Recent content by hogdawg23

The forced event is not possible at the site, there is a lot of machines that procees spans 2-10 days and the schedules are staggered all on top of each other. but I feel like I'm at a good place to take some readings and finish the calc. I will post update post gauge readings. Thank you so much!

I can hook a pressure gauge to the valve we are going to build off of. Once I have that pressure at point A, can I assume the rest of my calculations are carried out properly?

Its nitrogen, if I said argon that was a mistake, sorry. also the fluid is being consumed and vented to atmosphere not returned or reclaimed

pipe velocity for comparion, I'm using the air range of 10-30 m/s as my target because air is mostly nitrogenhttps://files.engineering.com/getfile.aspx?folder=86118a8e-504f-40f9-a432-3ac232eb879a&file=Screenshot_2021-11-03_090250.png

Sketchhttps://files.engineering.com/getfile.aspx?folder=f2413645-ce49-4c41-9132-f36517e99631&file=sketch2.jpg

OK so here is my drawing and a little explanation of what I've done so farhttps://files.engineering.com/getfile.aspx?folder=635010bc-8744-4196-a5e2-9a9354a32fb3&file=sketch1.jpg

Thank you, alchemon & pierreick. I will upload a sketch when I get home in about an hour.

I am an intern right now and took my fluids course last quarter (be kind, or at least helpful please). I am trying to size the diameter of the new pipe being looped into a room to supply argon to 8 different machines. I know each machines flowrate and pressure used. (example: 4 of the machines...