ASME dispersion

The ASME plume rise equations and the ASME dispersion parameters. 

The ASME Dispersion Parameters. The horizonal and vertical dispersion parameters are represented by the following empirical power law equation... 

ASME, Recommended Guide forthe Prediction of the Dispersion of Airborne Ejfluents, ASME, New York, 1968. 

Boilers with relatively large furnaces, large steam space, and internal chelant, polymer, and/or antifoam treatment can often tolerate higher levels of FW impurities than those in the table and still achieve adequate deposition control and steam purity. Removal of these impurities by external pretreatment is always a more positive solution. Alternatives must be evaluated as to practicality and economics in each individual case. The use of some dispersant and antifoam internal treatment is typical in this type of boiler operation therefore, it can tolerate higher FW hardness than the boilers in Table 12.2 (ASME Table 1). 

Welker, J. R. 1987. Thermal Radiation and Vapor Dispersion Exclusion Zones. Paper presented at the ASME Pipeline Engineering Symposium. Dallas, TX. New York American Society of Mechanical Engineers. 

Narumanchi, S.V.J., J.Y. Murthy, and C.H. Amon. Computations of Sub-micron Heat Transport in Silicon Accounting for Phonon Dispersion, in ASME Summer Transfer Conference, HT2003-47490. 2003. Las Vegas, NV. 

Mazumder, S., and Majumdar, A., Monte Carlo Study of Phonon Transport in Solid Thin Films Including Dispersion and Polarization. ASME Journal of Heat Transfer, 2001.123 p. 749-759. 

Chen, P.P. and Crowe, C.T. (1984), On the Monte Carlo method for modeling particle dispersion in turbulence, ASME Symp. Gas-Solid Flows, p. 37. 

Sommerfeld, M. (1990), Numerical simulation of the particle dispersion in turbulent flow the importance of particle lift forces and particle/wall collision models, in Numerical Methods for Multiphase Flows, Vol. 91, ASME, New York. 

O. C. Iloeje, W. M. Rohsenow, and P. Griffith, Three-Step Model of Dispersed Flow Heat Transfer (Post CHF Vertical Flow), ASME Paper 75-WA/HT1,1975. 

Fig. 1.23 Sketch of the cross-section of superhelical DNA in a cell. Left DNA is dispersed throughout the cell. Right DNA is confined within the nucleoid phase [255]. Reprinted from C. L. Woldringh and T. Odijk in Organization of the Prokaryotic Genome, R. L. Charlebois Ed.). ASM Press, Amsterdam, Copyright 1999, with permission from ASM Press...

Fan, F.G. and Ahmadi, G. (1995a). Dispersion of EUipsoidal Particles in an Isotropic Pseudo-Turbulent Flow Field. ASME J. Fluid Eng., Vol. 117, pp. 154-161. 

Figure 8 The peak position vs. the reciprocal of temperature for zeolite 4A/silicone oil suspension. The ions from zeolite are responsible for the dielectric dispersion peak. Redrawn from F.E. Filisko, and D.R. Gamota, Recent Adv. Non-newtonian Flows, ASME, 153(1992)75.

The effect of the computational grid size on the prediction of a flammable cloud dispersion. In International Conference on Ocean, Offshore and Arctic Engineering, 2013, San Francisco, California, USA. Proceedings of the ASME 2014 33th International Conference on Ocean, Offshore and Arctic Engineering, 2014. pp. 1-8. 

Usmanova, R. R. Zaikov, G. E. Stoyanov, O. V. and Klodzinska, E. Research of the Mechanism of Shock-Inertial Deposition of Dispersed Particles from Gas Flow.The Bulletin of the Kazan Technological University 2013,7(5( Pl, 203-207 p. (in Russian). Vasquez, S. A. and Ivanov, V. A. A phase coupled method for solving multiphase problems on unstructured meshes. In Proceedings of ASME FEDSM OO ASME 2000 Fluids Engineering Division Summer Meeting. Boston June 2000. 

VioUet PL, Simonin O Modelling dispersed two-phase flows closure, validation and software development, Appl Mech Rev 47(6) S80-S84, 1994. Part 2, ASME. 

---