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Chilton

Chilled surface drying ChiUproofing Chilton-Colburn analogy Chimeramycins Chimeras... [Pg.192]

IControl Systems), Chilton Company, Radnor, Pa., pubHshed monthly. [Pg.340]

Only two companies produce specialty malts in roasters or specialty kilns in North America Breiss Malting Co. (Chilton, Wisconsin) and Extractos y Maltas (Mexico City). Other malting companies produce high dried malts in conventional kilns which are used by brewers for color or flavor purposes. Specialty malts represent less than 2% of malt sold in North America. [Pg.484]

B. Liptak, ed.. Instrument Engineer s Handbook, Chilton, Radnor, Pa., 1982. [Pg.44]

B. G. Liptak, Instrument Engineers Handbook—Process Measurement and Analysis, 3rd ed., Chilton Book Co., Radnor, Pa., 1995, pp. 523—601. [Pg.29]

D. P. Swanson, H. M. Chilton, andj. H. Thrall, eds.. Pharmaceuticals in Medical Imaging, Macmillan Co., New York, 1990. [Pg.472]

Christopher Boemer Kenneth Chilton Washington University... [Pg.549]

Much of the material was taken from Sec. 1. of the fifth edition. The contribution of Cecil H. Chilton in developing that material is acknowledged. [Pg.21]

Chilton-Colbum factor for mass transfer, Eq. (5-291) Dimensionless Dimensionless... [Pg.589]

The penetration theory predicts that should vary by the square root of the molecular difriisivity, as compared with film theoiy, which predicts a first-power dependency on D. Various investigators have reported experimental powers of D ranging from 0.5 to 0.75, and the Chilton-Colburn analogy suggests a 2/3 power. [Pg.604]

Chilton-Colburn analogies, Ns = 1-0, (gases), f = drag coefficient. Corresponds to item 5-21-F and refers to same conditions. 8000 < Nr < 300,000. Can apply analogy, jo =//2, to entire plate (including laminar portion) if average values are used. [Pg.605]

U. Tubes, turbulent, smooth tubes, Chilton-Colburn analogy... [Pg.609]

On occasion one will find that heat-transfer-rate data are available for a system in which mass-transfer-rate data are not readily available. The Chilton-Colburn analogy provides a procedure for developing estimates of the mass-transfer rates based on heat-transfer data. Extrapolation of experimental or Jh data obtained with gases to predict hquid systems (and vice versa) should be approached with caution, however. When pressure-drop or friction-factor data are available, one may be able to place an upper bound on the rates of heat and mass transfer, according to Eq. (5-308). [Pg.625]

Time Systems, McGraw-HiU, New York, 1985 Hawryszldewycs, Database Analysis and Design, Science Research Associates Inc., Chicago, 1984 Kham-hata, Microprocessois/Microcomputers Architecture, Software, and Systems, 2d ed.. Whey, New York, 1987 Liptak, Instrument Engineers Handbook, Chilton Book Company, Philadelphia, 1995 Melhchamp (ed.), Real-Time Computing with Applications to Data Acquisition and Control, Van Nostrand Reinhold, New York, 1983. [Pg.770]

For systems other than air-water vapor, the value of h /k c, may differ appreciably from unity, and the wet-bulb and adiabatic-saturation temperatures are no longer equal. For these systems the psychrometric ratio may be obtained by determining h /k from heat- and mass-transfer an ogies such as the Chilton-Colburn analogy [Ind. Eng. Chem., 26, 1183 (1934)]. For low humidities this analogy gives... [Pg.1151]

Data for determining the size of natural-draft towers have been presented by Chilton [Proc. Inst. Elec. Eng., 99,440 (1952)] and Rish and Steel (ASCE Swuposium on Thermal Power Plants, October 19.58). Chilton showed that the duty coefficient Df of a tower is approximately constant over its normal range of operation and is related to tower size by an efficiency factor or performance coefficient as follows ... [Pg.1169]

Equations (13-115) to (13-117) contain terms, for rates of heat transfer from the vapor phase to the hquid phase. These rates are estimated from convective and bulk-flow contributions, where the former are based on interfacial area, average-temperature driving forces, and convective heat-transfer coefficients, which are determined from the Chilton-Colburn analogy for the vapor phase and from the penetration theoiy for the liquid phase. [Pg.1292]


See other pages where Chilton is mentioned: [Pg.31]    [Pg.46]    [Pg.417]    [Pg.462]    [Pg.482]    [Pg.47]    [Pg.48]    [Pg.81]    [Pg.80]    [Pg.548]    [Pg.548]    [Pg.548]    [Pg.107]    [Pg.559]    [Pg.59]    [Pg.461]    [Pg.28]    [Pg.178]    [Pg.255]    [Pg.448]    [Pg.468]    [Pg.364]    [Pg.548]    [Pg.553]    [Pg.604]    [Pg.625]    [Pg.664]    [Pg.757]    [Pg.1051]    [Pg.1291]   
See also in sourсe #XX -- [ Pg.134 , Pg.525 ]

See also in sourсe #XX -- [ Pg.5 ]

See also in sourсe #XX -- [ Pg.766 , Pg.786 ]




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Chilton, James

Chilton, Thomas

Chilton-Colburn

Chilton-Colburn analogy

Chilton-Colburn j-factor

Chilton-Colburn relation

Chilton—Colburn factor

Interfacial transfer Chilton-Colburn analogy

Mass transfer Chilton-Colburn analogy

The -factor of Chilton and Colburn for flow in tubes

Turbulent flow Chilton-Colbum analogy

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