Respuesta :
Answer:
[tex]s_1=7.1292\frac{kJ}{kg*K}[/tex], nevertheless, the outlet quality is not possible due to negative entropy generation.
Explanation:
Hello,
In this case, with the given conditions, it is possible to extract the entropy at the turbine inlet from the steam overheated tables at 20 bar and 400 °C, realizing that 20 bar equals 2 MPa. In such a way, the entropy at those conditions is:
[tex]s_1=7.1292\frac{kJ}{kg*K}[/tex]
Moreover, we should prove that the 98% quality is possible in terms of the entropy generation which MUST be positive based on the entropy balance:
[tex]s_{gen}=s_2-s_1[/tex]
Thus, we also compute the entropy at the outlet, looking for liquid-vapor water at 1.5 bar with the given quality:
[tex]s_2=1.3548\frac{kJ}{kg*K}+0.98*5.9187\frac{kJ}{kg*K}\\s_2=7.155\frac{kJ}{kg*K}[/tex]
Hence the entropy generation turns out:
[tex]s_{gen}=s_2-s_1=7.155-7.1292=-0.0259\frac{kJ}{kg*K}[/tex]
Finally, such value means that the outlet quality is not thermodynamically possible.
Regards.
Following are the calculation of the entropy at the turbine inlet:
Inlet pressure, [tex]P_1 =\overline{20}\\\\[/tex]
Inlet temperature, [tex]T_1 =400^{\circ} \ C\\\\[/tex]
Exit pressure, [tex]P_2 =\overline{1.5}\\\\[/tex]
Using the values of the steam table:
[tex]\to P_1 = \overline{20} \\\\ \to T_1= 400^{\circ}\ C\\\\\to s_1=7.127 \ \frac{KJ}{kg \ K}\\\\[/tex]
Also at
[tex]\to P_2= \overline{1.5} \\\\\to S_{f2} =1.4336 \ \frac{kJ}{kg K}\\\\\to S_{fg2} =5.7898 \ \frac{kJ}{kg K}\\\\[/tex]
Considering the "x" that represents the quality of steam in a turbine for an isentropic operation.
[tex]\to s_1=s_2\\\\\to s_1=s_{f2}+xs_{fg2}\\\\\to x=\frac{s_1-s_{f2}}{s_{fg2}}\\\\[/tex]
[tex]= \frac{7.127-1.4336}{5.7898}\\\\=0.9833\\\\= 98.3\%\\\\[/tex]
Therefore, there is NO, the steam's quality is not [tex]\bold{98\%}[/tex], and the steam has a quality of [tex]\bold{x=98.33\%}[/tex].
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