport calculation is dynamic. Therefore, the accuracy of the concentration results depends on the selected time-step interval. [Pg.1087]

All the previous material balance examples have been steady-state balances. The accumulation term was taken as zero, and the stream flow-rates and compositions did not vary with time. If these conditions are not met the calculations are more complex. Steady-state calculations are usually sufficient for the calculations of the process flow-sheet (Chapter 4). The unsteady-state behaviour of a process is important when considering the process start-up and shut-down, and the response to process upsets. [Pg.54]

Rate constant temperature dependence Processing threshold Calculation of rate constants at different temperatures, including collision numbers and concentrations of species in steady state Calculation of the rate of photodissociation and cosmic ray-induced molecular processing from photon and particle fluxes... [Pg.154]

Maidana MA, Naudin JJ, Espino M, Garcia MA, Sanchez-Arcilla A (2002) Feasibility and usefulness of steady-state calculations of the mean circulation in the vicinity of the Ebro mouth. Model tests against field data. Cont Shelf Res 22 229-245... [Pg.19]

The steady-state calculation method for surface water is based on the mass balance schematically shown in Figure 9. [Pg.71]

The global phosphate system is described in Figure 7.10 (Lasaga, 1980). Table 7.1 gives the amounts held by each reservoir, and Table 7.2 the fluxes between reservoirs. Assuming steady-state, calculate the evolution of the world phosphate system if 10000 x 109 kg of phosphorus from fertilizer (mined from an isolated reservoir) were dumped on land in a short period of time. [Pg.376]

Assume HN03 is in a steady state. Calculate the ratio [N02]/[HN03] at a temperature of 300 K and 1 atm pressure using the DeMore et al. (1997) recommendations and those of Brown et al. (1999a, 1999b). For (a) T = 300 K and P = 1 atm and (b) T = 220 K and P = 150 Torr, characteristic of the lower stratosphere/ upper troposphere, would the revised kinetics be expected to bring the measurements and models into better agreement ... [Pg.287]

Cantrell, C. A., R. E. Shetter, J. G. Calvert, F. L. Eisele, E. Williams, K. Baumann, W. H. Brune, P. S. Stevens, and J. H. Mather, Peroxy Radicals from Photostationary State Deviations and Steady State Calculations during the Tropospheric OH Photochemistry Experiment at Idaho Hill, Colorado, 1993, J. Geophys. Res., 102, 6369-6378 (1997b). [Pg.639]

To achieve (b), it is necessary to use relief sizing methods that take account of the dynamics of the pressure relief, event. Pressure relief systems for runaway chemical reactions usually discharge a two-phase mixture (see 4.3). If a steady-state calculation were used to size the relief system, then it would be necessary to size it for the volumetric rate of two-phase mixture equal to the volumetric, rate, of gas/ vapour generation at a particular point (e.g. at the relief pressure for vapour systems). This leads to very large calculated relief system sizes. [Pg.35]

However, because the relief system is discharging a two-phase mixture, it is acting to empty the reactor. Account can be taken of this by performing a dynamic (non-steady-state) calculation, and many of the methods described later in this Workbook do this. By taking advantage of emptying, a smaller relief system size can... [Pg.35]

Figure 22.3 One-dimensional concentration profiles at steady-state calculated from the diffusion/advec-tion/reaction equation (Eq. 22-7) for different parameter values D (diffii-sivity), x (advection velocity), and kr (first-order reaction rate constant). Boundary conditions at x = 0 and x - L are C0 and CL, respectively. Pe = 7. vx ID is the Peclet Number, Da = Dk/v] is the Damkohler Number. See text for further explanations. Figure 22.3 One-dimensional concentration profiles at steady-state calculated from the diffusion/advec-tion/reaction equation (Eq. 22-7) for different parameter values D (diffii-sivity), x (advection velocity), and kr (first-order reaction rate constant). Boundary conditions at x = 0 and x - L are C0 and CL, respectively. Pe = 7. vx ID is the Peclet Number, Da = Dk/v] is the Damkohler Number. See text for further explanations.
There is still another point to be discussed, which may limit the calculations presented in Tables 23.4 and 23.5. In 1986, when the concentrations were measured, the lake may not have been at steady-state. In fact, the PCB input, which mainly occurred through the atmosphere, dropped by about a factor of 5 between 1965 and 1980. However, the response time of Lake Superior (time to steady-state, calculated according to Eq. 4 of Box 12.1 from the inverse sum of all removal rates listed in Table 23.4) for both congeners would be less than 3 years. This is quite short, especially if we use the model developed for an exponentially changing input (Chapter 21.2, Eq. 21-17) with a specific rate of change a = - 0.1 yr 1 (that is, the rate which... [Pg.1069]

In a steady-state calculation, it must be the case that the surface species concentrations (or site fractions) are not changing with time, that is,... [Pg.474]

Gas studies are well covered with extensive explanation and interpretation of experimental data, such as steady state calculations, all illustrated by frequent use of worked examples. Solution kinetics are similarly explained, and plenty of practice is given in dealing with the effects of the solvent and non-ideality. Students are given plenty of practice, via worked problems, in handling various types of mechanism found in solution, and in interpreting ionic strength dependences and enthalpies, entropies and volumes of activation. [Pg.455]

Let us return to the comparison we made in Chapter 2 of multiple CSTRs in series. In Section 2.6.1 the steady-state designs of 1-, 2-, and 3-CSTR processes were developed, and in Section 2.9.1 the capital costs of the three alternative processes were determined. The steady-state calculations indicate control problems in the first reactor of the 2-CSTR and 3-CSTR processes because the jacket temperatures are getting closer to the supply cooling water temperature. [Pg.130]

Now, in analogy with Slater s Xa, the total energy functional can be conveniently expanded in a Taylor s series around the steady state calculated in advance by a preliminary SCF procedure. This state is characterized by the set of occupation... [Pg.278]

The column was modeled with AspenPlus / using the rigorous radf rac column model, in conjunction with the Redlich-Kwong-Soave equation of state for property estimation. Steady-state calculations indicated a reflux ratio of 87.67. This is a consequence of the difficult separation problem posed by the two closeboiling components. [Pg.196]

Nonlinearity of a reaction rate is a reason for improvement of the simple irreversible reaction A" — B. Low-frequency temperature oscillation around the average value T increases the reaction rate compared to a steady-state calculated at this average temperature. A positive effect can also be obtained due to concentration variation if n > 1 and a time average concentration is restricted. [Pg.496]

PL2 - slope of placebo effect as a function of time (in days), Di - slope of drug effect as a function of AUC (24 h steady state), D2 - slope of drug effect as a fraction of the slope of placebo effect on time, E50 -drug effect that results in a 50% reduction in TSS, AUC - area under the plasma concentration versus time curve over 24 h at steady state calculated from individual predicted CL in the analysis. [Pg.744]

Note that these are all steady-state calculations. The concentration does not change as a function of time. Thus, this calculation cannot be used to determine the concentration of the dye in the lake just after the dye begins to be added or just after the dye stops being added. But do not worry we have other tools for getting at these issues. [Pg.28]

Non-ideal explosives have Chapman-Jouguet (C-J) detonation parameters (pressure/velocity) significantly different from that expected from a thermochemical / hydrodynamic code for equilibrium and steady state calculations. Therefore, common computer codes such as Cheetah, EXPL05 and others often do not correctly predict the detonation parameters of non-ideal explosives such as ANFO or me-talized explosives. [Pg.105]

The entropy production rate is determined with quasi-steady-state calculations. The following constant gradients in the gas phase at each stage are used ... [Pg.179]

By use of the techniques described in Section V-b-2, steady-state calculations were performed for both a summer and a winter latitude of 30°N with the set of equations in Section V.B.3. The values adopted for those constituents with fixed altitude profiles were consistent with the above conditions. The calculations were made with and without the inclusion of rainout as a loss path for long-lived species. [Pg.486]

The process operates at steady state. Calculate the required cooling rate. [Pg.362]

For provinces younger than the Paleozoic, the compilation of Pollack et al. (1993) indicates mean heat flow values that are larger than that for the Paleozoic (64 mW m for the Mesozoic and up to 97 mW m for the Cenozoic, compared to the mean Paleozoic value of 58 mW m ). Such values are clearly affected by recent magmatic and tectonic events and hence cannot be used for steady-state calculations. We may consider with little chance of error that the mean Paleozoic value reflects average crustal heat production up to the present day. For the Mesozoic, the difference is small and within the uncertainty range. [Pg.1344]

Measurements and steady state calculations of OH concentrations at Manna Loa Observatory. J. Geophys. Res. 101, 14665-14679. [Pg.1932]

Figure 6 Ozone production efficiency, expressed as the rate of production of odd oxygen (O3 -h NO2) divided by the loss of NO . from steady state calculations. The calculations assume (i) CO and CH4 only (solid line) (ii) anthropogenic VOC with VOC/ NO = 10 (dashed line) (iii) anthropogenic VOC with VOC/NO c = 20 (short dashed line) (iv) CH, CH4 and 1 ppb isoprene (circles) and (v) anthropogenic VOC/NO = lOand 1 ppb isoprene (asterisks) (source Sillman, 1999 (reproduced by permission of Elsevier from Atmos. Environ. 1999, 33, 1821-1845) based on similar unpublished analyses by Greg Frost, NOAA Aeronomy lab). Figure 6 Ozone production efficiency, expressed as the rate of production of odd oxygen (O3 -h NO2) divided by the loss of NO . from steady state calculations. The calculations assume (i) CO and CH4 only (solid line) (ii) anthropogenic VOC with VOC/ NO = 10 (dashed line) (iii) anthropogenic VOC with VOC/NO c = 20 (short dashed line) (iv) CH, CH4 and 1 ppb isoprene (circles) and (v) anthropogenic VOC/NO = lOand 1 ppb isoprene (asterisks) (source Sillman, 1999 (reproduced by permission of Elsevier from Atmos. Environ. 1999, 33, 1821-1845) based on similar unpublished analyses by Greg Frost, NOAA Aeronomy lab).
Also steady state calculations, performed in different applied flow and potential conditions, need still to be compared in full detail with measurements performed in the same conditions. It is believed however that it is already proven that the concepts work and will open new possibilities for bubble simulations in electrochemical reactors. [Pg.116]


See other pages where Steady state calculations is mentioned: [Pg.325]    [Pg.128]    [Pg.40]    [Pg.111]    [Pg.17]    [Pg.326]    [Pg.641]    [Pg.163]    [Pg.194]    [Pg.583]    [Pg.587]    [Pg.251]    [Pg.556]    [Pg.137]    [Pg.482]    [Pg.523]    [Pg.4967]    [Pg.4968]   
See also in sourсe #XX -- [ Pg.28 ]




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