Hi
I want to ask, what is the criteria to say that a selected PSV is oversized ?
For instance, I have a calculated relief rate of 100%. When I calculate the orifice size I found that the orifice size is 1.877 in2 (larger than 1.838 in2 for K size but much lower than 2.853 in2 for L size)
If...
Hi, I'm currently working in a Gas Processing design and I'm a little bit confused in one subject.
So here is the case
I have two Feed Gas Scrubbers (upstream and downstream of Compressor). The Feed Gas is normally in 100% vapor form (no liquid flashing expected).
Bottom of these scrubbers...
Hi, my name is pine and I'm currently have assignment to create switching table for Dehydration using Mol Sieve.
Our client would like to have the unit able to operate in both 2x100% (1 operate, 1 regen, 1 standby) and 3x50% mode (2 operate at 50%, 1 regen)
My questions are :
1. Lets say that...
