Control of parallel dry methane and steam methane reforming processes for Fischer-Tropsch syngas
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文摘

Plantwide control structure developed for two units operating in parallel to produce syngas.

Each unit has two fresh feed streams with total methane split to achieve desired combined H2/CO ratio of product syngas.

High-temperature reactors heated by combustion of fuel are effectively modeled using plug-flow tubular reactor models with constant heat flux.

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