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Methane was used as a carbon source, and nanostructural growth was afforded at 1000 °C.
The HGL surfaces were created using the same process as used for the CNWs, to maintain the chemical composition; however, a lower relative concentration of methane was used.
Combined CO2 reforming and partial oxidation of methane was used to produce synthesis gas over the Pt/ZrO2 catalyst.
Methane was used as a nonreactive tracer, and trichloroethene, benzene and toluene were used as reactive tracers.
The experimental pressure and temperature were varied from 6.9 to 69 bar (methane was used as make-up gas) and from 10to2525 °C respectively.
The present work presents a phase equilibrium scheme upon which heavy oil swelling and light crude vaporization were found when carbon dioxide (or methane) was used as advancing gas.
Similar(46)
'Methane' is used throughout to illustrate relationships for simplicity.
Steam reforming, autothermal reforming, and partial oxidation of methane are used to reform methane to synthesis gas [5, 6, 7].
When high consumption peaks appear, methane is used to produce electricity.
As oxidant various oxygen nitrogen mixtures and as fuel methane were used.
The reactor works with Ni-based oxygen carriers, methane is used as fuel and continuous cyclic operations are simulated.
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