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HO2 and CH3 are major intermediate species presented during the oxidation of natural gas at intermediate temperatures and high pressures.
The parallel development of hydrocarbon reforming technology has also stimulated interest in IT-SOFC systems as syngas can now be effectively produced from natural gas at intermediate temperatures.
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This work reports on the investigation of CO2 selective membranes for pre-combustion and post- combustion processes, in which CO2 is extracted from multi-component gas streams at intermediate temperature (400 °C600 °C).
They operate efficiently at intermediate temperatures (550 650 °C) using a variety of light hydrocarbon fuels such as natural gas.
At intermediate temperatures of ∼1123 1250 K, [NOx] was higher and reached a maximum of ∼22 p.p.m. in the gases leaving the bed.
At intermediate temperatures, dynamic strain ageing effects occur.
Therefore, the premixed methane oxidation is initiated at intermediate temperatures.
At intermediate temperatures, the formation of hydrocarbon and alcohol intermediates slows the oxidation process relative to the low temperatures.
A CGO electrolyte was used due to the higher ionic conductivity at intermediate temperatures [29].
Compared to H2O diffusion in rhyolite, diffusivity in dacite is lower at intermediate temperatures but higher at superliquidus temperatures.
However, this phenomenon shows interesting behavior at intermediate temperature range.
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