Thanks, David, TehMightyEngineer, Mike and Buggar.
Your responses were not surprising, and yet very helpful.
If there are any other suggestions you may have for how to earn a living during those "between jobs" periods, I would be immensely grateful.
Otherwise, I would consider the matter...
Hello. Greetings to All.
When I consider all of the hundreds of spreadsheets and other calculations that I have created, I would very much like to standardize them, or otherwise develop them, and sell them online.
I ask all of you: Have you heard of such an endeavor or if you have, do you...
Thanks, TD2K.
The Varec 221P will open at ~ 15.0 psia at ~650,000 scfh blow by rate.
However, in relation to vast pressure difference between the pipe exit and tank pressures, I suspect that expansion waves will occur near the pipe exit and give significant rise to the local pressure near the...
Hello to All.
An abnormal condition causes natural gas to blow through a liquid level control valve [LCV] to an atmospheric tank [p design is 15.7 psia]. I can show that the tank's relief valve has sufficient capacity to handle the gas flow rate, but I do not know how to determine the maximum...
Hello to All!
I am looking for textbooks, short courses, or other means to learn the fundamentals of Chemical Engineering [without going back to University].
As a mechanical engineer, I have found my niche to be fluid mechanics, thermo, and heat transfer. However, I often need to push the...
