Hi, AMXX,
As Georgeverghese said, the problem is the pressure downstream of the check valve or SDV.
If the downstream of the compressor is a storage for emergency condition, it means the downstream pressure is always nearly the rated discharge pressure of compressor.
In similar application(the...
At first, for the reciprocating compressor, the discharge shutdown valve is not common item. We normally use non-return valve at discharge side. Sometimes we need a blowdown valve to release the pressure at discharge side.
And your question is when the SDV can be closed. Of course the SDV can...
I'm sorry that I don't understand "a gas feed"
You said that you wanted to know the liquid mass and the gas mass of the cooler outlet.
If you don't use HYSYS or similar software, you can calculate manually.
You know the components, percent of the gas. So you can calculate the partial pressure of...
Hi
At first, I believed the flow of Nitrogen should be 151.54 cfm or scfm, but not actual flow. The unit is the same as nitrogen generator.
You'd better to confirm the flowrate in cfm or scfm, the difference is 20℃ or 0℃. That 151.54 cfm =0.931*151.54 scfm
And the pressure should be 145psig...
I know that the Microsoft Project is a software for the project management. I had seen some project plan by Project.
For myself, I use Excel for the project management but need some more time.
