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The comparison of hydrogen storage behaviors between the reactors incorporating the traditional straight pipe and new helical coil heat exchangers is firstly conducted based on the numerical simulation.
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Our buses then drove between the reactors and the sea.
In between the reactors, there is a storage container (vessel), and the vessel is attached to counterflow heat exchangers between ingoing and outgoing reactors.
Tepco has injected chemicals into the ground meant to harden and form a wall between the reactors and the sea.
Thermal coupling between combustion and reforming of ethanol is plausible and an adequate behavior of the reactor in terms of hydrogen yield and conversion of ethanol is predicted.
The growth kinetics follows the simple Monod equation, The flow behavior in the reactor is assumed to be completely mixed, The reactor is operating under steady state, and.
Also, the much larger size of a commercial-scale fermentor causes significantly different fluid dynamic behavior in the reactor.
Unfortunately, the enzyme kinetic constants determined for isolated PEDH cannot be directly applied to describe the behavior of the reactor system.
The distance between the reactor and lamp is 8.5 cm.
In the boiling water reactor, a direct communication exists between the reactor and the turbine.
The distance between the reactor and lamp housing is 8.5 cm.
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