Having been challenged by the client regarding tank spacing in bunded areas it would be useful for me to be able to calculate the maximum distance a jet of fluid could move horizontally from a punctured tank before hitting the ground. I am trying to keep this simple and generic, but lets assume...
Would anyone be able to provide me with a copy of an article that appeared in Chemical Engineer magazine that was published way back in nov (7th) 1977? The article was probably called "Arrangements for process and storage vessels" and was part 5 of the CE refresher on plant layout.
If asked to support vertical pipes of the order 3" to 6" with a horizontal run before and after were would you initially expect to place the pipe supports and guides. What are the major do's and dont's. Lets assume the pipes are inside the building, are non critical but expansion needs...