Big Chemical Encyclopedia

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

Articles Figures Tables About

Boiling model

Thome et al. (2004) and Dupont et al. (2004) proposed the first mechanistic analysis for vaporization in a micro-channel, with a three-zone flow boiling model describing... [Pg.43]

Boiling models. As the result obtained by applying dimensional analysis is limited by the validity and completeness of the assumptions made prior to the analysis, experiments are the only safe basis for determining the correctness and adequacy of the assumptions. Several suggested models are reviewed briefly here. [Pg.88]

Past work by us as well as others has identified the following critical solvent components hydrogen donors, phenols, hydrogen shuttlers, hydrogen abstractors. Our studies used low boiling model compound mixture solvents for ease of distribution... [Pg.155]

Description of single component boiling/condensing boiling model... [Pg.117]

Because the boiling model described above is fully explicit, it is rapid and easy to apply. It has been used with success in modelling steam drums and boiler recirculation loops, direct-contact feedwater heaters, high-pressure feedwater heaters, deaerator towers and vessels, condensers and refrigeration loops. The application of the boiling model to a steam drum and recirculation loop will be discussed in the next section because of its importance for the modelling of power stations. [Pg.120]

While a rigorous treatment of the evaporator would make due allowance for its distributed nature, very useful and surprisingly accurate results are achieved by treating it as a lumped-parameter system, using the boiling model presented in Section 12.2. This may be used to determine the temperature and pressure inside the evaporator, and the split between water and steam. [Pg.121]

The saturated contents of the steam drum may be modelled directly by the boiling model of Section 12.2. [Pg.122]

CHANG, H.R., REID, R.C., Spreading-Boiling Model for Instantaneous Spills of Liquefied Petroleum Gas (LPG) on Water, J. Hazardous Materials 7 (1982) 19-35. [Pg.241]

Recently, some microscale heat transfer flow boiling models and correlations having a more general character have been proposed. Kandlikar and Balasubramanian [80]... [Pg.82]

Transient Reactor Analysts Code (TRAC) equation of state O for water and steam (obtained by fits to the steam tables) and a stiff gas equation of state for the melt. The constitutive relations required for the interfield coupling terms (heat transfer, momentum exchange, and phase change) include a bulk boiling model, a subcooled surface boiling model, a three-field flow regime map, and adaptations of standard heat transfer and momentum transfer correlations. [Pg.362]

Mass transfer between the water and steam fields is described by a simple bulk boiling model, assuming the existence of an interface between the two fields at the... [Pg.364]

In RUN4A the subcooled boiling model, surface entrainment model, and surface tracking were used. The melt distribution at time of bottom contact for this case is shown in Fig. 5, where it is apparent that the overall mixture region is considerably larger than in RUNl. The time of bottom contact is also later, 0.4s vs 0.3s. A steam chimney is still present, but steam is now being generated near the main melt mass at the tank bottom, as seen in Fig. 6. [Pg.375]

As another example, we shall consider the influence of the number of descriptors on the quality of learning. Lucic et. al. [3] performed a study on QSPR models employing connectivity indices as descriptors. The dataset contained 18 isomers of octane. The physical property for modehng was boiling points. The authors were among those who introduced the technique of orthogonahzation of descriptors. [Pg.207]

The primal advantage of hierarchical databases is that the relationship between the data at the different levels is easy. The simplicity and efficiency of the data model is a great advantage of the hierarchical DBS. Large data sets (scries of measurements where the data values are dependent on different parameters such as boiling point, temperature, or pressure) could be implemented with an acceptable response time. [Pg.233]

Another way of predicting liquid properties is using QSPR, as discussed in Chapter 30. QSPR can be used to And a mathematical relationship between the structure of the individual molecules and the behavior of the bulk liquid. This is an empirical technique, which limits the conceptual understanding obtainable. However, it is capable of predicting some properties that are very hard to model otherwise. For example, QSPR has been very successful at predicting the boiling points of liquids. [Pg.303]

Nitromethane is a very common material. Just go down to your local drag strip and pick up a gallon or two for doping your high performance cars fuel. It s also available up to 40% pure in RC model fuels. Simply fractionally distill the nitromethane (bp 101°C) out of the model fuel mixture and you re ready to go. If methanol Is present in the fuel formulation, some will azeotropically distill over with the nitromethane lowering its boiling point slightly, but this does not present a problem. [Pg.105]

View molecular models of dimethyl ether and ethylene oxide on Learning By Modeling Which one has the greater dipole moment Do the calculated dipole moments bear any relation ship to the observed boiling points (ethylene oxide +10°C dimethyl ether —25°C) d... [Pg.700]

Most theories of droplet combustion assume a spherical, symmetrical droplet surrounded by a spherical flame, for which the radii of the droplet and the flame are denoted by and respectively. The flame is supported by the fuel diffusing from the droplet surface and the oxidant from the outside. The heat produced in the combustion zone ensures evaporation of the droplet and consequently the fuel supply. Other assumptions that further restrict the model include (/) the rate of chemical reaction is much higher than the rate of diffusion and hence the reaction is completed in a flame front of infinitesimal thickness (2) the droplet is made up of pure Hquid fuel (J) the composition of the ambient atmosphere far away from the droplet is constant and does not depend on the combustion process (4) combustion occurs under steady-state conditions (5) the surface temperature of the droplet is close or equal to the boiling point of the Hquid and (6) the effects of radiation, thermodiffusion, and radial pressure changes are negligible. [Pg.520]

The agar-based impression materials are used extensively for dupHcating casts. Frequendy, it is desired to retain the original model for reference and do the actual work on a dupHcate cast. Partial-denture fabrication requires that the original stone cast be dupHcated in an investment. For dupHcating, the agar-based impression material is usually diluted with water, boiled, cooled to the desired temperature, and carefully poured over the model to be dupHcated. [Pg.491]

Nonboiling Height Model This model applies the churn-turbulent assumptions to only a toppoi tiou of the fluid in the protected equipment. Below this portion, boiling does not occur and there is no liquid swell. The location of this nonboihng height is estimated from a balance of the hydrostatic effec ts and the recirculation effects. [Pg.2292]


See other pages where Boiling model is mentioned: [Pg.46]    [Pg.8]    [Pg.89]    [Pg.182]    [Pg.59]    [Pg.371]    [Pg.375]    [Pg.46]    [Pg.8]    [Pg.89]    [Pg.182]    [Pg.59]    [Pg.371]    [Pg.375]    [Pg.2]    [Pg.82]    [Pg.664]    [Pg.120]    [Pg.172]    [Pg.39]    [Pg.421]    [Pg.63]    [Pg.74]    [Pg.192]    [Pg.493]    [Pg.253]    [Pg.1281]    [Pg.1290]    [Pg.1304]    [Pg.1340]    [Pg.2079]    [Pg.2554]   
See also in sourсe #XX -- [ Pg.117 ]




SEARCH



Application of the boiling model to a steam drum and recirculation loop

Boiling point group contribution models

Boiling, liquid pools, model

Models for Prediction of Incipient Boiling Heat Flux and Wall Superheat

Normal boiling-point model

Physical Model of the Explosive Boiling

Transitional boiling model

© 2024 chempedia.info