Hi all
In a natural gas power plant, I am in charge of installing a turbo-expander in our process, so we can recover the expansion energy to produce electricity.
The natural gas comes with a pressure of 64 bar and a temperature of 27 ° C, the flow is around 64000 m3/h, it is treated in a heating/expansion station in order to achieve at the turbine inlet, a pressure of 28 bar and a temperature of 28 ° C. The idea is to remove this expansion technique (by using only reducing pressure valves), and replace them with a turbo-expander connected to a generator to recover the expansion energy.
However, since the inlet and the outlet temperature are so close, my concern is there any manufacturer can help me on this issue, do you think that design change is doable? We can also invest in a preheating station upstream/downstream the turbo expander, but it should be sensitive as an investment.
Thank you for your support.