By W. L. Culbertson, J. Horn (auth.), K. D. Timmerhaus (eds.)
1969 marked the go back of the Cryogenic Engineering convention, now affiliated with the nationwide Academy ofSciences during the department ofEngineering, nationwide examine Council, to the college of California at l. a.. As in 1962, the Cryogenic Engineering convention gratefully recognizes the help of UCLA, its Engineering and actual Seien ces Extension department, and particularly J. Dillon, S. Houston, H. L. Tallman, and their stafffor serving as hosts to the 1969 Cryogenic Engineering convention. The nationwide Academy of Sciences is a personal honorary association of greater than seven hundred scientists and engineers elected at the foundation of remarkable contributions to wisdom. validated by way of a Congressional Act of Incorporation, the Academy works to extra technological know-how and its use for the overall welfare by means of bringing jointly the main certified contributors to house medical and technological difficulties of extensive importance. The nationwide examine Council was once geared up as an enterprise of the nationwide Academy of Sciences in 1916, to let the vast neighborhood of U.S. scientists and engineers to affiliate their efforts with the Iimited club of the Academy in provider to technological know-how and the country. The department of Engineering is without doubt one of the 8 significant Divisions into which the nationwide examine Council is equipped for the behavior of its paintings. Its club comprises representatives of the nation's best technical societies as weH as a couple of members-at-Iarge. The Cryogenic Engineering convention is a corporation of the department of Engineering.
Read or Download Advances in Cryogenic Engineering: Proceedings of the 1969 Cryogenic Engineering Conference University of California at Los Angeles, June 16–18, 1969 PDF
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Extra info for Advances in Cryogenic Engineering: Proceedings of the 1969 Cryogenic Engineering Conference University of California at Los Angeles, June 16–18, 1969
64 cm spacing between equilibrium trays is packed with copper wool, and the transfer area provided by the trays has been designed to allow study of solidvapor phase equilibrium in a wide variety of systems. Two additional stainless stee1 capillary tubes, not shown in Fig. I, are used to support the cell from the top plate. Refrigeration is provided by injection of refrigerant liquid, from a reservoir (1400 cm 3 ) below the cell, through a heat exchanger soldered to a skirt on the base of the cello The resulting refrigerant gas passes through an annular space on the cell, exits at the upper end, and is used to cool a light copper radiation shield.
L. 11-........... "I NATURAL GAS INTERMEDfATE PRESSURE MET LNG PRODUCT Fig. 3. General Cascade A complex flowsheet. 0000 Computer Simulation of Natural Gas Uquefaction Plant Processes 25 This plant has two refrigerants (propane and ethylene), three evaporators, and seven additional countercurrent exchangers. The maximum number of streams in an exchanger in this flowsheet is limited to seven; thus the propane high pressure liquid and intermediate pressure vapor do not undergo heat exchange. Carbon dioxide is removed at the warm end of the plant and water is removed after the first exchanger.
J. Kidnay, M. J. Hiza, and P. F. Dickson NBS Institute/ar Basic Standards Baulder, Calarada INTRODUCTION The concentration vs time, or breakthrough, curves for a number of binary systems containing hydrogen have been measured on both charcoal [IJ and a synthetic zeolite [z]. The equations proposed by Eagleton and Bliss [3J were applied to these breakthrough curves in order to evaluate a gas phase mass transfer coefficient k g and an adsorbed phase mass transfer coefficient k s • In many commercial adsorption units, however, more than one impurity is removed from the gas being purified.