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Recent studies have identified uncertainties in fuel diffusion coefficients as a source of significant uncertainty in combustion modeling.
The results indicate that the simulations are sensitive to the transport parameters used to calculate fuel diffusion.
The lateral fuel diffusion rate decreased with the increase of sample width, streamwise location and flow velocity.
The reaction zone associated with the gradual fuel diffusion into the sweep side improves the membrane performance by maintaining a more uniform oxygen flux.
Data are presented to compare soot formation in both surrogate and practical fatty acid methyl ester biodiesel and petroleum fuel diffusion flames.
The B-number was width-independent for wider slabs but decreased with the decreasing sample width for narrower slabs as a result of lateral fuel diffusion and heat loss.
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A numerical model with detailed gas-phase chemistry and transport was used to predict homogeneous fuel conversion processes and to capture the important features (e.g., the location, temperature, thickness and structure of a flame) of laminar oxy-fuel diffusion flames stabilized on the sweep side of an oxygen permeable ion transport membrane (ITM).
Each chip has 300 μm thru holes for catalyst supporter and 400 μm thru holes for fuel-diffusion layer.
The membrane-electrode assemblies (MEA) consist of two identical polymer chips positioned on both sides of the proton exchange membrane, which play the roles of current collector, fuel-diffusion layer, and catalyst supporter.
When rapid vaporization leads to a kernel of high fuel vapor concentration, combustion may begin before the fuel diffuses in the air coflow, in a layer of intense reaction that locally depletes the oxygen and leaves behind a region of high temperature fuel vapor surrounded by a diffusion flame.
Developing a robust, intelligent design tool for multivariate optimization of multi-phase transport in fuel cell diffusion media (DM) is of utmost importance to develop advanced DM materials.
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