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Forced unsteady-state operation of fixed bed catalytic reactor by periodical flow reversal is considered.
This problem has attracted significant attention with regard to operation of fixed and fluidized beds.
For the design and operation of fixed bed gasifiers the understanding of the occurring physicochemical phenomena is essential.
An experimental set-up is presented, which allows cycling of the feed for transient operation of fixed bed microreactors at frequencies up to 10 Hz.
Safe and reliable design and operation of fixed and floating marine structures often located in remote and hostile environments is challenging.
Distributed irrigation control (DIC) for site-specific management and/or operation of fixed irrigation systems is easier to install and maintain as compared to centralized irrigation control (CIC), but requires multiple controllers in the field.
Similar(53)
Bed pressure drop is an import parameter related to operation and performance of fixed bed gasifiers.
We show that through process optimization, the batch-operation of fixed bed CLC reactors is void of significant exhaust gas temperature fluctuations and can reach high thermal efficiencies with in-situ CO2 capture.
The present study reports the assembly and operation of a fixed bed using the microporous titanosilicate ETS-4 as sorbent.
Temperature variation in a cocurrent cooling medium and its influence on the operation of a fixed bed catalytic reactor of the type used for orthoxylen oxydation is examined.
Herein, a theory-based pseudo-homogeneous model to describe the operation of a fixed bed reactor for the ODHP to correspondence olefin over V2O5/γ-Al2O3 V2O5/γ-Al2O3 presented.
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