Article ID Journal Published Year Pages File Type
645779 Applied Thermal Engineering 2014 10 Pages PDF
Abstract

•Diffusion coefficients are needed for predicting evaporation losses in fuel systems.•Nine equations were applied to the binary gaseous alcohol-air mixtures.•Experimental results were obtained at temperatures 25–50 °C for C1 to C5 alcohols.•Results were compared with data from literature and from equations predictions.•A new four-parameter equation is proposed showing good agreement with experiments.

Alcohols (not only ethanol but also methanol, propanol, butanol and pentanol) are receiving increasing attention as components for blending with conventional fuels (gasoline and diesel or biodiesel fuels) because they can be an efficient means to increase the renewable fraction of fuels and to reduce emissions. Mathematical models for predicting evaporation losses in storage and fuel distribution systems require information about diffusion coefficients, among other characteristic parameters of the alcohols and of the alcohol-air gaseous mixtures. Nine equations in the literature have been described and applied to the binary gaseous mixtures alcohol-air to estimate the diffusion coefficient. Other equations were discarded because they are not applicable to alcohol-air systems. The resulting diffusion coefficients were plotted against temperature for the five mentioned alcohols, and the results were compared with experimental data obtained from measurements with capillary glass tubes immersed in a controlled temperature glycerine bath at 25 °C, 30 °C, 40 °C and 50 °C. The diffusion coefficients were determined from the variation of the height of the liquid column and the vapour pressure. From comparing the standard deviations with respect to the experimental data, although the best fit for all alcohols was reached with the Arnold equation (0.0247 cm2/s), it was concluded that there is not a unique optimal formula for all alcohols. Additionally, all the revised equations underestimate the effect of temperature for methanol, ethanol and propanol. Specific logarithmic equations were proposed in this work for estimating the diffusion coefficient for each alcohol, and finally, a four-parameter equation was also proposed for the five alcohols studied, which provided excellent agreement (standard deviation 0.0045 cm2/s).

Related Topics
Physical Sciences and Engineering Chemical Engineering Fluid Flow and Transfer Processes
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