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Incorporation of Microreactor Measurements into a Pilot‐Scale Phthalic Anhydride Reactor
A major obstacle in the development of industrial catalysts is the scalability of both catalyst performance and synthesis. While utilizing pilot‐scale test reactors allows for a direct transfer from the development stage to the application, it comes at the cost of flexibility. The amount of catalyst required in a pilot‐scale test reactor often surpasses the yields of novel synthesis procedures, requiring extensive scale‐up efforts. Here, pilot‐scale reactors are combined with small lab‐scale reactors, using the example of oxidation of o‐xylene to phthalic anhydride.
Incorporation of Microreactor Measurements into a Pilot‐Scale Phthalic Anhydride Reactor
A major obstacle in the development of industrial catalysts is the scalability of both catalyst performance and synthesis. While utilizing pilot‐scale test reactors allows for a direct transfer from the development stage to the application, it comes at the cost of flexibility. The amount of catalyst required in a pilot‐scale test reactor often surpasses the yields of novel synthesis procedures, requiring extensive scale‐up efforts. Here, pilot‐scale reactors are combined with small lab‐scale reactors, using the example of oxidation of o‐xylene to phthalic anhydride.
Incorporation of Microreactor Measurements into a Pilot‐Scale Phthalic Anhydride Reactor
Fischer, Nico (author) / Hubach, Patrick (author) / Woll, Christian (author)
Chemie Ingenieur Technik ; 87 ; 159-162
2015-02-01
4 pages
Article (Journal)
Electronic Resource
English
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