Q3. x=4 For the design of an industrial reactor, determine the molar volume of n-butane at 510 K and 266X kPa by each of the following: a) The ideal gas equation b) The generalized compressibility...


Q3.<br>x=4<br>For the design of an industrial reactor, determine the molar volume of n-butane at 510 K and<br>266X kPa by each of the following:<br>a) The ideal gas equation<br>b) The generalized compressibility factor equation (Pitzer Compressibility)<br>ВР<br>c) Equation Z = 1+<br>= 1+ B with the generalized correlation for B= B° + @B'<br>RT<br>RT<br>B<br>d) Virial Equation in form by Vi+1= (1++<br>with Virial Coefficients<br>P<br>B = -28X cm/ mol and C = -30,00X cm/ mol ( three iterations enough)<br>e) State the reasons for the difference in the values predicated by four methods.<br>Note: Use the Lee Kesler generalized correlation table given in Data sheet and Properities of<br>Pure Species Table in Data Sheet to get the required values for part b).<br>

Extracted text: Q3. x=4 For the design of an industrial reactor, determine the molar volume of n-butane at 510 K and 266X kPa by each of the following: a) The ideal gas equation b) The generalized compressibility factor equation (Pitzer Compressibility) ВР c) Equation Z = 1+ = 1+ B with the generalized correlation for B= B° + @B' RT RT B d) Virial Equation in form by Vi+1= (1++ with Virial Coefficients P B = -28X cm/ mol and C = -30,00X cm/ mol ( three iterations enough) e) State the reasons for the difference in the values predicated by four methods. Note: Use the Lee Kesler generalized correlation table given in Data sheet and Properities of Pure Species Table in Data Sheet to get the required values for part b).

Jun 09, 2022
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