Seeking help with calculations for modified asphalt heat exchangers
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For a 100,000 t/a modified asphalt project, approximately 30,000 tons of flash oil are produced. The oil and gas enter at around 400°C and exit at about 110°C. I would like to calculate the theoretical heat exchange area; an industrial naphthalene vaporization cooler is planned to be used for this purpose. However, since I don’t have access to the physical property data of the flash oil, I’m unable to proceed with the calculations. Do you have any experience with similar projects or field applications? Please share any relevant information, thank you~
The physical property data of anthracene oil can be used as a reference for calculations.