Problems encountered in HTRI calculations
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1. HTRI does not use process simulation software to import heat exchanger data; instead, it requires manual entry of the property data for all hot and cold streams. The heat load calculated in this way differs significantly from that obtained through PRO2 simulation – is this due to inconsistencies in the two approaches? 2. When using HTRI, instead of importing heat exchanger data through process simulation software, all property data of the hot and cold streams are entered manually. What should be taken into consideration? There seems to be something wrong with the calculation results. Are there any examples or something I can refer to?
Material properties are generally imported from simulation software, and it is important to check them after import