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The relations between methane conversion, gas composition and oxygen partial pressure were also used to formulate the oxygen balance in mixed conducting membrane reactors, with tubular reactor and continuous stirred tank reactor (CSTR) configurations.
The values of oxygen partial pressure required to attain the highest yield of CO and H2 were also used to estimate the stability requirements to be met by mixed conducting membrane materials.
Thermodynamic data have been used to predict the dependence of methane conversion on temperature and oxygen partial pressure in mixed conducting membrane reactors, and the corresponding fractions of water vapor, H2, CO and CO2.
This paper investigates the transient behaviour of an oxygen mixed conducting membrane (OMCM -based gas turbine (GT) pOMCM -based
In the first part of this paper we present a detailed model of an oxygen mixed conducting membrane (OMCM) monolith for air separation.
On this basis, a number of interesting findings were obtained: i) the mixed conducting membrane did not cause any short circuit; on the contrary, the cell reached a decent open circuit voltage (OCV) of ∼1.0 V.
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Oxygen mixed conducting membranes (OMCM) that separate oxygen from air can be used to develop oxy-combustion concepts to capture carbon dioxide with a small energy penalty.
They are also still attractive as oxygen distributors for the partial oxidation of long chain alkanes, although dense mixed conducting membranes are now on the way to be commercialized for methane involving reactions.
The initiation of oxygen permeation and POM were studied in mixed conducting ceramic membrane reactors.
This paper reports the application of mixed conducting perovskite membranes for simultaneous in situ O2 separation and catalytic oxidation of ammonia to nitric oxide.
In this work, we report the silver doping as a novel strategy for developing single-phase mixed conducting ceramic membranes with perovskite-type structure for the efficient oxygen separation from air.
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