among those points are points corresponding to T=400F and p=500lbf/in2. Learn how to connect the points by solid lines in Excel, but make sure the points are still visible. Example: 2. Add to the p-v diagram a function T(v)=400F that includes 3 branches: one in the liquid phase (Table A-5E), one in the two-phase mixture (inside the vapor dome, Table 2E ), and one in the vapor phase (Table A-4E). Make sure that the data points are visible and connected by a solid line. It is enough to use 2 points per branch in the liquid and liquid-vapor mixture phases, and 3- 4 points in the vapor phase. 3. Add to the T-v diagram a function p(v)=500lbf/in2 that includes 3 branches: one in the liquid phase (Table A-5E), one in the two-phase mixture (inside the vapor dome, Table 3E ), and one in the vapor phase (Table A-4E). Make sure that the data points are visible and connected by a solid line. It is enough to use 2 points per branch in the liquid and liquid-vapor mixture phases, and 3-4 points in the vapor phase. Notice that lines of constant T and p may grow very rapidly in the liquid phase. To improve the plot quality in the liquid phase, apply the log scale to both axes..

1. among those points are points corresponding to T=400F and p=500lbf/in2. Learn how to
connect the points by solid lines in Excel, but make sure the points are still visible. Example: 2.
Add to the p-v diagram a function T(v)=400F that includes 3 branches: one in the liquid phase
(Table A-5E), one in the two-phase mixture (inside the vapor dome, Table 2E ), and one in the
vapor phase (Table A-4E). Make sure that the data points are visible and connected by a solid
line. It is enough to use 2 points per branch in the liquid and liquid-vapor mixture phases, and 3-
4 points in the vapor phase. 3. Add to the T-v diagram a function p(v)=500lbf/in2 that includes 3
branches: one in the liquid phase (Table A-5E), one in the two-phase mixture (inside the vapor
dome, Table 3E ), and one in the vapor phase (Table A-4E). Make sure that the data points are
visible and connected by a solid line. It is enough to use 2 points per branch in the liquid and
liquid-vapor mixture phases, and 3-4 points in the vapor phase. Notice that lines of constant T
and p may grow very rapidly in the liquid phase. To improve the plot quality in the liquid phase,
apply the log scale to both axes.