How can we make a duhring plot in EES?

Sometimes when I run parametric table of EES (sweep a variable) I have get unstable answer at some rages.

For example for 0, 1, 2, 3 I get 10, 0.005, 9.5, 0.00000014

But when I don't use parametric table and by running them singularly in the main window of EES with F5 key, I get 10, 9.7, 9.5, 9.3 for 0, 1, 2, 3

What's the problem?

I have reduced convergence criteria but the problem is not solved...

For example, I attached a photo. Starting and ending range of the variable are the same, but the results are not. The marked result is the true result.

I have a very basic idea about this topic and thus I want to know books or journals I should refer to enhance my knowledge. I would also like to know the latest research topics under this topic.

EDIT: I want to learn about thermal management in electronic equipment.

Thank you in advance!

The water extract composition is considered known. How? The extract is sent to throttle valve. 

I use EES software to simulate an absorption refrigerator. This machine is composed of several elements, absorber, generator, condenser, evaporator, expansion valves and heat exchangers. I tried two code structuring strategies: all equations placed in the main program, a subprogram for each item called from the main program. According to simulations I performed the simulation time is substantially shorter and the convergence is improved by using the structure with only a main program. Can you explain me why this structure is more efficient and if I can get the same performances using subprograms?

I am looking for a formula to calculate specific temperature drop in duct based on airflow, knowing the specific power loss, airflow, thermal properties of the duct, and air temperatures. The goal is to be able to produce the graph attached.

Real heat transfer coefficient  h during nucleate boiling process means  a ratio     h=q/(T-Ts).  Effective heat transfer coefficient is calculated as h = q/(T-Tm). Where q is heat flux density; Ts is saturation temperature; Tm is medium temperature. A temperature difference T-Ts  is responsible for bubble growth during boiling and in this case HTC h is a function of T-Ts .  Difference T-Tm >>T-Ts and  it can differ more than 10 times. It means that effective heat transfer coefficient (HTC) is 10 time less as compared with the real HTC. What do you think about It?

How to do geothermal power plant optimization by using EES software with turbine and condenser pressure parameters