Urgent issues in the dual-high-pressure dual-tower process of straight-chain hydrocarbon hydrogenation units
Thread Content
I would like to ask those experienced members of the forum who have worked with units for the hydrogenation of straight-run diesel (70% straight-run diesel and 30% coker diesel) what kind of problems they have encountered during operation, or whether issues arose due to improper design that affected the normal functioning of the units. Regarding the optimization of the design and operation of this unit, which features two high-pressure sections (cold and hot high-pressure sections) as well as two towers (hydrogen sulfide stripping tower and distillation tower), I would appreciate it if everyone could share their insights. I have no experience working with this type of unit, so I hope you can offer me some guidance. Thank you all! ! ! :handshake
I work on these types of devices; this design is quite reasonable, it’s easy to operate and the product is of good quality. There’s nothing wrong with it. If you have any problems, feel free to post them and I’ll reply