Abstract
Current practice in the liquefied natural gas (LNG) industry is to chill the product at atmospheric pressure to its saturation temperature or slightly below so that the liquid can be handled readily without resort to the use of pressure vessels. This practice is advantageous in that a minimum thickness of steel is required in the construction of the vessels for the containment; however, the practice has a number of disadvantages compared with maintaining the product in the liquid phase at some intermediate temperature and pressure.
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References
A. E. Uhl and J. R. Giese, “Economics of LNG Import-Export Systems,” presented at the Petroleum Mechanical Engineering and Pressure Vessel Conference, New Orleans, Louisiana, September 1972.
S. Chansky and H. E. Haley, “How to Use the Cold in LNG,” LNG Economics and Technology, Energy Communications Incorporated, Dallas, Texas (1972).
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A. R. Duffy and R. J. Eiker, “Fracture Behavior in Pipe Pressured with LNG,” Battelle Memorial Institute, Columbus, Ohio (1971).
ASME Boiler and Pressure Vessel Code, Section VIII, Division 1.
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© 1980 Springer Science+Business Media New York
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Bennett, C.P. (1980). Marine Transportation of LNG at Intermediate Temperature. In: Timmerhaus, K.D., Snyder, H.A. (eds) Advances in Cryogenic Engineering. Advances in Cryogenic Engineering, vol 35 A. Springer, Boston, MA. https://doi.org/10.1007/978-1-4613-9856-1_84
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DOI: https://doi.org/10.1007/978-1-4613-9856-1_84
Publisher Name: Springer, Boston, MA
Print ISBN: 978-1-4613-9858-5
Online ISBN: 978-1-4613-9856-1
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