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The customer for both reactors: Constellation Energy.
The test was applied in all cycles for both reactors.
The reaction time (RT) was maintained at 23 h for both reactors.
The ratio of NO2 −/(NO3 − + NO2 −) was most of the time more than 0.9 for both reactors.
At least elements to calculate the cost of the plant, for both reactors are given.
Results show that the models considered for both reactors predict the experimental values well.
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For both the reactors, reactor heat is removed passively by natural circulation of the coolant.
The minimal medium used for both reactor and 10 ml batch fermentations was described by Jensen et al. ([2012]).
VOC combustion is a demanding process for both reactor and catalyst design.
A quasi-continuous production of CO is demonstrated for both reactor designs.
For both reactor concepts, the heat and mass transfer inside the reactor or the material store respectively, have been analyzed in detail by means of numerical simulations.
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CEO of Professional Science Editing for Scientists @ prosciediting.com