Leung

Marshaii M D, Charo A, Leung H O and Kiemperer W 1985 Characterization of the iowest-iying n bending state of Ar-HCi by far infrared iaser-Stark spectroscopy and moieouiar beam eiectric resonance J. Chem. Phys. 83 4924-33... 

Bian R X, Dunn R C, Xie X S and Leung P T 1995 Single molecule emission characteristics in near-field microscopy Phys. Rev. Lett. 75 4772-5... 

Leung K, Pokrant S and Whaley K B 1998 Exciton fine structure in CdSe nanoclusters Phys. Rev. B 57 12 291... 

J. M. Parry, C. S. Leung, and R. Wells, Structure and Operating Mechanisms of Inorganic Separators, Report NMSM CR-134692, Mar. 1974. 

Robert G. Emmet, Peter Harriott, Tim Laros, Wallace Leung, Shelby A. Miller,... 

Wallace Leung, Sc.D., Director, Process Technology, Rird Macliine Company Member, American Filtration and Separation Society (Director) (Section 18, Liquid-Solid Operations and Equipment)... 

There have been several analyses of turbulent heat transfer in annuh for example, Deissler and Taylor (NACA Tech. Note 3451, 1955), Kays and Leung [Int. J. Heat Ma.ss Transfer, 6, 537 (1963)], Lee [Int. J. Heat Transfer, 11, 509 (1968)], Sparrow, HaUman and Siegel [Appl. Sci. Res., 7A, 37 (1958)], and Johnson and Sparrow [Am. Soc. Mech. Eng. J. Heat Transfer, 88, 502 (1966)]. The reader is referred to these for details of the analyses. 

In a series of papers by Leung and coworkers (AlChE J., 32, 1743-1746 [1986] 33, 524-527 [1987] 34, 688-691 [1988] J. Loss Prevention Proc. Ind., 2[2], 78-86 [April 1989] 3(1), 27-32 [Januaiy 1990] Trans. ASME J. Heat Transfer, 112, 524-528, 528-530 [1990] 113, 269-272 [1991]) approximate techni ques have been developed for homogeneous equilibrium calculations based on pseudo-equation of state methods for flashing mixtures. 

FIG. 14-106 Overall integrated penetration as a function of particle-size distribution and collector parameters. (Calvett, Yung, and Leung, NTIS Puhl. PB-248050, 1975.)... 

FIG. 14-115 Experimental collection efficiencies of rectangular impactors. C is the Stokes-Ciinningbam correction factor Pp, particle density, g/ond U, superficial gas velocity, approaching the impactor openings, cm/s and ig, gas viscosity, P. Calveri, Yung, and Leung, NTIS Puhl. PB-24S050 based on Mercer and Chow, J. Coll. Interface Sci., 27, 75 (1.96S).]... 

FIG. 14-116 Experimental results showing effect of gas velocity and liquid load on entrainment from (a) vertical tube hanks with horizontal gas flow and (b) horizontal tnhe hanks with upflow. To convert meters per second to feet per second, multiply hy 3.281. (Calvert, Yung, and Leung, NTIS Publ PB-24S050. )... 

FIG. 14-122 Incremental pressure drop in knitted mesh due to the presence of hqiiid a) with the mesh crimps in the same direction and (h) with crimps in the alternating direction, based on the data of York and Poppele [Chem. Eng. Prog., 50, 421 (1954)]. To convert centimeters per minute to feet per minute, multiply hy 0.0328 to convert centimeters per second to feet per second, multiply hy 0.0328. (From Calveti, Yung, and Leung, NTIS Puhl PB-24S050, 1975.)... 

Solutions are given here for only the first three regimes. For Regime 4, see Leung and Epstein (1991). 

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