Phase equilibria of ethanol fuel blends

French, Raymond N.; Malone, Patrick V.

doi:10.1016/j.fluid.2004.09.012

Cited by 89 publications

(67 citation statements)

References 56 publications

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“…The water solubility of DMF is less than one part in one hundred, whereas ethanol is completely miscible with water in any proportions. This may make it possible to blend DMF with gasoline at the refinery instead of blending at terminals outside the refinery [22] and might make it possible to send gasoline containing DMF through pipelines.…”

Section: Fuel Propertiesmentioning

confidence: 99%

Study of the knocking propensity of 2,5-dimethylfuran–gasoline and ethanol–gasoline blends

Rothamer

Jennings

2012

Fuel

105

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Section: Fuel Propertiesmentioning

confidence: 99%

Study of the knocking propensity of 2,5-dimethylfuran–gasoline and ethanol–gasoline blends

Rothamer

Jennings

2012

Fuel

105

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“…Consequently, ethanol is now for example in the USA added to gasoline (gasohol). As discussed by French and Malone [1], 0378 the addition of ethanol to gasoline affects the production, storage, distribution, and use of the obtained gasoline, because the physical properties are changed and complex thermodynamic behaviors are encountered.…”

Section: Introductionmentioning

confidence: 99%

Comparative experimental and modeling studies of the viscosity behavior of ethanol+C7 hydrocarbon mixtures versus pressure and temperature

Zéberg-Mikkelsen

Watson

Baylaucq

et al. 2006

Fluid Phase Equilibria

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“…As a consequence, ethanol is now, e.g., in the U.S.A., added to gasoline (gasohol) in proportions up to 10 vol.%. As discussed by French and Malone [1], the addition of ethanol to gasoline affects the production, storage, distribution, and use of the obtained gasoline, because the physical properties are changed and complex thermodynamic behaviors are encountered.…”

Section: Introductionmentioning

confidence: 99%

High-Pressure Viscosity Measurements for the Ethanol + Toluene Binary System

Zéberg-Mikkelsen¹,

Baylaucq²,

Watson³

et al. 2005

Int J Thermophys

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The viscosity of the ethanol + toluene binary system has been measured with a falling-body viscometer for seven compositions as well as for the pure ethanol in the temperature range from 293.15 to 353.15 K and up to 100 MPa with an experimental uncertainty of 2%. At 0.1 MPa the viscosity has been measured with a classical capillary viscometer (Ubbelohde) with an uncertainty of 1%. A total of 209 experimental measurements have been obtained for this binary system, which reveals a non-monotonic behavior of the viscosity as a function of the composition, with a minimum. The viscosity behavior of this binary system is interpreted as the result of changes in the free volume, and the breaking or weakening of hydrogen bonds. The excess activation energy for viscous flow of the mixtures is negative with a maximum absolute value of 335 J · mol −1 , indicating that this binary system is a very weakly interacting system showing a negative deviation from ideality. The viscosity of this binary system is represented by the Grunberg-Nissan and the Katti-Chaudhri mixing laws with an overall uncertainty of 12% and 8%, respectively. The viscosity of methanol (23 point) has also been measured in order to verify the calibration of the falling-body viscometer within the considered T, P range.

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Phase equilibria of ethanol fuel blends

Cited by 89 publications

References 56 publications

Study of the knocking propensity of 2,5-dimethylfuran–gasoline and ethanol–gasoline blends

Study of the knocking propensity of 2,5-dimethylfuran–gasoline and ethanol–gasoline blends

Comparative experimental and modeling studies of the viscosity behavior of ethanol+C7 hydrocarbon mixtures versus pressure and temperature

High-Pressure Viscosity Measurements for the Ethanol + Toluene Binary System

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