We are supplying this cheapish compressor to one of our customers. They are a small bakery and need a back up air system to run our liquid handling machinary when the compressor they share with the f

Can a Back Pressure valve be designed on a condensate return line to prevent flashing in the line. There is a hotwell downstream on the valve at 0 psig. The condensate is generated by 150# steam @ 360

I have to control the outlet temperature of natural gas process fluid, which flows in the tube side of a vertical beu HEX. At the shell side steam is condensates. By modulate steam mass flow with a t

When calculating heat loss through underground steam distribution piping, do I use sensible heating valve or total (sensible+latent) heating valve?

What will the resulting fluid properties be if, 1200kg/h SH steam at 0.8 bar(a) and 340 deg. C is allowed to flow into a exhuast steam duct kept at 0.8 bar(a), 93.5 deg. C (saturated temperature) by m