Risks of changing the batch reaction process in the reactor to a fixed-bed continuous reaction process
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There is a concern: currently, an intermittent reaction process is used in the reaction vessels, with liquid raw materials and solid powder catalysts. If we were to switch to a continuous fixed-bed reaction process, what risks might exist from a process perspective?
It mainly depends on the heat effect of the reaction; excessively high temperatures usually lead to a decrease in catalyst activity
There are many factors related to the resistance of liquid raw materials in a fixed-bed reactor, such as whether they will clog, their flowability, and so on