Water consumption for temperature and pressure reducers?
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How much water is required to reduce 3.5MPA steam to 2.0 MPA steam using a temperature and pressure reducer? How to calculate ASPEN?
3.5MPA steam, superheated steam? 2.0, saturated steam?
A flash module can be used to carry out a design-based solution~
Q1H1+Q2H2=Q3H3 Is 35 barg superheated steam? ? The pressure reduction process is also accompanied by a temperature difference; I won’t calculate this either, but it can be simulated using valves
If they are all saturated, very little water needs to be added. From the simulations, after depressurization of 3.0 MPaA saturated steam, the superheat is very small; taking heat losses into account, it is essentially at saturation. Use the flash module to adjust the make-up water volume so that the amount of water separated by the flash module equals 0