Design conditions for expansion joints in high-pressure heat exchangers
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There is a type 3 high-pressure heat exchanger with design pressures of 120 KG/CM2G and 55/F for the tube side/shell side. In KG/CM2G, design temperature: 280/290 degrees Celsius. Operating pressure: 91/46; operating temperatures (IN/OUT): 239/250 and 261.4/257.6. Are the existing process conditions sufficient for the design of the expansion joints on the shell side? If it is insufficient, what other parameters are needed? Thank you!
Just having the design temperature and design pressure is not enough to proceed with the further design work~~~~~~~ The properties of the materials in the tube side and shell side are also very important! How can it be determined whether it belongs to Category 3 containers with only the design pressure and temperature available? ^_^ This post was last edited by www557 on 2009-4-11 23:35