I have a question about carburetor calculation and would like to ask a fellow car enthusiast
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I am currently trying to determine whether an increased vaporization capacity of the chloromethane vaporizer will be sufficient to meet the load requirements. The heating medium used is 4 kilograms of steam. The outlet temperature of the existing vaporizer is higher than the saturation temperature. I am using the kettle reboiler model to calculate the heat transfer area for boiling, but I’m not sure whether it’s necessary to calculate separately the heat transfer area for the superheated steam after vaporization. In other words, the total heat transfer area should equal the boiling heat transfer area plus the superheating heat transfer area. I would appreciate any advice from those with experience in this field
It is not carried out in phases; it should take place simultaneously within the heat exchanger.