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McKay

R. A. McKay,M Study of Selected Parameters in S olid Propellant Processing,]et Propulsion Lab, Pasadena, Calif., Aug. 1986 J. L. Brown and co-workers. Manufacturing Technologyfor SolidPropellantIngredients/Preparation Reclamation, Morton Thiokol, Inc., Brigham City, Utah, Apt. 1985 W. P. Sampson, Eow Cost Continuous Processing of Solid Rocket Propellant, Al-TR-90-008, Astronautics Laboiatoiy/TSTR, Edwards AEB, Oct. 1990. [Pg.56]

J. Cigan, T. McKay, and T. O Keefe, eds., Cead—Zinc—Tin 80, Proceedings of a World Sjmposium on Metallurgy and Environmental Control, The Metallurgical Society, Warrendale, Pa., 1979. [Pg.567]

R. B. McKay, Proceedings of the TTth Internationa/ Conference of Organic Coatings Science and Techno/ogy, Athens, Greece, 1980, p. 499. [Pg.360]

Column crystalhzers of the end-fed type can be used for purification of many eutectic-type systems and for aqueous as well as organic systems (McKay loc. cit.). Column ciystaUizers have been used for xylene isomer separation, but recently other separation technologies including more efficient melt ciystaUization equipment have tended to supplant the Phillips style ciystaUizer. [Pg.1995]

FIG. 22-12 Pulsed -column capacity versus column size for 65 percent p-xylene feed. To convert gallons per hour to cubic meters per hour, multiply hy 0.9396 to convert square feet to square meters, multiply hy 0.0929. (McKay et al., prepr., 59th nat. meet. AIChE, East Columbus, Ohio.)... [Pg.1995]

Technological Applications of Dispersions, edited by Robert B. McKay... [Pg.953]

A detailed study performed by McKay et al. (1989) revealed some of the conditions necessary for a turbulent jet to initiate a detonation directly. These experiments are covered in more detail in Section 4.1.5. [Pg.86]

A deflagration-detonation transition was first observed in 1985 in a large-scale experiment with an acetylene-air mixture (Moen et al. 1985). More recent investigations (McKay et al. 1988 and Moen et al. 1989) showing that initiation of detonation in a fuel-air mixture by a burning, turbulent, gas jet is possible, provided the jet is large enough. Early indications are that the diameter of the jet must exceed five times the critical tube diameter, that is approximately 65 times the cell size. [Pg.89]


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See also in sourсe #XX -- [ Pg.289 ]

See also in sourсe #XX -- [ Pg.43 ]

See also in sourсe #XX -- [ Pg.43 ]




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