The issue of direct supply of reprocessing materials
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Currently, naphtha S, N, and CL are used in many processes, such as catalytic charring cracking and wax oil hydrocracking; however, steam may be introduced into the bottom of the stripping tower, and this steam can cause the water content in the naphtha to exceed acceptable levels. Refineries use various methods to improve the reformation of naphtha obtained through catalytic charring cracking or hydrocracking. Please share your thoughts!
Medium-pressure hydrogenation flows into the reformer after passing through a molecular sieve dehydration tank
I’m supplying this hydrogenated heavy naphtha directly; it just has a bit too much water, but all other parameters are normal
Direct supply of cracked barite – no major issues
What is the general water content when you supply it directly?
We are going to the tank area. I would like to ask what the advantages are of direct supply? In addition to saving one storage tank
Hydrocracked naphtha is essentially free of water