4.3 Article

Evaluation of models for predicting relative viscosity of ultrasound-assisted synthetic water-in-oil emulsions of Brazilian crude oil

Journal

JOURNAL OF DISPERSION SCIENCE AND TECHNOLOGY
Volume 42, Issue 1, Pages 119-131

Publisher

TAYLOR & FRANCIS INC
DOI: 10.1080/01932691.2019.1664910

Keywords

Water-in-oil-emulsions; ultrasound-assisted emulsification; crude oil rheology; Farah model; Ronningsen model

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The study focused on the dynamic viscosity and rheological properties of water-in-oil emulsions, highlighting the significant influence of water volumetric fraction on the rheological behavior of the emulsions. Additionally, it was found that viscosity increased as the water volumetric fraction increased, while temperature increase led to a decrease in viscosity.
Emulsions of water-in-oil (W/O) is a very common occurrence in the oil and gas industries. The viscosity and rheological properties of the emulsions are of great interest to the petroleum industry, especially during oil exploitation and transportation. In this study, emulsion dynamic viscosities were measured (20 degrees C-50 degrees C), and rheological profiles were modeled according to Ronningsen, ASTM D-341, Farah, and other viscosity models . Also, a methodology for producing water-in-oil emulsions using ultrasound energy was proposed, and the generated emulsion properties were compared with relevant literature. Emulsions were prepared with 22.3 degrees API crude oil without surfactants. A 400 W ultrasound generator was used for sonication at 24 kHz, and the effects of sonication time and ultrasound amplitude on dynamic viscosity and droplet size distribution were investigated. The emulsions generated by ultrasound sonication showed stability and homogeneity, and droplet size distribution of D-0.5=0.10 mu m and D-4.3=0.37 mu m. The rheological profiles strongly depended on emulsion viscosity and water volumetric fraction. The water volumetric fraction was shown to be the most important factor, the viscosity increased as volumetric fraction increase, while temperature increase led to a viscosity decrease. The experimental results were well fitted by the model proposed by Farah with a 5.5% error.

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