It is said that screw expanders are good because they can operate at wet (x
Please also look at "Effect of R245fa quality X on the generated power from an ORC-system using a Twin Screw Expander", which I uploaded as a contribution to this question.
Another question: How do you take DIFFUSION into consideration when you calculate performance of expanders having steam quality x
This might be something also.
In this data set the steam mass flow is constant.
As you can see the Power decreases when the x-value decreases.
These calculations are made with built-in volume ratio =1, which means that flashing/condensation takes place after the opening of the control volume.
What is the opinion for using a Turbine instead of a Twin Screw Expander in the case where expansion takes place in the superheated region? For me it seems that the turbine is a better...
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For example a mixture of oil/air at Pin=10 bar Pout =1 bar.
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If you run a screw expander with steam quality x
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