How to calculate the relief flow rate of a safety valve when the heat exchange tube of a heat exchanger breaks
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Heat exchanger: the steam is in the tube side at 250 degrees and 1.1 MPa, while butane is in the shell side at 40 degrees and 2 MPa. If the heat exchange tube breaks and C4 enters the steam side, its volume expands instantly. I’ve searched through many documents but found no information on this situation; how do you determine the amount of material that needs to be released in such cases? Thank you
This is quite simple. Take a look at these standards; I won’t do the calculations for you. If you calculate it according to these standards, it will also serve as a form of practice for you. If you have any questions, feel free to ask me
You don’t understand what I mean; when carbon tetrafluoride enters the steam, it expands instantly