Seek help with the issue of heat exchanger calculation in the settings of the HGT20570 safety valve
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Seeking help with the calculation of the heat exchanger in the settings of the HGT20570 safety valve. As shown in the standards, this formula is only provided for when the high-pressure side is in a liquid phase; so how should the calculation be done when the high-pressure side is in a gas phase? Please help
Hello, for the calculation formulas in this, what value should be used for the adiabatic index K? Also, the inner diameter in the formulas is given in millimeters – does it need to be converted to meters before being used? Thank you