How to choose the tray form of absorption tower?
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Hello fellow sea friends. I now want to design a gas-liquid absorption tower. After the gas-liquid reaction, a relatively viscous slurry material is generated. What kind of absorption tower should I choose and what kind of trays are better? Thank you everyone for participating in the discussion...
I think you can choose the petrofrac model because it is a strict model for simulating responsible gas-liquid fractionation operations in the petroleum refining industry. Typical operation packages include vacuum lube oil fractionators, delayed coking main fractionators, etc.
Brother upstairs, could you please give us a detailed introduction to your model? What is the scope of application? Sajia doesn’t understand.
The third floor probably talks about what kind of tower to choose during software simulation. I think the poster can try a packed tower. If it is sticky, I think there is no problem with a packed tower. For example, a vacuum tower is considered sticky, right? Isn’t packing also used in industry? The author can check the literature by himself, and see how people use trays for some viscous materials, such as heavy oil, lubricating oil, etc.
The key is that packed towers are easy to block, and the operating pressure difference of the tower is relatively large. I have doubts about bubble towers and the like, let alone packed towers.
It is prone to clogging, so you need to choose a tray type with strong anti-clogging ability.
Are there any better suggestions upstairs? What type of tray has the best resistance to blockage?