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If you use note 3 equation in API 581 and took steam ideal gas constant values from table 4.2 you will obtain a value of Cp equal to 4.2185E+14 Where R = 8.314 , so the value k will be 1.000000000000020 which is not applicable to be used in equation 3.6 or 3.7
Also the actual value of...
1.33 seems reasonable k for steam but I am talking about k that calculated as per API 581 , the problem coming from values Of ideal gas constants (A, B,C,D &E )in table 4.2 in API 581 , these values used in equation in note 3 .
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I faced a problem during the application of API 581-2016 edition and I hope you could help me in this issue.
I am trying to apply RBI for a steam vessel , when I chose the representative fluid as steam , no release rate was calculated , this is because of the huge value of Cp...
I faced a problem during the application of API 581-2016 edition and I hope you could help me in this issue.
I am trying to apply RBI for a steam vessel , when I chose the representative fluid as steam , no release rate was calculated , this is because of the huge value of Cp that was...
I faced a problem during the application of API 581-2016 edition and I hope you could help me in this issue.
I am trying to apply RBI for a steam vessel , when I chose the representative fluid as steam , no release rate was calculated , this is because of the huge value of Cp that was...