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Membrane reactors for selective oxidation of methane to higher hydrocarbons were designed and successively operated.
This report describes evaluation studies on processes that directly convert methane to higher hydrocarbons and oxygenates.
The catalytic oxidative coupling of methane to higher hydrocarbons (OCM) as an alternative route to ethylene or liquid fuels obtained much attention.
This paper presents new conversion method of methane to higher hydrocarbon fuels such as methyl alcohol (methanol), formaldehyde, using pulsed discharge plasma under room temperature and atmospheric pressure.
A comprehensive reactor model of the oxidative coupling of methane to higher hydrocarbons (OCM) in a fluidized-bed reactor was developed.
Conversion of methane to higher hydrocarbons, polycyclic aromatic hydrocarbons (PAHs), and soot was investigated under fuel-rich conditions in a laminar flow reactor.
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Microbial conversion of methane to high-value bio-based fuels, chemicals, and materials offers a path to mitigate GHG emissions and valorize this abundant-yet -underutilized carbon source.
Selectivity for methane conversion to higher hydrocarbons rises to over 80% as reactor temperature is raised to about 800°C over these catalysts when oxygen/methane in the feed is limited.
In this paper, we study single-step natural gas conversion technologies that directly convert methane to olefins and higher hydrocarbons.
The recent literature on the direct conversion of methane to oxygenates and higher hydrocarbons is reviewed, with particular attention on the production of methanol and ethene.
The achieved gas permeability of 2.25×10−15 m2 for a 0.4 mm thick support will not limit the gas transport for oxygen production but in partial oxidation of methane to syngas at higher oxygen fluxes.
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