Hi. Great video, but my question is how does the psv compensate for the back pressure once the relief valve has popped open? Won't the back pressure and pressure in relieving line equalize?
Good afternoon, I'm currently starting my preparation for the FE Exam Chemical, I am a chemical Engineer graduated in Cuba, Do you have any advice for me, any study method or courses? Thank you very much
At 3:20, I inadvertently flipped the circulating cooling water and make-up cooling water conductivities. The cycle calculation should be circulating cooling water divided by the make-up cooling water.
Great video. Do you have any recommendations for proper study material? Any insight on problems that you practiced with? Level of difficulty compared to FE?
Great presentation Matt! -- and very helpful. If there is hydrocarbon leakage from the PSV's atmospheric vent would that indicate a bellows failure - perhaps due to a significant increase in header pressure? --David Ranum
Matt very simple explanation with your radio broadcaster voice very helpful info for instrument commodity guys. Keep it up the good work. ex-colleague from Alberta.
Very educational, I’ve crawled through a few towers during inspections, never thought about really putting much emphasis on the trays due to operations having control over that. I’ve seen missing tray valves and broken attachment welds as well. Maybe check out API 571 for more info over damage mechanisms. 👍🏼
Thanks Matt for the explanation. Is it necessary that letter of recommendation comes from people from the same filed/major? I am a chemical engineer who worked with mechanical PEs mostly and can provide the letter from them.