By J. Macinko, D. B. Chelton, J. Dean (auth.), K. D. Timmerhaus (eds.)
By renowned request, the nationwide Bureau of criteria was once back a bunch to a convention on cryogenic engineering on August 19-21, 1957. comparable conferences have been held the following in 1954 and 1956. The recognition of over 40 papers for this convention was once definitely an indication of the expanding task and curiosity during this engineering box. There turns out little question that it'll keep growing, justifying the necessity for annual conferences. To make the complaints extra fascinating an try was once made to incorporate up to attainable of the overall dialogue which each one paper. to procure person reprints of somebody specific paper, please touch the authors at once. 1957 CRYOGENIC ENGINEERING convention COMMITTEE B. W. Birmingham nationwide Bureau of criteria S. C. Collins Massachusetts Institute of expertise E. F. Hammel Los Alamos clinical Laboratory R. B. Scott nationwide Bureau of criteria ok. D. Timmerhaus collage of Colorado W. T. Ziegler Georgia Institute of know-how i ACKNOWLEDGMENTS The 1957 Cryogenic Engineering convention Committee gratefully recognizes the ongoing aid and curiosity of the subsequent businesses who've made the 1957 Cryogenic Engineering convention and the ebook of this lawsuits attainable. L' Air Liquide Air items, Inc. Allison department, common Motor s American Messer company Aro gear company Beech plane company Bell airplane Boeing aircraft corporation Cambridge company Convair Curtiss-Wright company Garrett company basic electrical corporation Herrick L. Johnston, Inc. Hofman Laboratories Linde corporation A. D. Little, Inc.
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Extra info for Advances in Cryogenic Engineering: Proceedings of the 1957 Cryogenic Engineering Conference, National Bureau of Standards Boulder, Colorado, August 19–21, 1957
LOOO cu. ft. liquid oxygen, assuming ideal compres sion Ideal Case A Actual Case B B-A Work equivalent, taking compression inefficiency factor into account, kw. ft. 55 1. 07 1. 54 1. 03 1. 05 1. 85 1. 41 It will be observed that the figure for total irreversibility suffered in the ideal case differs slightly from that given in Tables II and III. This is because in Table IV separation into the actual products has been as sumed for the ideal unit, in order to facilitate direct comparison with the actual rectification system, whereas previously, in comparing the complete cycle, an ideal separation was assumed, giving rise to a higher liquid oxygen yield.
Ft. of liquid oxygen is therefore not very great. In a large plant producing gaseous products only, however, the power consumption may be only about one third of that of a liquid oxygen plant, but it can be shown that the work penalty due to the adiabatic nature of the rectification process is of the same order. The incentive for increased reversibility in the rectification process is therefore conSiderably greater in this case if it can be achieved without a proportionate increase in capital charges.
Figure 4. -~- ... ) Figure 3. Temperature-liquid flow diagrams for reversible separation of an ethylene-ethane-propylene mixture -50- complete reversible separation. The ternary column separates the feed into a binary mixture of ethylene-ethane at the top and a binary mixture of ethane-propylene at the bottom. The top and bottom binary columns then complete the reversible separation of the respective binaries. A plot of temperature versus liquid flow for the ternary column is shown as the solid line on Figure 3a.
Advances in Cryogenic Engineering: Proceedings of the 1957 Cryogenic Engineering Conference, National Bureau of Standards Boulder, Colorado, August 19–21, 1957 by J. Macinko, D. B. Chelton, J. Dean (auth.), K. D. Timmerhaus (eds.)